One-Flask Synthesis of Meso-Substituted Dipyrromethanes and

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固体超强酸催化α-蒎烯合成龙脑的研究

固体超强酸催化α-蒎烯合成龙脑的研究

固体超强酸催化α-蒎烯合成龙脑的研究下载提示:该文档是本店铺精心编制而成的,希望大家下载后,能够帮助大家解决实际问题。

文档下载后可定制修改,请根据实际需要进行调整和使用,谢谢!本店铺为大家提供各种类型的实用资料,如教育随笔、日记赏析、句子摘抄、古诗大全、经典美文、话题作文、工作总结、词语解析、文案摘录、其他资料等等,想了解不同资料格式和写法,敬请关注!Download tips: This document is carefully compiled by this editor. I hope that after you download it, it can help you solve practical problems. The document can be customized and modified after downloading, please adjust and use it according to actual needs, thank you! In addition, this shop provides you with various types of practical materials, such as educational essays, diary appreciation, sentence excerpts, ancient poems, classic articles, topic composition, work summary, word parsing, copy excerpts, other materials and so on, want to know different data formats and writing methods, please pay attention!固体超强酸催化α-蒎烯合成龙脑的研究引言龙脑是一种广泛应用于药物、香料和化妆品等领域的重要化合物,其合成一直是有机化学领域的研究热点之一。

石榴花水提物调节AHR

石榴花水提物调节AHR

叶雨萌,荣雨,李包娟,等. 石榴花水提物调节AHR/BNIP3改善糖尿病小鼠肝脏胰岛素信号[J]. 食品工业科技,2024,45(7):320−327. doi: 10.13386/j.issn1002-0306.2023100075YE Yumeng, RONG Yu, LI Baojuan, et al. Pomegranate Flower Water Extract Modulates AHR/BNIP3 to Improve Hepatic Insulin Signaling in Diabetic Mice[J]. Science and Technology of Food Industry, 2024, 45(7): 320−327. (in Chinese with English abstract). doi:10.13386/j.issn1002-0306.2023100075· 营养与保健 ·石榴花水提物调节AHR/BNIP3改善糖尿病小鼠肝脏胰岛素信号叶雨萌,荣 雨,李包娟,周克春,张䶮之*(新疆医科大学药学院,新疆乌鲁木齐 830000)摘 要:目的:探讨石榴花水提物(pomegranate flower water extract ,PFW )对2型糖尿病小鼠肝脏胰岛素信号传导的影响及机制。

方法:将C57BL/6J 随机分为正常组、模型组、二甲双胍组(Met )、石榴花水提物低剂量组(PFWL )和石榴花水提物高剂量组(PFWH )。

连续给药11周后,称小鼠体质量,检测空腹血糖(FBG )、胰岛素(INS )、甘油三酯(TG )和总胆固醇(TC )的含量,计算胰岛素抵抗指数(HOMA-IR );苏木素-伊红(HE )染色观察肝组织病理变化;Western blot 法检测肝组织中胰岛素受体底物1(IRS1)、p-IRS1(Ser307)、蛋白激酶B (AKT )、p-AKT (Ser473)、糖原合成酶激酶-3β(Gsk3β)、p-Gsk3β(S9)、芳香烃受体(AhR )、磷脂酰乙醇胺N-甲基转移酶(PEMT )、Bcl-2/腺病毒E1B-19kDa 相互作用蛋白3(BNIP3)蛋白表达。

药物化学专业英语词汇

药物化学专业英语词汇

medicinal药品,药物, 药的,药用的 be split into 分成,分为pharmaceutical 药学的,制药的,药品 starting materialsynthetic, 合成的,人造的,;synthetics化学合成品, synthesis合成(法), semisynthetic, synthesize, synthesesalkaloid 生物硷lead structure 先导结构 intermediate 中间体isolation 分离 natural source 天然来源enzyme 酶 heart glycoside 强心苷steroid 甾体 precursor 前体organ/target organ 靶器官 peptidehormone 激素 insulinpancreas vaccinepolysaccharide serumcholesterol 胆固醇 amino acidgelatine hydrolysis水解/hydrolysate水解产物/hydrolyze水解hydroxylation antibiotic 抗生素,抗菌的antibody interferon 干扰素fermentation 发酵 dextran 葡聚糖ーlactam natural producttherapy/therapeutic治疗的/therapeutic margincaffeine咖啡因 yeastmicrobiological mutantmicroorganism geneticmould high performancebacterial proteinmucous membranemetabolism新陈代谢 metabolite代谢物plasma 血浆 molecule /molecular weightfood additive organiclactic acid乳酸 citric acid 柠檬酸penicillin penicilliumtetracycline derivative衍生物contamination污染 sterile无菌的aerobic oxygencarbon dioxide carbohydratestarch saccharide/ polysaccharideglucose葡萄糖 nitrogenureaPhosphate optimalammonium sulfate ammoniaseparate filtrateabsorption extractionrecombinant encodepurification chromatographic procedurecalcium regiospecific reaction区域专一性反应stereospecific reaction 立体专一性反应isomerization/isomeric fructosecountless test diagnose diagnosticanalysis/ analyst/ analytical/ analyze protease Ingredient in combination withDigestion enymatic cleavageBy means of fumaric acidBindimmobilize racemate /racemicacetyl heterogeneouscatalysis mediumester synthetic routeregistration compoundOrganometallic pyridinearomatic toluenexylene phenolrecrystallization/crystal methanol/ethanolacetone ethyl acetatebenzene/ chlorobenzene diethyl ethersodium hydroxide hydrochloric acidsulfuric acid nitric acidacetic acid potassium carbonatechlorine/ chloride iodine/iodidefluorine/ fluoride bromine/bromideimpurity quality certificateGMP in large amount facilityInspection analogousHygienic be subjected toadminister/administration biologic responsebiologic membrane to a large extentpenetration spatial arrangement pharmacologic stereochemistrythree-dimensional structure lipidstructure-activity relationship stericcorrelation parameterpartition coefficient distribution fuction conformation extractionoptical isomerism/optical isomer enantiomorphic/ enantiomorph by no means tartaric acidManually magnificationdrug design polarized light dextrorotatory levorotatory Clokwise countclockwiseAntipode nonsuperimposable mirror imageCoincide with glyceraldehydeAbsolute literatureconfiguration crystallographyasymmetric center accessisomeric enantiomerdiastereoisomer atomic numberPrioritymagnification solubilityspatial sequencein vivo/in vitro receptorintravenous injection静脉注射 be susceptible to敏感的With respect to contractSubstrate epoxidationcarcinogen oxidation /oxidasepreparation predominantspecies complexdehydrase/dehydrogenase/decarboxylase/hydrolytic enzymes/isomerase/permease Choline one out of every ten 十分之一clinical 临床的 interactionexcrete/excretion inversionCoordination DelayEfficacy in place相称的,合适的entity drug developmentattrition toxicity/toxic/ toxicology/Anti-infectives Healthcarerepro-toxicology/genotoxicity drug candidateindication pharmacokinetics adverse profileformulary/formulation/formulor onsetdose/once a day dosing dosage/dosage form/overdosage regulatory interdependentsubacute亚急性的/chronic clinical/preclinicalvital optimum/ optimizeimpurity pilot plantcritical path criteriaupdate in paralleladequate stabilitypotency dermal cardiovascular 心血管的respiratory nervousconcurrently labelsynergies 协同作用 antagonizereversible/irreversible permissiblelifespan diseasetumour inhalercapsule rodentfoetal teratologyexposure patchset-up hazardOn a large scale shelf-lifetannin caffeineIn common vacuum fitrationhomogeneous gallic acidhydroxyl group esterifyphenolic precipitatenon-hydrolyzable carboxyl groupacidic calcium carbonatechloroform flavonoiddistillation sublimationsalicylic acid three neck round bottom flask separatory funnel steam bathdistillation flask beakerrinse ozoneice water bath condenserheparin digestionAside from fall intoProvide for as withCation compendialBatch –to batchcoagulation clotdecolorize anticoagulantprecipitation methodologyextraneous intestinalmucosa casingnitrate proteolyticdegrade/ degradation peroxideantithrombin thrombinplatelet aggregationintratracheal parenteraltopical comatoserelegate tabletsyrup suspensionemulsion versusbreakage leakagechip cracktaste masking expirationEven partially portableAdsorbent be free of / be free fromPreference 偏爱 otherwise ad. 另外,别样Burden 负担,负重, on standing 搁置microbiologic preservationdispense bioavailabilitysystemic effects self-administration of medicationmotion sickness medical emergencysterile ophthalmicirrigate mucousabradeViable 能生长发育的,生存的 Mucous menbraneBody compartment 体室,体腔 Body cavityCircumvent 围绕,包围,智胜,防止…发生,迂回 Exceptionally 特殊地,异常地Wound受伤 Vessel 管,脉管Specialized 专业的,专业性的 By far 非常,更加Monograph专题文章,专题论文 Stringent 严格的,严厉的Inclusive 范围广的 Gravimetric 重量分析法的Electrolytic 电介质的,电解的 Conductivity 电导率Conductance 电导,电导性 Immerse 将…浸入Electrode 电极 Specific 比的Resistance Withstand 经受得住Stress 恶劣的 Redictable 可预报的Reproducible 可重现的 Necessary 必然的Solubilizers 加溶剂 Chelate 螯合Excipient 赋型剂 Ingredient 配料Medicinal agent Dispense 使分散,使疏开,配方(药)Ingenuity 独创性,精明 FormulatorMeager 贫乏的 Continuance 持续pellet vehiclegravimetric instantaneousosmosis dissociatepyrogen antioxidantbuffer tonicityantifungal inhibitorantifoaming colligativeextemporaneous specificationpreparation optimizeaccumulation availabilitydelivery/ deliver peroralrelease sustaingastrointestinal predefinecavity marginionic/ion simulatedistinctly efficacypaddle intestinalinterval a steady-state blood or tissue level elimination blood vesselelectrode/electrolytic conductivity/conductanceresistanceexcipient thermalviable disintegrationresidence time accomplishmaximum/maximize potentiateprescribe uniformitycompliance specificationphysiologic agitationIn the face of 面临 Fluctuation 波动Deliberate 深思熟虑的 Peroral 经口的Depot 仓库 Repository 仓库Sustained release, Sustained action,prolonged action, controlled release,extended action, timed release,repository dosage forms Implicit固有的peak 峰 dumpmaintenance dose maintenance periodmethane, ethane, Propane, butane/tetrane, pentaneethylene, Propylene/propene, butylene, 1-pentenemethanol,ethanol/ethyl alcohol, Propanol/ propyl alcohol, Butanol/Butyl alcohol, 1-pentanolcalibrate asepticstoichiometry replenishmenttubular product yieldscirculate atomizediscrete reactantmaterial transfer regenerationreactant conversion deviate fromviscosityexothermic endothermicshort-circuiting 短路 laminar flowadiabatic radialproduct yields well-stirred batch reactorreactor configuration semibatch reactorcontinous-flow stirred-tank reactorback-mixing返混 cross-sectionpressue drop countercurrentpacked-column rate-limiting stepfluidized or fluid bed tubular reactortubular plug-flow reactor batch operationturbulent trickle bedmultiplicity in series 逐次的,串联的feed Cross-flow 错流,横向流Panel-bed 板式床 reaction driving froces 反应驱动力Chain-terminating Hydraulic 水力学的mechanical seal 机械密封 viscous 粘滞的Be prone to 倾向于, 易于中药traditional Chinese drug生药crude drug草药medicinal herb民族药ethnic drug地产药材native drug道地药材famous-region drug中成药Chinese patent medicine海洋生药学marine pharmacognosy药用植物学medicinal botany植物化学phytochemistry植物化学分类学plant chemotaxonomy生药拉丁名Latin name of crude drug学名scientific name来源source混淆品adulterant类同品allied drug伪品counterfeit drug代用品substitute掺伪adulteration天然产物natural product化学成分chemical constituent有效成分effective constituent主成分main constituent活性成分active constituent莽草酸途径shikimic acid pathway乙酸一丙二酸途径acetate-malonate pathway乙酸- 甲瓦龙酸途径acetate-mevalonate pathway 单糖monosaccharide戊糖pentose己精hexose庚糖heptose辛糖octose脱氧糖deoxysaccharide, deoxysugar呋喃糖furanose吡喃糖pyranose寡糖oligosaccharide二糖disaccharide三糖trisaccharide四糖tetrasaccharide五糖pentosacc haride多糖polysaccharide淀粉starch树胶gum果胶pectin半纤维素hemicellulose纤维素cellulose甲壳质chitin肝素heparin硫酸软骨素chondroitin sulfate玻璃酸hyaluronic acid直链淀粉amylose支链淀粉amylopectin糖原glycogen费林试验Fehling test苷glycoside糖杂体heteroside苷元aglycone苦杏仁酶emulsin氰苷cyanogenic glycoside, cyanogenetic glycoside 酚苷phenolic glycoside多酚polyphenol醛苷aldehyde glycoside醇苷alcoholic glycoside吲哚苷indole glycoside树脂醇苷resinol glycoside硫苷thioglycoside呫吨酮xanthone呫吨酮苷xanthonoid glycoside蒽醌anthraquinone蒽醌苷anthraquinone glycoside蒽酚anthranol氧化蒽酚oxanthranol蒽酮anthrone二蒽酮dianthrone羟基蒽醌hydroxyanthraquinone博恩特雷格反应Borntrager reaction 黄酮类flavonoid黄酮苷flavonoid glycoside黄酮flavone黄烷flavane黄酮醇flavonol黄烷酮flavanone黄烷酮醇flavanonol异黄酮isoflavone异黄烷酮isoflavanone新黄酮类neoflavonoid裂环烯醚萜苷secoiridoid glycoside 木脂体lignan木脂内酯lignanolide新木脂体neolignan木素lignin萜terpene萜类terpenoid半萜hemiterpene单萜monoterpene倍半萜sesquiterpene二萜diterpene三萜triterpene四萜tetraterpene多萜polyterpene齐墩果烷oleanane挥发油volatile oil精油essential oil鞣质tannin鞣酸tannic acid可水解鞣质hydrolysable tannin缩合鞣质condensed tannin鞣酐phlobaphene鞣花鞣质ellagitannin没食子鞣质gallotannin双缩脲反应biuret reaction脂肪fat脂肪油fatty oil去油de-fatting蜡wax环烯醚萜苷iridoid glycoside环烯醚萜iridoid裂环烯醚苷secoiridoid皂化saponification酸败rancidity饱和脂肪酸saturated fatty acid不饱和脂肪酸unsaturated fatty acid有机酸organic acid树脂resin油树脂oleoresin树胶树脂gum resin香树脂balsam香脂酸balsamic acid苷树脂glycosidal resin苦味素bitter principle色素pigment微量元素trace element生物碱alkaloid吖啶生物碱acridine alkaloid阿朴啡类生物碱aporphine alkaloid苄基异喹啉生物碱benzylisoquinoline alkaloid双苄基异喹啉生物碱bisbenzylisoquinoline alkaloid 双吲哚生物碱bisindole alkaloid咪唑生物碱imidazole alkaloid吲哚生物碱indole alkaloid吲哚联啶生物碱indolizidine alkaloid吲哚烷胺生物碱indolylalkylamine alkaloid异喹啉生物碱isoquinoline alkaloid大环生物碱macrocyclic alkaloid吗啡烷生物碱morphinane alkaloid羟吲哚生物碱oxindole alkaloid菲啶生物碱phenanthridine alkaloid苯烷胺生物碱phenylalkylamine alkaloid哌啶生物碱piperidine alkaloid嘌呤生物碱purine alkaloid吡啶生物碱pyridine alkaloid吡咯生物碱pyrrolidine alkaloid吡咯联啶生物碱pyrrolizidine alkaloid喹唑啉生物碱quinazoline alkaloid喹啉生物碱quinoline alkaloid喹啉联啶生物碱quinolizidine alkaloid甾体生物碱steroid alkaloid萜类生物碱terpenoid alkaloid四氢异喹啉生物碱tetrahydroisoquinoline alkaloid碘化汞钾试剂Mayer's reagent碘化铋钾试剂Dragendorff's reagent碘化钾碘试剂Wagner's reagent硅钨酸试剂Bertrand's reagent, silicotungstic acid reagent磷钼酸试剂Sonnenschein's reagent, phospho-molybdic acid reagent 苦味酸试剂Hager's reagent, picric acid reagent矾酸铵-浓硫酸试液Mandelin test solution钼酸铵-浓硫酸试液Frohde test solution甲醛-浓硫酸试液Marquis test solution莨菪烷tropane莨菪烷生物碱tropane alkaloid除虫菊素类pyrethroid-acetal 醛缩醇acetal- 乙酰acid 酸-al 醛alcohol 醇-aldehyde 醛alkali- 碱allyl 丙烯基alkoxy- 烷氧基-amide 酰胺amino- 氨基的-amidine 脒-amine 胺-ane 烷anhydride 酐anilino- 苯胺基aquo- 含水的-ase 酶-ate 含氧酸的盐、酯-atriyne 三炔azo- 偶氮benzene 苯bi- 在盐类前表示酸式盐bis- 双-borane 硼烷bromo- 溴butyl 丁基-carbinol 甲醇carbonyl 羰基-caboxylic acid 羧酸centi- 10-2chloro- 氯代cis- 顺式condensed 缩合的、冷凝的cyclo- 环deca- 十deci 10-1-dine 啶dodeca- 十二-ene 烯epi- 表epoxy- 环氧-ester 酯-ether 醚ethoxy- 乙氧基ethyl 乙基fluoro- 氟代-form 仿-glycol 二醇hemi- 半hendeca- 十一hepta- 七heptadeca- 十七hexa- 六hexadeca- 十六-hydrin 醇hydro- 氢或水hydroxyl 羟基hypo- 低级的,次-ic 酸的,高价金属-ide 无氧酸的盐,酰替…胺,酐-il 偶酰-imine 亚胺iodo- 碘代iso- 异,等,同-ite 亚酸盐keto- 酮ketone 酮-lactone 内酯mega- 106meta- 间,偏methoxy- 甲氧基methyl 甲基micro- 10-6milli- 10-3mono- ( mon-) 一,单nano- 10-9nitro- 硝基nitroso- 亚硝基nona- 九nonadeca- 十octa- 八octadeca- 十八-oic 酸的-ol 醇-one 酮ortho- 邻,正,原-ous 亚酸的,低价金属oxa- 氧杂-oxide 氧化合物-oxime 肟oxo- 酮oxy- 氧化-oyl 酰para- 对位,仲penta- 五pentadeca- 十五per- 高,过petro- 石油phenol 苯酚phenyl 苯基pico- 10-12poly- 聚,多quadri- 四quinque- 五semi- 半septi- 七sesqui 一个半sexi- 六sulfa- 磺胺sym- 对称syn- 顺式,同,共ter- 三tetra- 四tetradeca- 十四tetrakis- 四个thio- 硫代trans- 反式,超,跨-yl 基-ylene 撑(二价基,价在不同原子上)-yne 炔。

简明不对称合成天然蚂蚁生物碱(+)-Monomorine I

简明不对称合成天然蚂蚁生物碱(+)-Monomorine I

简明不对称合成天然蚂蚁生物碱( )+ Monomorine I
周德军,姚 倩,宋慧颖,李木子,梁晓晨,孟令普
(河南理工大学医学院,河南 焦作 ) 454000
摘要:运用 Martin 还原法高立体选择性构建顺式四氢吡咯,再经过非均相催化加氢脱保护,同时亲核闭环形 成 3,5二取代吲哚里西丁双环结构。通过此方法由已知 内γ 酰胺为原料 5 步合成天然蚂蚁生物碱(+) Monomorine I,总收率可达 56% ,产物与 5 位差向异构体的比大于 20 ∶ 1。 关键词:不对称合成;Dietary Hypothesis Martin 还原法;3,5二取代吲哚里西丁;(+)Monomorine I 中图分类号:O621 254 文献标志码:A
: ; ;, ;( ) Key words asymmetric synthesis Dietary Hypothesis Martin′s reduction method 3 5disubstituted indolizidine + monomorine I
在非洲马达加斯加岛、中南美亚马逊平原和 南亚印度尼西亚群岛等原始森林里栖息着很多颜 色新奇鲜艳的毒青蛙,至今已从它们的皮肤提取 液中分离出来 800 多种生物碱[1 。经 ] ~3 研究证 明,它们对人类中枢神经递质烟碱性乙酰胆碱受 体具有良好的亲和力,将来有可能成为一类治理 帕金森、老年痴呆症以及癫痫等中枢神经方面疾 病的有 效 药 物[4 ~ 6]。后 经 生 物 学 家 们 研 究,此 类 生物碱的真正生产者并不是毒青蛙而是它们的食 物如蚂蚁、甲虫、蜈蚣以及蜘蛛等[7]。毒青蛙体内
( , , , ) Medical School Henan Polytechnic University Jiaozuo 454000 China

三辛胺萃取分离苹果酸的特性

三辛胺萃取分离苹果酸的特性

万方数据
688
高 校
化 学 工
程 学 报
2002 年 12 月
O 的典型特征峰 度时 C
所以
TOA 与苹果酸间存在离子对成盐机制 同时 当苹果酸浓度不变时
而当 TOA 的浓度远大于苹果酸浓 羧酸盐峰几乎未变化
O 峰仍然存在
随 TOA 浓度的升高
说明苹果酸无法以离子对的形式结合第二个 TOA
100
80
x , mol ⋅L 图3 Fig.3
−1
x , mol ⋅L 图4 Fig.4
TOA 浓度对苹果酸萃取平衡的影响( 正辛醇为稀释剂) Dependence of extraction equilibrium on TOA concentration with n-octanol as diluent
第 16 卷第 6 期 2002 年 12 月
高 校 化 学 工 程 学 报 Journal of Chemical Engineering of Chinese Universities
No.6 Vol.16 Dec. 2002
文章编号: 1003-9015(2002)06-0686-05
三辛胺萃取分离苹果酸的特性
生物发酵液
的物理萃取法相比 多个官能团或自聚 复杂 点
由于有机溶质的 因此萃取机理十分
有关的研究报道也十分缺乏 探索萃合比的基本规律
利用其两个羧基的特 但大多
建立经验规则是十分有益的工作 丁二酸
[3]
二元有机酸的萃取行为曾有文献报道 为萃取分配系数( D) 的规律性研究 的萃合比进行了探讨 苹果酸( 羟基丁二酸
mol ⋅L−1 (TOA)
y, mol⋅L
y, mol⋅L−

marked manuscript

marked manuscript

Quality evaluation of Flos Lonicerae through a simultaneous determination of seven saponins by HPLC with ELSDXing-Yun Chai1, Song-Lin Li2, Ping Li1*1Key Laboratory of Modern Chinese Medicines and Department of Pharmacognosy, China Pharmaceutical University, Nanjing, 210009, People’s Republic of China2Institute of Nanjing Military Command for Drug Control, Nanjing, 210002, People’s Republic of China*Corresponding author: Ping LiKey Laboratory of Modern Chinese Medicines and Department of Pharmacognosy, China Pharmaceutical University, Nanjing 210009, People’s Republic of China.E-mail address: lipingli@Tel.: +86-25-8324-2299; 8539-1244; 135********Fax: +86-25-8532-2747AbstractA new HPLC coupled with evaporative light scattering detection (ELSD) method has been developed for the simultaneous quantitative determination of seven major saponins, namely macranthoidinB (1), macranthoidin A (2), dipsacoside B (3), hederagenin-28-O-β-D-glucopyranosyl(6→1)-O-β-D- glucopyranosyl ester (4), macranthoside B (5), macranthoside A (6), and hederagenin-3-O-α-L-arabinopyranosyl(2→1)-O-α-L-rhamnopyranoside (7)in Flos Lonicerae, a commonly used traditional Chinese medicine (TCM) herb.Simultaneous separation of these seven saponins was achieved on a C18 analytical column with a mixed mobile phase consisting of acetonitrile(A)-water(B)(29:71 v/v) acidified with 0.5% acetic acid. The elution was operated from keeping 29%A for 10min, then gradually to 54%B from 10 to 25 min on linear gradient, and then keep isocratic elution with 54%B from 25 to 30min.The drift tube temperature of ELSD was set at 106℃, and with the nitrogen flow-rate of 2.6 l/min. All calibration curves showed good linear regression (r2 0.9922) within test ranges. This method showed good reproducibility for the quantification of these seven saponins in Flos Lonicerae with intra- and inter-day variations of less than 3.0% and 6.0% respectively. The validated method was successfully applied to quantify seven saponins in five sources of Flos Lonicerae, which provides a new basis of overall assessment on quality of Flos Lonicerae.Keywords: HPLC-ELSD; Flos Lonicerae; Saponins; Quantification1. IntroductionFlos Lonicerae (Jinyinhua in Chinese), the dried buds of several species of the genus Lonicera (Caprifoliaceae), is a commonly used traditional Chinese medicine (TCM) herb. It has been used for centuries in TCM practice for the treatment of sores, carbuncles, furuncles, swelling and affections caused by exopathogenic wind-heat or epidemic febrile diseases at the early stage [1]. Though four species of Lonicera are documented as the sources of Flos Lonicerae in China Pharmacopeia (2000 edition), i.e. L. japonica, L. hypoglauca,L. daystyla and L. confusa, other species such as L. similes and L. macranthoides have also been used on the same purpose in some local areas in China [2]. So it is an important issue to comprehensively evaluate the different sources of Flos Lonicerae, so as to ensure the clinical efficacy of this Chinese herbal drug.Chemical and pharmacological investigations on Flos Lonicerae resulted in discovering several kinds of bioactive components, i.e. chlorogenic acid and its analogues, flavonoids, iridoid glucosides and triterpenoid saponins [3]. Previously, chlorogenic acid has been used as the chemical marker for the quality evaluation of Flos Lonicerae,owing to its antipyretic and antibiotic property as well as its high content in the herb. But this compound is not a characteristic component of Flos Lonicerae, as it has also been used as the chemical marker for other Chinese herbal drugs such as Flos Chrysanthemi and so on[4-5]. Moreover, chlorogenic acid alone could not be responsible for the overall pharmacological activities of Flos Lonicerae[6].On the other hand, many studies revealed that triterpenoidal saponins of Flos Lonicerae possess protection effects on hepatic injury caused by Acetaminophen, Cd, and CCl4, and conspicuous depressant effects on swelling of ear croton oil [7-11]. Therefore, saponins should also be considered as one of the markers for quality control of Flos Lonicerae. Consequently, determinations of all types of components such as chlorogenic acid, flavonoids, iridoid glucosides and triterpenoidal saponins in Flos Lonicerae could be a better strategy for the comprehensive quality evaluation of Flos Lonicerae.Recently an HPLC-ELSD method has been established in our laboratory for qualitative and quantitative determination of iridoid glucosides in Flos Lonicerae [12]. But no method was reported for the determination of triterpenoidal saponins in Flos Lonicera. As a series studies on the comprehensive evaluation of Flos Lonicera, we report here, for the first time, the development of an HPLC-ELSD method for simultaneous determination of seven triterpenoidal saponins in the Chinese herbal drug Flos Lonicerae, i.e.macranthoidin B (1), macranthoidin A (2), dipsacoside B (3), hederagenin-28-O-β-D-glucopyranosyl(6→1)-O-β-D- glucopyranosyl ester (4), macranthoside B (5), macranthoside A (6), and hederagenin-3-O-α-L-arabinopyranosyl(2→1)-O-α-L-rhamnopyranoside (7) (Fig. 1).2. Experimental2.1. Samples, chemicals and reagentsFive samples of Lonicera species,L. japonica from Mi county, HeNan province (LJ1999-07), L. hypoglauca from Jiujang county, JiangXi province (LH2001-06), L. similes from Fei county, ShanDong province (LS2001-07), L. confuse from Xupu county, HuNan province (LC2001-07), and L. macranthoides from Longhu county, HuNan province (LM2000-06) respectively, were collected in China. All samples were authenticated by Dr. Ping Li, professor of department of Pharmacognosy, China Pharmaceutical University, Nanjing, China. The voucher specimens were deposited in the department of Pharmacognosy, China Pharmaceutical University, Nanjing, China. Seven saponin reference compounds: macranthoidin B (1), macranthoidin A (2), dipsacoside B (3), hederagenin-28-O-β-D-glucopyranosyl(6→1)-O-β-D- glucopyranosyl ester (4), macranthoside B (5), macranthoside A (6), and hederagenin-3-O-α-L-arabinopyranosyl(2→1)-O-α-L-rhamnopyranoside (7) were isolated previously from the dried buds of L. confusa by repeated silica gel, sephadex LH-20 and Rp-18 silica gel column chromatography, their structures were elucidated by comparison of their spectral data (UV, IR, MS, 1H- NMR and 13C-NMR) with references [13-15]. The purity of these saponins were determined to be more than 98% by normalization of the peak areas detected by HPLC with ELSD, and showed very stable in methanol solution.HPLC-grade acetonitrile from Merck (Darmstadt, Germany), the deionized water from Robust (Guangzhou, China), were purchased. The other solvents, purchased from Nanjing Chemical Factory (Nanjing, China) were of analytical grade.2.2. Apparatus and chromatographic conditionsAglient1100 series HPLC apparatus was used. Chromatography was carried out on an Aglient Zorbax SB-C18 column(250 4.6mm, 5.0µm)at a column temperature of 25℃.A Rheodyne 7125i sampling valve (Cotati, USA) equipped with a sample loop of 20µl was used for sample injection. The analog signal from Alltech ELSD 2000 (Alltech, Deerfield, IL, USA)was transmitted to a HP Chemstation for processing through an Agilent 35900E (Agilent Technologies, USA).The optimum resolution was obtained by using a linear gradient elution. The mobile phase was composed of acetonitrile(A) and water(B) which acidified with 0.5% acetic acid. The elution was operated from keeping 29%A for 10min, then gradually to 54%B from 10 to 25 min in linear gradient, and back to the isocratic elution of 54%B from 25 to 30 min.The drift tube temperature for ELSD was set at 106℃and the nitrogen flow-rate was of 2.6 l/min. The chromatographic peaks were identified by comparing their retention time with that of each reference compound tried under the same chromatographic conditions with a series of mobile phases. In addition, spiking samples with the reference compounds further confirmed the identities of the peaks.2.3. Calibration curvesMethanol stock solutions containing seven analytes were prepared and diluted to appropriate concentration for the construction of calibration curves. Six concentrationof the seven analytes’ solution were injected in triplicate, and then the calibration curves were constructed by plotting the peak areas versus the concentration of each analyte. The results were demonstrated in Table1.2.4. Limits of detection and quantificationMethanol stock solution containing seven reference compounds were diluted to a series of appropriate concentrations with methanol, and an aliquot of the diluted solutions were injected into HPLC for analysis.The limits of detection (LOD) and quantification (LOQ) under the present chromatographic conditions were determined at a signal-to-noise ratio (S/N) of 3 and 10, respectively. LOD and LOQ for each compound were shown in Table1.2.5. Precision and accuracyIntra- and inter-day variations were chosen to determine the precision of the developed assay. Approximate 2.0g of the pulverized samples of L. macranthoides were weighted, extracted and analyzed as described in 2.6 Sample preparation section. For intra-day variability test, the samples were analyzed in triplicate for three times within one day, while for inter-day variability test, the samples were examined in triplicate for consecutive three days. Variations were expressed by the relative standard deviations. The results were given in Table 2.Recovery test was used to evaluate the accuracy of this method. Accurate amounts of seven saponins were added to approximate 1.0g of L. macranthoides,and then extracted and analyzed as described in 2.6 Sample preparation section. The average recoveries were counted by the formula: recovery (%) = (amount found –original amount)/ amount spiked ×100%, and RSD (%) = (SD/mean) ×100%. The results were given in Table 3.2.6. Sample preparationSamples of Flos Lonicerae were dried at 50℃until constant weight. Approximate 2.0g of the pulverized samples, accurately weighed, was extracted with 60% ethanol in a flask for 4h. The ethanol was evaporated to dryness with a rotary evaporator. Residue was dissolved in water, followed by defatting with 60ml of petroleum ether for 2 times, and then the water solution was evaporated, residue was dissolved with methanol into a 25ml flask. One ml of the methanol solution was drawn and transferred to a 5ml flask, diluted to the mark with methanol. The resultant solution was at last filtrated through a 0.45µm syringe filter (Type Millex-HA, Millipore, USA) and 20µl of the filtrate was injected to HPLC system. The contents of the analytes were determined from the corresponding calibration curves.3. Results and discussionsThe temperature of drift tube and the gas flow-rate are two most important adjustable parameters for ELSD, they play a prominent role to an analyte response. In ourprevious work [12], the temperature of drift tube was optimized at 90°C for the determination of iridoids. As the polarity of saponins are higher than that of iridoids, more water was used in the mobile phase for the separation of saponins, therefore the temperature for saponins determination was optimized systematically from 95°C to 110°C, the flow-rate from 2.2 to 3.0 l/min. Dipsacoside B was selected as the testing saponin for optimizing ELSD conditions, as it was contained in all samples. Eventually, the drift tube temperature of 106℃and a gas flow of 2.6 l/min were optimized to detect the analytes. And these two exact experimental parameters should be strictly controlled in the analytical procedure [16].All calibration curves showed good linear regression (r2 0.9922) within test ranges. Validation studies of this method proved that this assay has good reproducibility. As shown in Table 2, the overall intra- and inter-day variations are less than 6% for all seven analytes. As demonstrated in Table 3, the developed analytical method has good accuracy with the overall recovery of high than 96% for the analytes concerned. The limit of detection (S/N=3) and the limit of quantification (S/N=10) are less than 0.26μg and 0.88μg respectively (Table1), indicating that this HPLC-ELSD method is precise, accurate and se nsitive enough for the quantitative evaluation of major non- chromaphoric saponins in Flos Lonicerae.It has been reported that there are two major types of saponins in Flos Lonicerae, i.e. saponins with hederagenin as aglycone and saponins with oleanolic acid as the aglycone [17]. But hederagenin type saponins of the herb were reported to have distinct activities of liver protection and anti-inflammatory [7-11]. So we adoptedseven hederagenin type saponins as representative markers to establish a quality control method.The newly established HPLC-ELSD method was applied to analyze seven analytes in five plant sources of Flos Lonicerae, i.e. L. japonica,L. hypoglauca,L. confusa,L. similes and L. macranthoides(Table 4). It was found that there were remarkable differences of seven saponins contents between different plant sources of Flos Lonicerae. All seven saponins analyzed could be detected in L. confusa and L. hypoglauca, while only dipsacoside B was detected in L. japonica. Among all seven saponins interested, only dipsacoside B was found in all five plant species of Flos Lonicerae analyzed, and this compound was determined as the major saponin with content of 53.7 mg/g in L. hypoglauca. On the other hand, macranthoidin B was found to be the major saponin with the content higher than 41.0mg/g in L. macranthoides,L. confusa, and L. similis, while the contents of other analytes were much lower.In our previous study [12], overall HPLC profiles of iridoid glucosides was used to qualitatively and quantitatively distinguish different origins of Flos Lonicerae. As shown in Fig.2, the chromatogram profiles of L. confusa, L. japonica and L. similes seem to be similar, resulting in the difficulty of clarifying the origins of Flos Lonicerae solely by HPLC profiles of saponins, in addition to the clear difference of the HPLC profiles of saponins from L. macranthoides and L. hypoglauca.Therefore, in addition to the conventional morphological and histological identification methods, the contents and the HPLC profiles of saponins and iridoids could also be used as accessory chemical evidence toclarify the botanical origin and comprehensive quality evaluation of Flos Lonicerae.4. ConclusionsThis is the first report on validation of an analytical method for qualification and quantification of saponins in Flos Lonicerae. This newly established HPLC-ELSD method can be used to simultaneously quantify seven saponins, i.e. macranthoidin B, macranthoidin A, dipsacoside B, hederagenin-28-O-β-D-glucopyranosyl(6→1)-O-β-D- glucopyranosyl ester, macranthoside B, macranthoside A, and hederagenin-3-O-α-L-arabinopyranosyl(2→1)-O-α-L-rhamnopyranoside in Flos Lonicerae. Together with the HPLC profiles of iridoids, the HPLC-ELSD profiles of saponins could also be used as an accessory chemical evidence to clarify the botanical origin and comprehensive quality evaluation of Flos Lonicerae.AcknowledgementsThis project is financially supported by Fund for Distinguished Chinese Young Scholars of the National Science Foundation of China (30325046) and the National High Tech Program(2003AA2Z2010).[1]Ministry of Public Health of the People’s Republic of China, Pharmacopoeia ofthe People’s Republic of China, V ol.1, 2000, p. 177.[2]W. Shi, R.B. Shi, Y.R. Lu, Chin. Pharm. J., 34(1999) 724.[3]J.B. Xing, P. Li, D.L. Wen, Chin. Med. Mater., 26(2001) 457.[4]Y.Q. Zhang, L.C. Xu, L.P. Wang, J. Chin. Med. Mater., 21(1996) 204.[5] D. Zhang, Z.W. Li, Y. Jiang, J. Pharm. Anal., 16(1996) 83.[6]T.Z. Wang, Y.M. Li, Huaxiyaoxue Zazhi, 15(2000) 292.[7]J.ZH. Shi, G.T. Liu. Acta Pharm. Sin., 30(1995) 311.[8]Y. P. Liu, J. Liu, X.SH. Jia, et al. Acta Pharmacol. Sin., 13 (1992) 209.[9]Y. P. Liu, J. Liu, X.SH. Jia, et al. Acta Pharmacol. Sin., 13 (1992) 213.[10]J.ZH. Shi, L. Wan, X.F. Chen.ZhongYao YaoLi Yu LinChuang, 6 (1990) 33.[11]J. Liu, L. Xia, X.F. Chen. Acta Pharmacol. Sin., 9 (1988) 395[12]H.J. Li, P. Li, W.C. Ye, J. Chromatogr. A 1008(2003) 167-72.[13]Q. Mao, D. Cao, X.SH. Jia. Acta Pharm. Sin., 28(1993) 273.[14]H. Kizu, S. Hirabayashi, M. Suzuki, et al. Chem. Pharm. Bull., 33(1985) 3473.[15]S. Saito, S. Sumita, N. Tamura, et al. Chem Pharm Bull., 38(1990) 411.[16]Alltech ELSD 2000 Operating Manual, Alltech, 2001, p. 16. In Chinese.[17]J.B. Xing, P. Li, Chin. Med. Mater., 22(1999) 366.Fig. 1 Chemical structures of seven saponins from Lonicera confusa macranthoidin B (1), macranthoidin A (2), dipsacoside B (3), hederagenin-28-O-β-D-glucopyranosyl(6→1)-O-β-D- glucopyranosyl ester (4), macranthoside B (5), macranthoside A (6), and hederagenin-3-O-α-L-arabinopyranosyl(2→1)-O-α-L-rhamnopyranoside (7)Fig. 2Representative HPLC chromatograms of mixed standards and methanol extracts of Flos Lonicerae.Column: Agilent Zorbax SB-C18 column(250 4.6mm, 5.0µm), temperature of 25℃; Detector: ELSD, drift tube temperature 106℃, nitrogen flow-rate 2.6 l/min.A: Mixed standards, B: L. confusa, C: L. japonica, D: L. macranthoides, E: L. hypoglauca, F: L. similes.Table 1 Calibration curves for seven saponinsAnalytes Calibration curve ar2Test range(μg)LOD(μg)LOQ(μg)1 y=6711.9x-377.6 0.9940 0.56–22.01 0.26 0.882 y=7812.6x-411.9 0.9922 0.54–21.63 0.26 0.843 y=6798.5x-299.0 0.9958 0.46–18.42 0.22 0.724 y=12805x-487.9 0.9961 0.38–15.66 0.10 0.345 y=4143.8x-88.62 0.9989 0.42–16.82 0.18 0.246 y=3946.8x-94.4 0.9977 0.40–16.02 0.16 0.207 y=4287.8x-95.2 0.9982 0.42–16.46 0.12 0.22a y: Peak area; x: concentration (mg/ml)Table 2 Reproducibility of the assayAnalyteIntra-day variability Inter-day variability Content (mg/g) Mean RSD (%) Content (mg/g) Mean RSD (%)1 46.1646.2846.2246.22 0.1346.2245.3647.4226.33 2.232 5.385.385.165.31 2.405.285.345.045.22 3.043 4.374.304.184.28 2.244.284.464.024.255.204 nd1)-- -- nd -- --5 1.761.801.821.79 1.701.801.681.841.77 4.706 1.281.241.221.252.451.241.341.201.26 5.727 tr2)-- -- tr -- -- 1): not detected; 2): trace. RSD (%) = (SD/Mean) ×100%Table 3 Recovery of the seven analytesAnalyteOriginal(mg) Spiked(mg)Found(mg)Recovery(%)Mean(%)RSD(%)1 23.0823.1423.1119.7122.8628.1042.7346.1351.0199.7100.699.399.8 0.722.692.672.582.082.913.164.735.515.7698.197.6100.698.8 1.632.172.152.091.732.182.623.884.404.6598.8103.297.799.9 2.94nd1)1.011.050.980.981.101.0297.0104.8104.1102.0 4.250.880.900.910.700.871.081.561.752.0197.197.7101.898.9 2.660.640.620.610.450.610.751.081.211.3397.796.796.096.8 0.97tr2)1.021.101.081.031.111.07100.9102.799.1100.9 1.81): not detected; 2): trace.a Recovery (%) = (Amount found –Original amount)/ Amount spiked ×100%, RSD (%) = (SD/Mean) ×100%Table 4 Contents of seven saponins in Lonicera spp.Content (mg/g)1 2 3 4 5 6 7 L. confusa45.65±0.32 5.13±0.08 4.45±0.11tr1) 2.04±0.04tr 1.81±0.03 L. japonica nd2)nd 3.44±0.09nd nd nd nd L. macranthoides46.22±0.06 5.31±0.13 4.28±0.10 tr 1.79±0.03 1.25±0.03 tr L. hypoglauca11.17±0.07 nq3)53.78±1.18nd 1.72±0.02 2.23±0.06 2.52±0.04 L. similes41.22±0.25 4.57±0.07 3.79±0.09nd 1.75±0.02tr nd 1): trace; 2): not detected.. 3) not quantified owing to the suspicious purity of the peak.。

α-酮异己酸的生物合成研究进展

α-酮异己酸的生物合成研究进展

2018年第37卷第12期 CHEMICAL INDUSTRY AND ENGINEERING PROGRESS·4821·化 工 进展α-酮异己酸的生物合成研究进展程申,张颂红,贠军贤(浙江工业大学化学工程学院,绿色化学合成技术国家重点实验室培育基地,浙江 杭州 310032) 摘要:α-酮异己酸是重要有机酸、药用氨基酸合成前体、新陈代谢调节因子和治疗药物,其生物合成路径条件温和,环境友好。

本文对α-酮异己酸的生理功能和体内代谢机理进行了归纳,并着重对其生物合成路径的研究进展进行了综述。

现有研究表明,α-酮异己酸可用葡萄糖为底物,通过代谢工程改造的谷氨酸棒杆菌或大肠杆菌工程菌发酵合成,但产物浓度较低;或以L-亮氨酸为底物,经氨基酸转氨酶、氧化酶、脱氨酶、重组工程菌或全细胞催化转化合成,产物浓度较高。

α-酮异己酸高产菌株的筛选、利用代谢工程方法对菌株进行改造以构建高效工程菌、发酵与分离提取工艺优化等问题,是今后需要研究的重点。

关键词:α-酮异己酸;生物合成;代谢工程中图分类号:Q939.97 文献标志码:A 文章编号:1000-6613(2018)12–4821–09 DOI :10.16085/j.issn.1000-6613. 2018-0193Recent advances in microbial synthesis of α-ketoisocaproateCHENG Shen, ZHANG Songhong,YUN Junxian(State Key Laboratory Breeding Base of Green Chemistry Synthesis Technology, College of Chemical Engineering,Zhejiang University of Technology, Hangzhou 310032, Zhejiang, China )Abstract :α-Ketoisocaproate (KIC) is not only an important organic acid and key precursor ofbranched chain amino acids for pharmaceuticals, but also a metabolic regulator and therapeutic agent. Biosynthesis pathway for the production of KIC has advantages of the mild reaction conditions and environment-friendly processes. In this work, the advances of the important physiological properties, the metabolisms and the biosynthetic pathways of KIC, were summarized. According to the references, two biosynthetic pathways are available for the preparation of KIC. The first one is the microbial fermentation approach using the strains of Corynebacterium glutamicum by metabolic engineering or recombinant Escherichia coli with glucose as the substrate, where the yield is low. The another is the enzymatic catalyzing using amino acid aminotransferases, oxidases or deaminases, the whole-cell bioconversion and the recombinant engineering strains using L-leucine as the substrate, where the yield is slightly high. Issues regarding the metabolic engineering improvement of the yield of KIC, the biosynthesis pathway, and the advanced fermentation and separation techniques, were proposed and considered as the important future research directions.Key words: α-ketoisocaproate ;biosynthesis ;metabolic engineeringα-酮异己酸(α-ketoisocaproate ,KIC )即4-甲基-2-氧代异己酸,是一种重要的高值有机酸和治疗药物,在生物体内可与L-亮氨酸相互转化,如图1所示。

醋酸在制氢中缓冲作用

醋酸在制氢中缓冲作用

ResearcharticleBuffering action of acetate on hydrogen production by Ethanoligenens harbinense B49Ji-Fei Xu a ,⁎,Yuan-Ting Mi a ,Nan-Qi Ren b ,⁎a School of Environmental and Resources,Inner Mongolia University,People's Republic of ChinabState Key Laboratory of Urban Water Resources and Environment,Harbin Institute of Technology,People's Republic of Chinaa b s t r a c ta r t i c l e i n f o Article history:Received 15January 2016Accepted 13July 2016Available online 3August 2016The buffering effect of acetate on hydrogen production during glucose fermentation by Ethanoligenens harbinense B49was investigated compared to phosphate,a widely used fermentative hydrogen production buffer.Speci fic concentrations of sodium acetate or phosphate were added to batch cultures,and the effects on hydrogen production were comparatively analyzed using a modi fied Gompertz model.Adding 50mM acetate or phosphate suppressed the hydrogen production peak and slightly extended the lag phase.However,the overall hydrogen yields were 113.5and 108.5mmol/L,respectively,and the final pH was effectively controlled.Acetate buffered against hydrogen production more effectively than did phosphate,promoting cell growth and preventing decreased pH.At buffer concentrations 100–250mM,the maximum hydrogen production was barely suppressed,and the lag phase extended past 7h.Therefore,although acetate inhibits hydrogen production,using acetate as a buffer (like phosphate)effectively prevented pH drops and increased substrate consumption,enhancing hydrogen production.©2016Ponti ficia Universidad Católica de Valparaíso.Production and hosting by Elsevier B.V.All rightsreserved.This is an open access article under the CC BY-NC-ND license(/licenses/by-nc-nd/4.0/).Keywords:AcetateBiohydrogen Buffering actionEthanoligenens harbinense phosphate1.IntroductionResearch into alternative energy sources has attracted renewed interest following an increased global awareness of accumulated CO 2in the atmosphere and its role as a potential cause of climate change [1].Hydrogen is an ideal clean and sustainable energy source that can be used in fuel cells,transportation and other pared with conventional hydrogen production processes,including the electrolysis of water,the reforming of natural gas and oil and the gasi fication of coal,biological hydrogen production offers a promising technique that makes use of renewable biomass and organic wastewater.Biohydrogen production can be divided into two main categories:hydrogen production by photosynthetic organisms using light and hydrogen production via fermentative metabolism by anaerobic bacteria [2,3,4].Relative to the photosynthetic production of hydrogen,fermentative processes offer the advantages of higher hydrogen production rates without illumination and the ability to convert organic wastes into more valuable energy sources.Many factors [5],such as the carbon source [6,7,8],nitrogen source [9,10],hydrogen pressure [11,12,13],pH [14],temperature [15]andend-products [16],can in fluence fermentative hydrogen production.Among these factors,pH is one of the factors controlling anaerobic biological processes [17].In an anaerobic reactor the pH value and its stability are important.This pH value and stability are relevant to different acid –base systems such as propionic,butyrate and mixed fatty acid systems.The formation of hydrogen is accompanied with volatile fatty acids (VFAs)or solvents during the anaerobic digestion process.The accumulation of these acids causes a sharp decrease in the culture pH and subsequently inhibits bacterial hydrogen production,a failure to control pH changes due to volatile fatty acid (VFA)imbalances can interrupt hydrogen production [17,18].Buffers and automatically controlled pH systems are two commonly used methods for this purpose in anaerobic hydrogen production systems.Because of their convenience and availability,carbonate and phosphate are two important components in acid –base buffer systems and are widely used in anaerobic hydrogen production systems [19].Phosphate in particular is regarded as an appropriate buffer,and its effects on hydrogen production by Ethanoligenens harbinense B49have already been studied [20].E.harbinense B49was isolated from a continuous flow,high-rate acidogenic reactor using ethanol-type fermentation,and it is a Gram-positive,mesophilic,strictly anaerobic bacterium that is phylogenetically related to the clostridia class.This bacterium is one of the most promising producer organisms due to its capability toElectronic Journal of Biotechnology 23(2016)7–11⁎Corresponding authors.E-mail address:Jifeixu@ (J.-F.Xu).Peer review under responsibility of Ponti ficia Universidad Católica deValparaíso./10.1016/j.ejbt.2016.07.0020717-3458/©2016Ponti ficia Universidad Católica de Valparaíso.Production and hosting by Elsevier B.V.All rights reserved.This is an open access article under the CC BY-NC-ND license (/licenses/by-nc-nd/4.0/).Contents lists available at ScienceDirectElectronic Journal of Biotechnologyefficiently and rapidly generate hydrogen[11],and its characteristics make it an interesting target for physiological and genetic studies aiming to improve its metabolic properties and increase its productivity with respect to hydrogen.This microorganism produces ethanol as a major fermentation product,in addition to CO2,acetate and H2 [21,22,23].The addition of ethanol had little inhibitory effect on fermentative hydrogen production,and the addition of acetate had a strong inhibitory effect on glucose consumption,bacterial growth and hydrogen production of E.harbinese B49[24].The hydrogen production is affected by the accumulation of self-produced byproducts,and acetate is therefore regarded as having an inhibitory rather than a buffering action during fermentative hydrogen production by E.harbinense B49.The inhibitory effect of acetate has been studied to understand the hydrogen-producing characteristics of these cultures,but its buffering effect has not been explored.In this paper,the effects of acetate on hydrogen production by E.harbinense B49were investigated to examine the buffering action of acetate on this process.2.Materials and methods2.1.Microorganism and mediaThe hydrogen-producing strain E.harbinense B49(AF481148in EMBL)was isolated from a continuousflow,high-rate acidogenic reactor using ethanol-type fermentation and then identified as a novel Ethanoligenens strain[24].The strain was stored in our lab at−80°C and cultured at36°C at an initial pH of6.5under strict anaerobic conditions.Cells from stock cultures were transferred into50-mL volumes of sterilised growth medium and incubated at35°C.When the cells entered a logarithmic growth phase,5mL of the pre-cultured broth was inoculated into a100-mL serum bottle containing50mL of basal medium,and the culture was grown anaerobically at35°C with shaking at130rpm.The hydrogen production medium consisted of (in g/L):glucose10.0,yeast extract3.0,NH4Cl0.5,MgCl20.18,K2HPO4 1.5,NaH2PO44.2and L-cysteine0.5.The basal medium also contained 1%trace element solution,1%vitamin solution and0.2%resazurin.The cells were harvested at the end of the exponential phase and used as inocula for the batch experiments.2.2.Batch testsThe buffering activities and inhibitory effects of phosphate,acetate and ethanol on the hydrogen-producing performance of strain B49 were investigated using serum bottles as batch reactors.All of the batch-fermentation studies were performed in250-mL serum bottles with a120-mL working volume.The hydrogen production medium also contained sodium acetate(NaAC·3H2O,at0,50,100,150,200or 250mM)or phosphate(Na2HPO4×2H2O-KH2PO4,at0,50,100,150, 200or250mM).Three bottles were tested in parallel for each condition.All media were sterilised by autoclaving at121°C and 15psig for30min.Each bottle was then inoculated with5.0mL of strain B49cell suspension and incubated under non-controlled pH conditions in an air-bath shaker at36±1°C and135rpm.The biogas was sampled for biogas content analysis using a syringe,and a liquid sample was simultaneously taken from the bottles.All tests were run in triplicate.2.3.Analytical methods2.3.1.Cell growth analysisThe cell dry weight was determined by drying the cells for24h at80°C to a constant weight in a convection-type hot air oven (HPG-9145,China).2.3.2.Liquid samplesCells in the liquid cultures were pelleted by centrifugation at 8000rpm for5min at room temperature.The culture supernatant was filtered through a2.5-cm diameter,0.45-μm polytetrafluoroethylene filter,transferred to sterile1-mL Eppendorf tubes and frozen until analysis.Volatile fatty acids and ethanol were detected using a gas chromatography(GC)system(HP6890,Agilent Technologies,USA) and aflame-ionisation detector(FID).The temperatures of the glass columns and injections were145°C and175°C,respectively.The carrier gas was N2,and the packing material was FON(which contains polyethylene glycol and2-nitroterephthalic acid),obtained from Shimadzu,Inc.The glucose concentration in the culture was determined according to the protocol in a kit(GOD-PAP,Shanghai Rongsheng Biological Technology Corporation,China),and the pH was measured using a pHS-25acidity voltmeter according to standard methods.2.3.3.Biogas compositionBiogas production was measured using the water displacement method.The biogas composition from the bioreactor was measured using GC(HP4890,Agilent)on an instrument equipped with a thermal conductivity detector(TCD).A stainless steel column packed with molecular sieve5A was used to detect H2.Nitrogen was used as the carrier gas at a rate of25mL/min.3.Modeling the kinetic parametersThe cumulative hydrogen production data werefitted using a modified Gompertz equation[25,26]as a suitable model for describing the progress of cumulative hydrogen production in the batch experiment.H¼PÁexp−expRmPλ−tðÞþ1½Equation1in which H is the cumulative hydrogen production(in mL/L);P is the hydrogen production potential(in mL/L);R m is the maximum hydrogen production rate(as mL/L/h);λis the time of the lag phase(h);e is 2.7182;and t is the incubation time(h).Table1Glucose degradation,cell growth and terminal pH at various acetate or phosphate concentrations.Buffer con.(mM)Degradation rate(%)Biomass(mg/L)Terminal pHPhosphate Acetate Phosphate Acetate Phosphate Acetate097±1.297±1.2619.32±61.9623±61.5 3.75±0.03 3.75±0.03 50100±1.4100±1.1646.07±58.3916±75.4 4.15±0.03 4.73±0.03 10095±0.6100±0.6616.87±46.51044±71.4 4.60±0.03 5.07±0.03 15087±1.1100±0.9505.68±56.41138±61.2 5.35±0.03 5.22±0.03 20063±1.6100±1.4455.19±50.31166±80.3 6.05±0.03 5.33±0.03 25050±0.598±0.8420.24±44.91213±90.1 6.20±0.03 5.41±0.03 8J.-F.Xu et al./Electronic Journal of Biotechnology23(2016)7–114.Results and discussion4.1.Glucose degradation and cell growthThe glucose degradation ef ficiencies,cell growth and terminal pH values at various phosphate and acetate concentrations are illustrated in Table 1.In the tests of acetate,the glucose was almost completely degraded at the end of fermentation,achieving 97–100%total glucose degradation.In contrast to acetate,the addition of phosphate had an obvious inhibitory effect on glucose degradation.From 0to 50mM phosphate,the glucose degradation reached approximately 97–100%.When more phosphate was added beyond 100mM,the glucose degradation rates declined,achieving only 50%glucose degradation at 250mM.This result indicates that the addition of excess phosphate had a signi ficant negative in fluence on glucose degradation.In the phosphate tests,cell growth was improved with 50mM phosphate.However,as the phosphate concentration increased,cell growth was gradually inhibited.In contrast,the total cell weight increased as more acetate was added.This result was inconsistent with that of another research report,a discrepancy that may be due to differences in the composition of the hydrogen production medium [24].The initial pH in all tests was approximately 6.5.As shown in Table 1,at the end of hydrogen-producing fermentation,the terminal pH values of media supplemented with 50mM or 100mM phosphate were much higher than those of acetate-supplemented media.However,when the concentrations of phosphate and acetate exceeded 150mM,the terminal pH values of the acetate-supplemented media were much higher than those supplemented with phosphate,due to the buffer system of sodium acetate and acetate.These results indicated that acetate was able to promote the cell growth of E.harbinense B49and raise the terminal pH as a result of its enhanced buffering of the fermentative system.In contrast,although phosphatewas able to raise the terminal pH by buffering Na 2HPO 4·2H 2O-KH 2PO 4,it also restrained cell growth.4.2.Time course of hydrogen production pro files4.2.1.Under different phosphate concentration conditionsHydrogen production by E.harbinense B49was signi ficantly affected by the phosphate concentration of the medium.As shown in Fig.1and Table 2,a slight increase in the cumulative hydrogen yield could be achieved by increasing the phosphate buffer concentration from 0mM to 50mM.A maximum P max of 108.54mmol/L and R max of 18.39mmol/L/h were observed at phosphate buffer concentrations of 50mM and 100mM,respectively.Subsequently,P max and R max decreased gradually as the phosphate buffer concentration increased,most likely due to the negative effect of increased cytoplasmic osmotic pressure [27].The lag phase times of hydrogen production became longer as the phosphate concentration increased.The final pH also increased with increasing phosphate buffer concentrations,whereas lower phosphate buffer concentrations were associated with lower pH values.Similar to glucose consumption and cell growth,hydrogen production also peaked at 50mM phosphate,as shown in Table 1and Table 2.Different results were obtained in previous studies of Citrobacter sp.Y19[28]and Rhodopseudomonas palustris P4[29].No inhibitory effect of phosphate on cell growth was observed at concentrations between 0and 300mM.The maximum hydrogen yield was obtained at concentrations of 50and 140mM phosphate by R.palustris P4and Citrobacter sp.Y19,respectively.The present results indicate that the optimal phosphate concentration is 50mM for E.harbinense B49.At this concentration,the maximal yield of hydrogen was produced;the most glucose was exhausted;and the lag phase was relatively shorter.Similar results were reported for Clostridium beijerinckii Fanp3[30].4.2.2.Under different acetate concentration conditionsThe effects of acetate concentration on hydrogen production are shown in Fig.2and Table 2.The glucose in the media was completely exhausted after 48h of incubation irrespective of the acetate concentration.However,the addition of acetate had a considerable impact on the cumulative hydrogen pared with hydrogen production medium that did not include acetate,an increase in the cumulative hydrogen yield could be achieved by increasing the acetate buffer concentration to 50mM,and the addition of additional acetate extended the lag phase of hydrogen production.The maximum P max of 113.53mmol/L and R max of 12.56mmol/L/h occurred at an acetate buffer concentration of 50mM and in media with no acetate added,respectively.When the concentration of acetate was greater than 50mM,slight inhibition of hydrogen production occurred,and the P max and R max values decreased gradually with increasing acetate concentration.However,cell growth was inversely related to the hydrogen production rate and increased with increasing acetate,as shown in Table 1.20406080100120C u m u l a t i v e H 2 p r o d u c t i o n (m M )Time (h)Fig.1.Time course of hydrogen production pro files during fermentation of glucose under different phosphate concentration conditions.The lines represent data calculated using Gompertz equation.Table 2Fermentation characteristics for hydrogen production at various phosphate or acetate concentrations.Buffer con.(mM)P max (mmol/L)R max (mmol/L/h)λ(h)R 2PhosphateAcetate Phosphate Acetate Phosphate Acetate Phosphate Acetate 0108.14108.1412.8412.56 4.2 4.20.99860.998650108.54113.5313.9610.53 4.4 6.80.99790.9905100102.69106.5218.39 6.197.08.80.99840.9932150105.86103.849.69 6.307.911.40.99550.998820084.34104.027.74 6.1610.511.60.99590.997125018.01100.222.967.4514.213.40.99440.99419J.-F.Xu et al./Electronic Journal of Biotechnology 23(2016)7–114.3.The amount of volatile organic compound and hydrogenThe amount of acetate,ethanol and hydrogen at various phosphate and acetate concentrations are shown in Fig.3.The amount of ethanol were increased slightly with increasing phosphate or acetate concentration,the concentration of acetate and the volume of hydrogen were varied only slightly while the concentration of acetate was increased,but decreased dramatically while the concentration of phosphate was increased.In contrast to acetate,the addition of phosphate had an obvious inhibitory effect on acetate and hydrogen production.At 250mM acetate,the volume of hydrogen exceeded 100mM which achieved the maximum volume of hydrogen at 50mM acetate.However,at 250mM phosphate,the volume of hydrogen was less than 20mM which is one fifth of the maximum volume of hydrogen at phosphate.This result indicates that the addition of excess phosphate had a signi ficant negative in fluence on hydrogen production.Hydrogen production from glucose by hydrogen-producing microorganisms also yields volatile organic acids,such as acetic acid and butyric acid,which lower the pH of the media and slow hydrogenproduction [31].To minimise the effects of these organic acids on the pH,phosphate buffers composed of Na 2HPO 4and NaH 2PO 4or KH 2PO 4were used to control the pH.Acetic acid is mainly a product of fermentation;therefore,acetate has been regarded as an inhibitor of hydrogen production and has not been used to control pH.However,the present results indicate that acetate was able to control the pH during fermentative hydrogen production from glucose by E.harbinense B49.We also evaluated the ability of phosphate and acetate to control pH during fermentation,and we found that although both phosphate and acetate were able to control the pH through their buffering activity,acetate was a stronger buffer than phosphate until the concentrations exceeded 150mM.The final pH increased with increasing concentrations of acetate and phosphate,but their patterns of buffer activity may be different.Sodium acetate and acetate,which were produced during fermentative hydrogen production,formed a buffer that grew increasingly strong.Acetate was “internal buffer system ”,while phosphate was “external buffer system ”.5.ConclusionsThe addition of acetate had both inhibitory and buffering effects on hydrogen production from glucose by E.harbinense B49.Acetate was able to control the pH changes caused by fermentative hydrogen production and increased the yield of hydrogen.At an acetate concentration of 50mM,maximal hydrogen production of 113.5mmol/L was achieved.The inhibitory effect of acetate on hydrogen production was mainly due to an extended lag phase,and acetate slightly decreased the cumulative hydrogen volume when added at concentrations between 100and 250mM.Therefore,using acetate as a buffering supplement can control the pH and alleviate the acidi fication of the growth medium.Con flict of interestWe have no con flict of interest to declare.AcknowledgmentsThis research was supported by the National Natural Science Foundation of China (Grant No.51108226).An earlier version of this paper was presented at 20th World Hydrogen Energy Conference 2014.References[1]Kotay SM,Das D.Biohydrogen as a renewable energy resource —Prospects andpotentials.Int J Hydrog Energy 2008;33:258–63./10.1016/j.ijhydene.2007.07.031.[2]Das D,Veziroglu T.Hydrogen production by biological processes:A survey ofliterature.Int J Hydrog Energy 2001;26:13–28./10.1016/S0360-3199(00)00058–6.[3]Hallenbeck PC,Ghosh D.Advances in fermentative biohydrogen production:Theway forward?Trends Biotechnol 2009;27:287–97./10.1016/j.tibtech.2009.02.004.[4]Ren N,Guo W,Liu B,Cao G,Ding J.Biological hydrogen production by darkfermentation:Challenges and prospects towards scaled-up production.Curr Opin Biotechnol 2011;22:365–70./10.1016/j.copbio.2011.04.022.[5]Wang JL,Wan W.Factors in fluencing fermentative hydrogen production:A review.Int J Hydrog Energy 2009;34:799–811./10.1016/j.ijhydene.2008.11.015.[6]Kádár Z,Vrije T,Van Noorden GE,Budde MAW,Szengyel Z,Réczey K,et al.Yieldsfrom glucose,xylose,and paper sludge hydrolysate during hydrogen production by the extreme thermophile Caldicellulosiruptor saccharolyticus .Appl Biochem Biotechnol 2004;114:497–508./10.1385/ABAB:114:1-3:497.[7]Niel EWJ,Pieternel AMC,Stams AJM.Substrate and product inhibition of hydrogenproduction by the extreme thermophile.Caldicellulo-siruptor saccharolyticus .Biotechnol Bioeng 2003;81:255–62./10.1002/bit.10463.[8]Panagiotopoulos IA,Bakker RR,Budde MAW,de Brije T,Claaseen PAM,Koukios EG.Fermentative hydrogen production from pretreated biomass:A comparative study.Bioresour Technol 2009;100:6331–8./10.1016/j.biortech.2009.07.011.[9]Lin CY,Lay CH.Carbon/nitrogen-ratio effect on fermentative hydrogen productionby mixed micro flora.Int J Hydrog Energy 2004;29:41–5./10.1016/S0360-3199(03)00083-1.306090120150)M m (n o i t c u d o r p f o s d l e i Y Concentration of buffer (mM)Fig.3.The change of acetate,ethanol and hydrogen yield under different phosphate or acetate concentration conditions (P and A represented phosphate and acetate buffer,respectively.The yield of acetate subtracted the concentration of acetate-supplemented in the media under different acetate concentration conditions).612182430364248C u m u l a t i v e H 2 p r o d u c t i o n (m M )Time (h)Fig.2.Time course of hydrogen production pro files during fermentation of glucose under different acetate concentration conditions.The lines represent data calculated using Gompertz equation.10J.-F.Xu et al./Electronic Journal of Biotechnology 23(2016)7–11[10]Xu L,Ren N,Wang X,Jia Y.Biohydrogen production by Ethanoligenens harbinenseB49:Nutrient optimization.Int J Hydrog Energy2008;33:6962–7./10.1016/j.ijhydene.2008.09.005.[11]Mizuno O,Dinsdale R,Hawkes FR,Hawkes DL,Noike T.Enhancement of hydrogenproduction from glucose by nitrogen gas sparging.Bioresour Technol2000;73: 59–65./10.1016/S0960-8524(99)00130–3.[12]Kraemer JT,Bagley DM.Supersaturation of dissolved H2and CO2duringfermentative hydrogen production with N2sparging.Biotechnol Lett2006;28: 1485–91./10.1007/s10529-006-9114-7.[13]Kraemer JT,Bagley DM.Improving the yield from fermentative hydrogenproduction.Biotechnol Lett2007;29:685–95./10.1007/s10529-006-9299-9.[14]Fang HHP,Liu H.Effect of pH on hydrogen production from glucose by a mixedculture.Bioresour Technol2002;82:87–93./10.1016/S0960-8524(01)00110–9.[15]Yokoyama H,Waki M,Moriya N,Yasuda T,Tanaka Y,Haga K.Effect of fermentationtemperature on hydrogen production from cow waste slurry by using anaerobic mi-croflora within the slurry.Appl Microbiol Biotechnol2007;74:474–83./10.1007/s00253-006-0647-4.[16]Zheng XJ,Yu HQ.Inhibitory effects of butyrate on biological hydrogen productionwith mixed anaerobic cultures.J Environ Manage2005;74:65–70./10.1016/j.jenvman.2004.08.015.[17]Lin CY,Lay CH.Effects of carbonate and phosphate concentrations on hydrogenproduction using anaerobic sewage sludge microflora.Int J Hydrog Energy2004;29:275–81./10.1016/j.ijhydene.2003.07.002.[18]Castro-Villalobos MC,García-Morales JL,Fernández FJ.By-products inhibition effectson bio-hydrogen production.Int J Hydrog Energy2012;37:7077–83./10.1016/j.ijhydene.2011.12.032.[19]Lin PJ,Chang JS,Yang LH,Lin CY,Wu SY,Lee KS.Enhancing the performance ofpilot-scale fermentative hydrogen production by proper combinations of HRT and substrate concentration.Int J Hydrog Energy2011;36:14289–94./10.1016/j.ijhydene.2011.04.147.[20]Wang XJ,Ren NQ,Xiang WS,Guo WQ.Influence of gaseous end-productsinhibition and nutrient limitations on the growth and hydrogen production by hydrogen-producing fermentative bacterial B49.Int J Hydrog Energy2007;32: 748–54./10.1016/j.ijhydene.2006.08.003.[21]Ren NQ,Xu L,Zhang Y,Xu H,Wang X,Chen G.Dependence on iron and hydrogenproducing pathway for novel strain Ethanoligenens sp.B49.Acta Sci Circumst 2006;26:1643–50./10.3321/j.issn:0253-2468.2006.10.011.[22]Hallenbeck PC,Abo-Hashesh M,Ghosh D.Strategies for improving biologicalhydrogen production.Bioresour Technol2012;110:1–9./10.1016/j.biortech.2012.01.103.[23]Castro JF,Razmilic V,Gerdtzen ZP.Genome based metabolicflux analysis ofEthanoligenens harbinense for enhanced hydrogen production.Int J Hydrog Energy 2013;8:1297–306./10.1016/j.ijhydene.2012.11.007.[24]Tang J.Inhibitory effects of acetate and ethanol on biohydrogen production ofEthanoligenens harbinese B49.Int J Hydrog Energy2012;37:741–7./10.1016/j.ijhydene.2011.04.067.[25]Wang AJ,Ren N,Shi Y,Lee DJ.Bioaugmented hydrogen production frommicrocrystalline cellulose using co-culture Clostridium acetobutylicum X9 and Ethanoligenens harbinense B49.Int J Hydrog Energy2008;33:912–7./10.1016/j.ijhydene.2007.10.017.[26]Antonopoulou G,Gavala HN,Skiadas IV,Lyberatos G.Modeling of fermentativehydrogen production from sweet sorghum extract based on modified ADM1.Int J Hydrog Energy2012;37:191–208./10.1016/j.ijhydene.2011.09.081.[27]Nath K,Das D.Modeling and optimization of fermentative hydrogen production.Bioresour Technol2011;102:8569–81./10.1016/j.biortech.2011.03.108.[28]Oh YK,Seol EH,Kim JR,Park S.Fermentative biohydrogen production by a newchemoheterotrophic bacterium Citrobacter sp.Y19.Int J Hydrog Energy2003;28: 1353–9./10.1016/S0360-3199(03)00024–7.[29]Oh YK,Seol EH,Lee EY,Park S.Fermentative hydrogen production by a newchemoheterotrophic bacterium Rhodopseudomonas palustris P4.Int J Hydrog Energy 2002;27:1373-19./10.1016/S0360-3199(02)00100–3.[30]Pan CM,Fan YT,Zhao P,Hou HW.Fermentative hydrogen production by the newlyisolated Clostridium beijerinckii Fanp3.Int J hydrog Energy2008;33:5383–91./10.1016/j.ijhydene.2008.05.037.[31]Van Lier JB,Grolle KC,Frijters CT,Stams AJ,Lettinga G.Effects of acetate,propionate,and butyrate on the thermophilic anaerobic degradation of propionate by methanogenic sludge and defined cultures.Appl Environ Microbiol1993;59: 1003–11.11J.-F.Xu et al./Electronic Journal of Biotechnology23(2016)7–11。

原位限域生长策略制备有序介孔碳负载的超小MoO_(3)纳米颗粒

原位限域生长策略制备有序介孔碳负载的超小MoO_(3)纳米颗粒

Vol.42 2021年5月No.51589~1597 CHEMICAL JOURNAL OF CHINESE UNIVERSITIES高等学校化学学报原位限域生长策略制备有序介孔碳负载的超小MoO3纳米颗粒王常耀,王帅,段林林,朱晓航,张兴淼,李伟(复旦大学化学系,上海200433)摘要采用原位限域生长策略制备了一系列有序介孔碳负载的超小MoO3纳米颗粒复合物(OMC-US-MoO3).其中,有序介孔碳被用作基质来原位限域MoO3纳米晶的生长.依此方法制备的MoO3纳米晶具有超小的晶粒尺寸(<5nm),并在介孔碳骨架内具有良好的分散度.制得的OMC-US-MoO3复合物具有可调的比表面积(428~796m2/g)、孔容(0.27~0.62cm3/g)、MoO3质量分数(4%~27%)和孔径(4.6~5.7nm).当MoO3纳米晶的质量分数为7%时,所得样品OMC-US-MoO3-7具有最大的孔径、最小的孔壁厚度和最规整的介观结构.该样品作为催化剂时,表现出优异的环辛烯选择性氧化性能.关键词有序介孔碳;氧化钼纳米晶;纳米材料;限域生长中图分类号O611.4文献标志码AIn situ Confinement Growth Strategy for Ordered Mesoporous CarbonSupport Ultrasmall MoO3NanoparticlesWANG Changyao,WANG Shuai,DUAN Linlin,ZHU Xiaohang,ZHANG Xingmiao,LI Wei*(Department of Chemistry,Fudan University,Shanghai200433,China)Abstract Ultrasmall particle sizes and excellent dispersity of the MoO3active species on support majorly dominate their catalytic performances.Herein,a series of ordered mesoporous carbon support ultrasmall mo⁃lybdena nanoparticles(OMC-US-MoO3)composites was synthesized through an in situ confinement growth strategy.Ordered mesoporous carbon was used as the matrix to in situ confine the growth of MoO3nanocrystals. The obtained MoO3nanocrystals show ultrasmall particle sizes(<5nm)and excellent dispersity on the meso-porous carbon frameworks.The obtained OMC-US-MoO3exhibits tunable specific surface areas(428―796 m2/g),pore volumes(0.27―0.62cm3/g),MoO3contents(4%―27%,mass fraction)and uniform pore sizes (4.6―5.7nm).As a typical example,the obtained sample with7%MoO3(denoted as OMC-US-MoO3-7)shows the largest pore size,smallest thickness of pore wall and most regular mesostructures.When being used as a catalyst,the OMC-US-MoO3-7exhibits an excellent catalytic activity for selective oxidation of cyclooctene with a high stability.Keywords Ordered mesoporous carbon;MoO3nanocrystal;Nanomaterials;Confinement growthdoi:10.7503/cjcu20200303收稿日期:2020-05-28.网络出版日期:2020-09-24.基金项目:国家自然科学基金(批准号:21975050)、国家重点研发计划纳米科技重点专项(批准号:2016YFA0204000, 2018YFE0201701)和中国博士后科学基金(批准号:2019M651342)资助.联系人简介:李伟,男,博士,教授,主要从事介孔材料的合成及应用研究.E-mail:*******************.cn1590Vol.42高等学校化学学报Epoxides,an important industrial chemicals,has been widely used in the fields of food additives,phar⁃maceutical intermediates,etc.[1,2].Catalytic epoxidation of olefin is one of the essential route to produce epo-xides,which oxygenation of carbon-carbon double bond to form cyclic epoxide groups.The kind of catalyst plays a key role on the epoxidation reaction.Among all catalysts,precious metal of gold based one illustrates high activity for olefin epoxidations[3,4].However,gold is limited resource and very expensive,even though it shows high conversion efficiency.Molybdenum oxide(MoO3),as one of the low cost,non-toxic and environ⁃mentally benign transition metal oxides,is widely used as heterogeneous catalysis for Friedel-Crafts alkyla⁃tion[5],hydrogenation reaction[6,7],epoxidation reaction[8,9],hydrogen evolution reaction[10],electrochemical energy storage for lithium-ion batteries[11,12],and gas sensors[13,14],etc..Gratifyingly,MoO3has been reported by several groups which have high activity for epoxidation of olefins in recent years[15,16].It is obvious that the size and morphology of MoO3active species are critical factors that affect their prop⁃erties for application[17~20].However,the synthesis and reaction process often easily causes serious sintering,migration and agglomeration of the MoO3nanoparticles,leading to the degradation of catalytic activity.Sup⁃ports are necessary for the immobilization of active species.Carbon has been widely used as an outstanding matrix to control the size and dispersity of supported metal oxides attributing to its advantages of intrinsical chemical inertness,high thermal stability,non-toxic and wide-sources[21~23].Molybdena supported carbon have been reported and show excellent performance as the catalyst for cyclooctene epoxidation[24,25].Recently,Chen group[26]fabricatedγ-Fe2O3@C@MoO3core-shell structured nanoparticles as a magnetically recyclable catalyst for the epoxidation reaction of olefins.The coated carbon layer play an efficient role for the stabiliza⁃tion of magnetic core.Biradar group[8]also reported a carbon microspheres-supported molybdena nanoparticles catalyst which also show outstanding effect for the epoxidation of olefins.However,above-mentioned catalysts are less porosity.Porous supports,especially,mesoporous carbon have been reported on many catalytic areas because of its large surface area,pore volume and pore size,which can not only improve the load capacity but also enlarge the reaction progress,where the diffusion process may be the rate-limiting step[26~28].Up to now,it is still urgent to fabricate mesoporous carbon supported MoO3catalyst with ultrasmall particle size and excel⁃lent dispersity.Herein,we construct an ordered mesoporous carbon support ultrasmall MoO3nanoparticles(OMC-US-MoO3)composites via an in situ confinement growth strategy.In this strategy,the ordered mesoporous carbon works as a matrix to in situ confine the growth of MoO3nanocrystals.The obtained MoO3nanocrystals show ultrasmall particle size(<5nm)and excellent dispersity on the mesoporous carbon frameworks.The content (mass fraction)of MoO3can be tuned from4%to27%.The obtained OMC-US-MoO3shows tunable specific surface areas(428―796m2/g),pore volumes(0.27―0.62cm3/g)and uniform pore size(4.6―5.7nm).As a typical example,the obtained sample with7%MoO3(denoted as OMC-US-MoO3-7)shows largest pore size,smallest thickness of pore wall and most regular mesostructures.When being used as a catalyst,the OMC-US-MoO3-7exhibits an excellent catalytic activity for selective oxidation of cyclooctene with a high stability.1Experimental1.1Chemicals and MaterialsPluronic F127(EO106PO70EO106,M w=12600)was purchased from Aldrich.All others chemicals were obtained from Aladdin company and used directly.Deionized water was used in all experiments.1.2Synthesis of Ordered Mesoporous Carbon Support Ultrasmall Molybdena NanoparticlesIn detail synthesis procedure,1.0g of Pluronic F127powders was added into10.0g of ethanol solution and stirred to a homogeneous clear solution at40℃.Afterwards,5.0g of20%(mass fraction)preformedNo.5王常耀等:原位限域生长策略制备有序介孔碳负载的超小MoO 3纳米颗粒phenolic resins ethanol solution and 1.0mL of peroxomolybdenum precursor solution were added into the ho⁃mogeneous system (5—200mg/mL ).The preformed phenolic resins was synthesized based on the reported method [27,28].Peroxomolybdenum precursor solution [29]was prepared by dissolving different contents of molyb⁃denum trioxide into 10.0mL of 30%hydrogen peroxide.The mixture solution was poured into dishes after 2h and then the dishes were heat treated at 40and 100℃for 8and 20h ,respectively ,forming the as -made com⁃posites consisting of Pluronic F127,phenolic resins ,and Mo species (denoted as as -made sample ).Then ,the calcination of as -made sample was implemented in a tubular furnace under N 2atmosphere.The temperature program was set from 25℃to 350℃with a ramp of 1℃/min ,maintenance for 3h ,and then to 600℃with 1℃/min ,maintenance for 2h.The obtained sample after pyrolysis was named as ordered mesoporous carbon support ultrasmall molybdena nanoparticles (OMC -US -MoO 3-x ),wherein x represent the actual mass fraction of MoO 3.1.3Activity Test The selective oxidation reaction of cyclooctene was carried out in the round -bottom flask (50mL ).In which ,40.0mmol of cyclooctene ,40.0mmol of 5.5mol/L TBHP in decane ,10mg of OMC -US -MoO 3-7cata⁃lyst (0.0048mmol/L of MoO 3),6.0g of 1,2-dichloroethane as solvent ,and 15.0mmol of chlorobenzene as internal standard.The reaction temperature is 80℃.At different time intervals ,conversion was calculated by sampling.The samples were analyzed on an Agilent 7890A gas chromatograph equipped with a HP -5column and products were confirmed by GC -MS.TOF values (mol of reacted cyclooctene per mol of catalyst and hour )was calculated at about half conversion of the reaction.The catalyst was reused after washing by water and drying.The test condition was kept same to the first time on the cyclic test.2Results and Discussion2.1Synthesis and CharacterizaitonThe developed in situ confinement growth strategy is employed to the preparation of ordered mesoporous carbon support ultrasmall molybdena nanoparticles (OMC -US -MoO 3)composites (Fig.1).In the synthesis sys⁃tem ,Pluronic F127is used as the structure -directing agent (soft -template ),preformed phenolic resins is used as carbon resource ,peroxomolybdenum solution is used as precursor ,and ethanol/H 2O is used as co -solvent ,respectively.The as -made sample and product OMC -US -MoO 3composites can be obtained after heat -treatment at 100and 600℃,respectively.The mass content of MoO 3in the OMC -US -MoO 3composites can be well tuned through adjusting the amount of peroxomolybdenum precursor in the synthesis system.TGA curves (Fig.2)show that the mass fractions of MoO 3species in the OMC -US -MoO 3composites areFig.1Illustration of the construction of OMC ⁃US ⁃MoO 3composites via the in situ confinementgrowth strategy Fig.2TGA curves of the OMC ⁃US ⁃MoO 3composites with different MoO 3contents obtained afterpyrolysis at 600℃,respectivelyMass fraction of MoO 3(%):a .4;b .7;c .10;d .16;e .27.1591Vol.42高等学校化学学报4%,7%,10%,16%and 27%(Table 1),respectively ,when adjusting the amount of molybdenum precursors in the synthesis system.The mass loss below 100℃is caused by the volatilization of adsorbed water in the composites.A slight mass increasement can be detected between 100and 300℃,demonstrating the existence of trace amount of MoO 2and abundant MoO 3in the composites.The mass increasement can be attributed to the oxidation of the trace amount MoO 2.Subsequently ,the huge mass loss above 300℃can be observed attribu -ting to the remove of carbon species in the composites.The mass loss between 100and 600℃is approximate to the mass fraction of MoO 3species in the composites.The SAXS patterns [Fig.3(A )]of OMC -US -MoO 3-4and OMC -US -MoO 3-7composites show two scatteringdiffraction peaks at 0.391and 0.782nm −1,and 0.412and 0.824nm ‒1,respectively ,indexing to the (100)and (200)reflections of a hexagonal mesosturtures with space group P 6mm .With the increasement of MoO 3content ,the q values of the (100)diffraction peaks shift to 0.532,0.617,and 0.678nm −1,for samples OMC -US -MoO 3-10,OMC -US -MoO 3-16,and OMC -US -MoO 3-27,respectively.The corresponding cell parame⁃ters of five composites are calculated to be about 18.5,17.6,13.6,11.7,and 10.7nm with the increased MoO 3content ,respectively.WAXRD patterns [Fig.3(B )]of five composites all show no diffraction peaks of MoO 3phase ,suggesting the ultrasmall particle size of MoO 3nanocrystals in the frameworks.This result demonstrates that the ordered mesoporous carbon frameworks can confine the size of MoO 3nanocrystals to an ultrasmall size even at a high MoO 3content effectively.Nitrogen adsorption -desorption isotherms of five OMC -US -MoO 3composites obtained after calcined at 600℃in N 2all display representative type -Ⅳcurves with H2hysteresis loops [Fig.4(A )],in agreement with the previously reported ordered mesoporous materials [30~32].Sharp capillary condensation steps in the relative pressure (p /p 0)of 0.41―0.70are observed for five composites ,demonstrating the narrow pore size distribu⁃tion.The Brunauer -Emmett -Teller (BET )surface area and pore volume of five composites are calculated and listed on Table 1.The surface area and pore volume decrease with the increased MoO 3content ,which can be attributed to the partial destroy and disappear of pore structures.The average pore sizes of five composites are also calculated and listed on Table 1from their pore size distribution curve [Fig.4(B )]derived from the adsorption branch based on BJH model.The average pore sizes are 4.7,5.7,5.5,5.4,and 4.6nm ,Table 1Structural and textural parameters for OMC -US -MoO 3with different content Sample No.12345MoO 3content (%,mass fraction )47101627S BET /(m 2·g -1)796693652574428V /(cm 3·g -1)0.620.540.490.410.27D /nm 4.75.75.55.4 4.6Fig.3SAXS(A)and WA ⁃XRD(B)patterns of the OMC ⁃US ⁃MoO 3composites with differentMoO 3contents obtained after pyrolysis at 600℃Mass fraction of MoO 3(%):a .4;b .7;c.10;d .16;e .27.1592No.5王常耀等:原位限域生长策略制备有序介孔碳负载的超小MoO 3纳米颗粒respectively.According to the cell parameters results ,the pore walls of five composites are calculated to be 14.1,11.9,8.1,6.3,and 6.1nm ,respectively.SEM images (Fig.5)show that OMC -US -MoO 3-4and OMC -US -MoO 3-7composites own the most regular mesostructures.Notably ,the regular [100]and [110]directions can be clear observed from the SEM images of OMC -US -MoO 3-7composites [Fig.5(B )and (F )].In addition ,the mesopores are opened and no obvious big metal nanoparticles can be observed from the surface.With further increasement of MoO 3content ,the reg⁃ular mesostructures is partial destroyed.TEM images of OMC -US -MoO 3-7composites [Fig.6(A )—(C )]taken along the [100]and [110]directions manifest a well -defined 2D hexagonal mesostructures in agreement with the result of the SAXS pattern [Fig.2(A )].The lattice spacing is measured to be 0.35nm from the HRTEM image [Fig.6(D )],attributing to the (040)crystalline planes of α-MoO 3[33].The average size of MoO 3nano⁃crystals is estimated to be (4.1±1.0)nm from the size statistics diagram.The survey spectrum of the OMC -US -MoO 3-7composites shows the presence of only Mo ,O and C elements [Fig.7(A )].The high -resolution Mo 3d core level XPS spectra [Fig.7(B )]show four peaks at 230.5,232.7,233.6,and 235.9eV ,demon⁃strating the co -existence of Mo 4+and Mo 6+species [34~36].The ratio of Mo 4+/Mo 6+is calculated to be about 13%.Only a few Mo 4+signals can be detected from the spectrum ,in agreement with the TGAresults.Fig.4N 2adsorption⁃desorption isotherms(A)and pore size distributions(B)of the OMC⁃US⁃MoO 3composites with different MoO 3contents obtained after pyrolysis at 600℃Mass fraction of MoO 3(%):a .4;b .7;c.10;d .16;e .27.Fig.5SEM images of OMC⁃US⁃MoO 3composites with different MoO 3contents obtained afterpyrolysis at 600℃Mass fraction of MoO 3(%):(A)4;(B)7;(C)10;(D)16;(E)27.1593Vol.42高等学校化学学报2.2Formation Mechanism Studies Based on the above results ,we propose that the in situ confinement growth strategy show significant impact on the formation of final OMC -US -MoO 3composites.The obtained MoO 3nanocrystals show ultrasmall particle size (<5nm )and excellent dispersity on the mesoporous carbon frameworks.This structure can be retained even the mass fraction of MoO 3is increased to 27%.However ,the regular mesostructures can be partial destroyed with the increased MoO 3mass content.According to the results that no large MoO 3nanocrys⁃tals can be detected from samples obtained after pyrolysis at 600℃,the unregular mesostructures can be attributed to the uncontrollable origin co -assembly process.2.3Selective Oxidation of Cyclooctene The selective oxidation reaction of cyclooctene with high catalytic performance and stability is still highly desired.However ,the stability of active nanoparticles in catalytic reaction is a major challenge ,especially for active nanoparticles with ultra -small size.For our case ,the OMC -US -MoO 3-7composites show most regular mesostructures ,largest pore sizes ,appropriate hole wall size ,MoO 3content and dispersity.So ,the obtained OMC -US -MoO 3-7composites catalyst is selected as the catalyst for cyclooctene epoxidation.The reactions were carried out using 1,2-dichloroethane as solvent in flask with chlorobenzene as internal standard at 80℃.The OMC -US -MoO 3-7composites catalyst shows a high TOF value of 2163h ‒1which is calculated on the basis of the experimental data at 2h.Meanwhile ,a high conversion (100%)of cyclooctene ,and selectivity (>99%)to 1,2-epoxycyclooctane at 8h can also be parison with the reported heterogeneous Mo -based catalyst using similar conditions was shown in Table 2.The present OMC -US -MoO 3-7catalystshowsFig.7Survey XPS spectrum(A)and high⁃resolution XPS spectra of Mo 3d (B)for OMC⁃US⁃MoO 3⁃7composites obtained after pyrolysis at 600℃Fig.6TEM images of OMC⁃US⁃MoO 3⁃7composites obtained after pyrolysis at 600℃Viewed along the hexagonal (A )and columnar (B ,C )directions and HRTEM image (D )of a representative MoO 3nanoparticle.1594No.5王常耀等:原位限域生长策略制备有序介孔碳负载的超小MoO 3纳米颗粒a higher TOF value than MoO 3/C [8],MoO 3/SiO 2[37],Mo -MOFs [9],Mo -MCM -41[38],Mo -SBA -15[38],[Pipera⁃zinCH 2{MoO 2(Salen )}]n [39],and MNP 30-Si -inic -Mo [40]as previous reported.It should be noted that cyclooc⁃tene still gave about 18%conversion [Fig.8(A )]in the absence of catalyst owing to the presence of strong TBHP oxidants ,which is consistent with previous reports [41,42].Further ,two other substrates ,cyclohexene and styrene were also tested under the same conditions to test the versatility of OMC -US -MoO 3-7as an epoxida⁃tion catalyst.Surprisingly ,the conversion of cyclohexene to 1,2-epoxyclohexane can reach 54%in 8h.Inaddition ,the conversion of styrene to styrene oxide can reach 95%in 36h ,respectively (Fig.S1,see the Sup⁃porting Information of this paper ).Beside the efficient conversion of catalyst and high TOF values ,the stability of catalyst is also very impor⁃tant ,especially for heterogeneous catalysis.Here ,the hot filtration test was used to assess the presence of active Mo species in solution.When the reaction lasted for 2h ,we removed the catalyst by hot filtration and let the mother liquid for reacting another 6h.The results showed that there was only a slight increase in con⁃version [Fig.8(A )],which is proof of a heterogeneous catalysis.For the recycling study ,cyclooctene epoxida⁃tion was performed maintaining the same reaction conditions except using the recovered catalyst.It can be clearly found that obvious changes are undetected for catalytic performance after five runs [Fig.8(B )].It indi⁃cates that ultrasmall MoO 3nanoparticles supported on ordered mesoporous carbon is highly stable and can be reused ,demonstrates its potential for industrial applications.The high conversion ,selectively ,and the TOF value for the cyclooctene epoxidation reaction can be attributed to the unique structure of the OMC -US -MoO 3-7composites.The high surface area ,volume ,andTable 2Calculating TOF value for epoxidation of cyclooctene and comparing with other catalysts *Catalyst OMC -US -MoO 3-7MoO 3/C MoO 3/SiO 2Mo -MOFs Mo -MCM -41Mo -SBA -15[PiperazinCH 2{MoO 2(Salen )}]n MNP 30-Si -inic -MoTime/h 2267331224Conv.(%)5280909397999546Epoxide sel.(%)>9910010099959398100TOF/h -1216353[8]72[35]270[9]22[36]40[36]16[37]2[38]*.TOF values(mol of reacted cyclooctene per mol of catalyst and hour)were calculated at abouthalf conversion of the reaction.Fig.8Time course plots of cyclooctene epoxidation(A)and reusability(B)by using OMC⁃US⁃MoO 3⁃7com⁃posites as catalystReaction conditions :40.0mmol of cyclooctene ,40.0mmol of 5.5mol/L TBHP in decane ,10mg of OMC -US -MoO 3-7catalyst (0.0048mmol/L of MoO 3),6.0g of 1,2-dichloroethane as solvent ,and 15.0mmol of chlorobenzene as internalstandard.The reaction temperature is 80℃.15951596Vol.42高等学校化学学报uniform mesopores can not only enrichment the reaction substrate but also in favor to the diffusion of sub⁃strates.The ultrasmall MoO3nanocrystals size and its excellent dispersity in the frameworks can expose more active sites.All these features are beneficial to the rapid conversion of substrate molecular with high selective⁃ly and conversion.3ConclusionsIn summary,an in situ confinement growth strategy was developed to the construction of ordered mesopo⁃rous carbon support ultrasmall molybdena nanoparticles(OMC-US-MoO3)composites.Ordered mesoporous carbon was used as an effective matrix to in situ confine the growth of MoO3nanocrystals.The obtained MoO3 nanocrystals show ultrasmall particle size(<5nm)and excellent dispersity on the mesoporous carbon frame⁃works.In addition,a serious of OMC-US-MoO3composite can be obtained with controllable specific surface areas(428―796m2/g),pore volumes(0.27―0.62cm3/g),MoO3contents(4%―27%,mass fraction)and uniform pore size(4.6―5.7nm).The mesostructures can be retained even the MoO3content as high as27%. As a typical example,the obtained sample with7%MoO3(denoted as OMC-US-MoO3-7)shows largest pore size,smallest thickness of pore wall and most regular mesostructures.When being used as a catalyst,the OMC-US-MoO3-7exhibits an excellent catalytic activity(2163h−1for TOF)for selective oxidation of cyclooc⁃tene with a high stability.Supporting Information:/CN/10.7503/cjcu20200303.This paper is supported by the National Natural Science Foundation of China(No.21975050),the Natio⁃nal Key Research and Development Program of China(Nos.2016YFA0204000,2018YFE0201701)and China Postdoctoral Science Foundation(No.2019M651342).References[1]Xi Z.,Zhou N.,Sun Y.,Li K.,Science,2001,292(5519),1139—1141[2]Kamata K.,Yonehara K.,Sumida Y.,Yamaguchi K.,Hikichi S.,Mizuno N.,Science,2003,300(5621),964—966[3]Liu B.,Wang P.,Lopes A.,Jin L.,Zhong W.,Pei Y.,Suib S.L.,He J.,ACS Catal.,2017,7(5),3483—3488[4]Bujak P.,Bartczak P.,Polanski J.,J.Catal.,2012,295,15—21[5]Dou J.,Zeng H.C.,J.Phys.Chem.C,2012,116(14),7767—7775[6]Xiao L.P.,Wang S.,Li H.,Li Z.,Shi Z.J.,Xiao L.,Sun R.C.,Fang Y.,Song G.,ACS Catal.,2017,7(11),7535—7542[7]Shetty M.,Murugappan K.,Green W.H.,Román⁃Leshkov Y.,ACS Sustainable Chem.Eng.,2017,5(6),5293—5301[8]Doke D.S.,Umbarkar S.B.,Gawande M.B.,Zboril R.,Biradar A.V.,ACS Sustainable Chem.Eng.,2016,5(1),904—910[9]Noh H.,Cui Y.,Peters A.W.,Pahls D.R.,Ortuño M.A.,Vermeulen N.A.,Cramer C.J.,Gagliardi L.,Hupp J.T.,Farha O.K.,J.Am.Chem.Soc.,2016,138(44),14720—14726[10]Luo Z.,Miao R.,Huan T.D.,Mosa I.M.,Poyraz A.S.,Zhong W.,Cloud J.E.,Kriz D.A.,Thanneeru S.,He J.,Adv.Energy Mater.,2016,6(16),1600528[11]Brezesinski T.,Wang J.,Tolbert S.H.,Dunn B.,Nat.Mater.,2010,9(2),146—151[12]Chen L.,Jiang H.,Jiang H.,Zhang H.,Guo S.,Hu Y.,Li C.,Adv.Energy Mater.,2017,7(15),1602782[13]Hosono K.,Matsubara I.,Murayama N.,Woosuck S.,Izu N.,Chem.Mater.,2005,17(2),349—354[14]Wang L.,Gao P.,Zhang G.,Chen G.,Chen Y.,Wang Y.,Bao D.,Eur.J.Inorg.Chem.,2012,2012(35),5831—5836[15]Fernandes C.I.,Capelli S.C.,Vaz P.D.,Nunes,C.D.,Appl.Catal.A:Gen.,2015,504,344—350[16]da Palma Carreiro E.,Burke A.J.,J.Mol.Catal.A:Chem.,2006,249(1),123—128[17]Chen W.,Pei J.,He C.T.,Wan J.,Ren H.,Zhu Y.,Wang Y.,Dong J.,Tian S.,Cheong W.C.,Angew.Chem.Int.Ed.,2017,56(50),16086—16090[18]Solar J.,Derbyshire F.,De Beer V.,Radovic L.R.,J.Catal.,1991,129(2),330—342[19]Lee S.H.,Kim Y.H.,Deshpande R.,Parilla P.A.,Whitney E.,Gillaspie D.T.,Jones K.M.,Mahan A.H.,Zhang S.,Dillon A.C.,Adv.Mater.,2008,20(19),3627—3632[20]Tavasoli A.,Karimi S.,Shoja M.,Int.J.Ind.Chem.,2013,4(1),211597 No.5王常耀等:原位限域生长策略制备有序介孔碳负载的超小MoO3纳米颗粒[21]Wang C.,Zhao Y.,Zhou L.,Liu Y.,Zhang W.,Zhao Z.,Hozzein W.N.,Alharbi H.M.S.,Li W.,Zhao D.,J.Mater.Chem.A,2018,6(43),21550—21557[22]Wang C.,Wan X.,Duan L.,Zeng P.,Liu L.,Guo D.,Xia Y.,Elzatahry A.A.,Li W.,Zhao D.,Angew.Chem.Int.Ed.,2019,58(44),15863—15868[23]Zhang P.,Zhang J.,Dai S.,Chem.Eur.J.,2017,23(9),1986—1998[24]Reyes P.,Borda G.,Gnecco J.,Rivas B.L.,J.Appl.Polym.Sci.,2004,93(4),1602—1608[25]Qin M.,Liu M.,Zhang Q.,Li C.,Liang S.,J.Appl.Polym.Sci.,2013,128(1),642—646[26]Zhang F.,Hu H.,Zhong H.,Yan N.,Chen Q.,Dalton Trans.,2014,43(16),6041—6049[27]Meng Y.,Gu D.,Zhang F.,Shi Y.,Yang H.,Li Z.,Yu C.,Tu B.,Zhao D.,Angew.Chem.Int.Ed.,2005,44(43),7053—7059[28]Wang S.,Zhao Q.,Wei H.,Wang J.Q.,Cho M.,Cho H.S.,Terasaki O.,Wan Y.,J.Am.Chem.Soc.,2013,135(32),11849—11860[29]Chen J.,Burger C.,Krishnan C.V.,Chu B.,J.Am.Chem.Soc.,2005,127(41),14140—14141[30]Liu R.,Shi Y.,Wan Y.,Meng Y.,Zhang F.,Gu D.,Chen Z.,Tu B.,Zhao D.,J.Am.Chem.Soc.,2006,128(35),11652—11662[31]Dong W.,Sun Y.,Lee C.W.,Hua W.,Lu X.,Shi Y.,Zhang S.,Chen J.,Zhao D.,J.Am.Chem.Soc.,2007,129(45),13894—13904[32]Liu R.,Ren Y.,Shi Y.,Zhang F.,Zhang L.,Tu B.,Zhao D.,Chem.Mater.,2008,20(3),1140—1146[33]Patnaik S.,Swain G.,Parida K.,Nanoscale,2018,10(13),5950—5964[34]Qin P.,Fang G.,Cheng F.,Ke W.,Lei H.,Wang H.,Zhao X.,ACS Appl.Mater.Interfaces,2014,6(4),2963—2973[35]Ji W.,Shen R.,Yang R.,Yu G.,Guo X.,Peng L.,Ding W.,J.Mater.Chem.A,2014,2(3),699—704[36]Qin P.,Fang G.,Ke W.,Cheng F.,Zheng Q.,Wan J.,Lei H.,Zhao X.,J.Mater.Chem.A,2014,2(8),2742—2756[37]Chandra P.,Doke D.S.,Umbarkar S.B.,Biradar A.V.,J.Mater.Chem.A,2014,2(44),19060—19066[38]Bakala P.C.,Briot E.,Salles L.,Brégeault J.M.,Appl.Catal.A:Gen.,2006,300(2),91—99[39]Bagherzadeh M.,Zare M.,J.Coord.Chem.,2013,66(16),2885—2900[40]Fernandes C.I.,Carvalho M.D.,Ferreira L.P.,Nunes C.D.,Vaz P.D.,anomet.Chem.,2014,760,2—10[41]Muylaert I.,Musschoot J.,Leus K.,Dendooven J.,Detavernier C.,Van Der Voort P.,Eur.J.Inorg.Chem.,2012,2012(2),251—260[42]El⁃Korso S.,Bedrane S.,Choukchou⁃Braham A.,Bachir R.,RSC Adv.,2015,5(78),63382—63392(Ed.:V,K)锂金属负极亲锂骨架的研究进展Recent Progress of Lithiophilic Host for Lithium Metal Anode詹迎新,石鹏,张学强,魏俊宇,张乾魁,黄佳琦ZHAN Yingxin,SHI Peng,ZHANG Xueqiang,WEI Junyu,ZHANG Qiankui,HUANG Jiaqi∗Chem.J.Chinese Universities,2021,42(5),1569 1580研究论文(Article)超薄骨架有序介孔CdS/NiS的制备及光催化产氢性能Ordered Mesoporous NiS-loaded CdS with UltrathinFrameworks for Efficient Photocatalytic H2Production杨晓梅,吴强,郭茹,叶凯波,薛屏,王晓中,赖小勇YANG Xiaomei,WU Qiang,GUO Ru,YE Kaibo,XUE Ping∗,WANG Xiaozhong,LAI Xiaoyong∗Chem.J.Chinese Universities,2021,42(5),1581 1588原位限域生长策略制备有序介孔碳负载的超小MoO3纳米颗粒In situ Confinement Growth Strategy for Ordered MesoporousCarbon Support Ultrasmall MoO3Nanoparticles王常耀,王帅,段林林,朱晓航,张兴淼,李伟WANG Changyao,WANG Shuai,DUAN Linlin,ZHU Xiaohang,ZHANG Xingmiao,LI Wei∗Chem.J.Chinese Universities,2021,42(5),1589 1597全固态锂金属电池多物理场耦合下的电化学过程仿真模拟Simulation of the Electrochemistry Process with the Coupling ofMultiple Physical Fields for All-solid-state Lithium Batteries孙哲韬,何英杰,陈邵杰,聂璐,黄缘齐,刘巍SUN Zhetao,HE Yingjie,CHEN Shaojie,NIE Lu,HUANG Yuanqi,LIU Wei∗Chem.J.Chinese Universities,2021,42(5),1598 1609Ⅴ。

应用化学专业英语1单元翻译

应用化学专业英语1单元翻译

应用化学专业英语1单元翻译第一篇:应用化学专业英语1单元翻译1.Chemistry can be broadly defines as the science of molecules and their transformations.化学可以广泛地定义为科学的分子和他们的转换。

化学可以广泛地定义为科学的分子和他们的转换。

与数学不同,化学比人类更久远。

生命的出现和人类生活在我们地球上都最可能是特殊化学过程的结果。

化学过程存从古至今存在人们的生活中。

•最初,这些过程不受我们的控制,例如,果汁的发酵,肉和鱼的腐烂,木材的燃烧。

后来,我们学着控制化学过程,用它们来准备一系列不同的产品例如食物。

在化学的发展中,四个阶段是突出的:史前化学,希腊化学,炼金术和科学化学。

The early beginnings of chemistry were clearly motivated by practical needs of people.早期的化学显然是出于实际的需要。

火的发现为远古人提供了第一个机会去实现控制化学反应过程。

他们学会制备铜制物品,铜和其它材料是现成的。

.由于化学过程的使用早于人们的书写,因而没有书面记录有关它们的化学技巧。

可以判断他们的化学能力只有从考古的发现的各个手工艺品。

正如早期的数学发展,清楚的预示着实际需求影响着化学的发展。

但化学和数学在这个阶段可能没有互相影响。

如果它们影响了,但是没有记录证明这个。

Greek chemistry was based mainly on speculation rather than on experiment.希腊化学主要基于猜测而不是实验。

这是所有古代希腊化学的一个共同特征。

古代希腊化学家实际是希腊哲学家。

所以不足为奇的是希腊人思考比实验更有兴趣。

实际上他们很少进行实验以外的思维实验。

对于数学来说这是一个好方法,但没有一个人把它推荐在物理、化学或生物科学上。

亚胺制备邻氨基苯甲酸生产工艺流程

亚胺制备邻氨基苯甲酸生产工艺流程

亚胺制备邻氨基苯甲酸生产工艺流程英文回答:Preparation of Anthranilic Acid from Imines.Anthranilic acid is an important intermediate in the synthesis of various pharmaceuticals, dyes, and pesticides. It can be prepared from imine, which is a condensation product of an amine and an aldehyde or ketone. The imine is then hydrolyzed to form the corresponding amine and carboxylic acid.The reaction scheme for the preparation of anthranilic acid from imine is as follows:R-CH=NR' + H2O -> R-COOH + R'-NH2。

Where R and R' are alkyl or aryl groups.The hydrolysis of imine can be carried out in acidic orbasic conditions. In acidic conditions, the imine is protonated and then attacked by water to form the amine and carboxylic acid. In basic conditions, the imine is deprotonated and then attacked by water to form the amine and carboxylic acid.The choice of reaction conditions depends on the imine and the desired product. For example, if the imine is unstable in acidic conditions, then it may be necessary to use basic conditions to hydrolyze it.The following are some of the advantages of using imine as a starting material for the preparation of anthranilic acid:Imines are relatively easy to prepare.The hydrolysis of imine is a high-yielding reaction.The reaction conditions are mild.中文回答:亚胺合成邻氨基苯甲酸工艺流程。

化学及化工专业词汇英语j-o-

化学及化工专业词汇英语j-o-

化学及化工专业词汇英语翻译j-oj acid j 酸jacket 夹套jacket cooling 套管冷却jacob cell 雅讣电池jacobsen rearrangement 雅可布森重排jade 硬玉jadeite 硬玉jalap 贾拉普japan 黑漆jasmin oil 茉莉花油jasmone 茉莉酮jasper 碧玉javel water 爪维尔水jaw breaker 腭式碎石机jaw crusher 腭式碎石机jelly 凝胶jena glass 耶拿玻璃jervine 介藜芦胺jet 喷射jet blower 喷射式通风机jet compressor 喷气压缩机jet condenser 喷水凝汽器jet fuel 喷气发动机燃料jet pump 喷射泵jewel 宝石jig sieve 振动筛joule 焦耳joule effect 焦耳效应joule thomson effect 焦耳汤姆森效应joule's law 焦耳定律juglone 胡桃酮julian tube 凯撒管junker's calorimeter 容克量热计jute 黄麻juvenile gas 初生气juvenile water 初生水k acid k 酸k meson k 介子kali fusion 钾熔融kalimeter 碳酸计kallikrein 舒血管素kanamycin 卡那霉素kaolin 瓷土kaolin clay 高岭土kaolinite 高岭石kaolinization 高岭土化kapok oil 爪哇木棉油karaya gum 剌梧桐屎karl fischer method 卡尔费歇尔法karl fischer's reagent 费氏试剂karyokinesis 核分裂karyolysis 核溶解karyoplasm 核质kata thermometer 卡他温度计kauri butanol value 贝壳杉脂丁醇值kauri gum 栲里松脂kauri resin 栲里松脂keene's cement 金纳水泥keesom relationship 基朔关系kelp 海草灰kelvin's temperature 开氏温度keratin 角蛋白keratin plastics 角质塑料kermes 胭脂虫粉kermesite 红锑矿kerogen 油母质kerosene 煤油kerosine 煤油ketene 乙烯酮ketene lamp 乙烯酮灯ketimine 酮亚胺keto acid 酮酸keto enol tautomerism 酮烯醇互变异构keto form 酮式ketoadipic acid 酮己二酸ketoalcohol 酮醇ketocapric acid 己酮酸ketoglutaric acid 氧代戊二酸ketoheptose 庚酮糖ketol 酮醇ketone 酮ketone decomposition 酮分解ketone group 酮基ketone musk 香酮ketone resin 酮尸ketonic ester 酮酯ketonisation 酮化ketose 酮糖ketoxime 酮肟key component 限界组分kieselguhr 硅藻土kieserite 水镁矾killed steel 冷静钢kiln 炉kinase 激酶kindling temperature 着火温度kinematic viscosity 运动粘度kinematical theory of diffraction 运动学的衍射论kinescope 显象管kinetic chain length 动力学链长kinetic current 反应电流kinetic energy 动能kinetic friction 动摩擦kinetic molecular theory 分子运动理论kinetic theory 动力学理论kinetic theory of gases 气体分子运动论kinetics of polymerization 聚合动力学kinetin 激动素king's yellow 雄黄kipp's apparatus 基普气发生器kipp's gas generator 基普气发生器kirchhoff's law 基尔霍夫定律kitol 鲸醇kjeldahl flask 基耶达尔氏测氮瓶kjeldahl method 基耶达尔法kjellin furnace 开林电炉kneader 捏和机kneading 捏和knife edge of balance 天平的支棱knock intensity 爆震强度knocking 爆震knoevenagel reaction 诺文葛耳反应knorr synthesis 克诺尔合成法koch's acid 柯赫酸kojic acid 曲酸kolbe schmitt reaction 科尔伯施密特反应korean paper 朝鲜纸kotoite 粒镁硼石kozeny carman's equation 康采尼卡曼方程krafft point 克拉夫特点kraft paper 牛皮纸kraft pulp 牛皮纸浆krypton 氪kyanite 蓝晶石labarraque's solution 拉巴腊克氏溶液labelled atom 示踪原子labile equilibrium 不稳平衡labile form 不稳形lability 不稳定性laboratory 实验室laboratory scale 实验室规模laboratory test 实验室试验lac 紫胶lac dye 紫胶染料lachrymator 催泪剂lacmoid 间苯二酚蓝lacquer 漆lacquer diluent 漆稀释剂lacquer enamel 瓷漆lacquering 涂漆lactacidogen 乳酸精lactalbumin 乳清蛋白lactam 乳胺lactamide 乳酸胺lactase 乳糖酶lactate 乳酸盐lactic acid 乳酸lactic acid bacteria 乳酸菌lactic acid fermentation 乳酸发酵lactic anhydride 乳酸酐lactide 交酯lactim 内酰亚胺lactobutyrometer 乳脂计lactoflavin 乳黄素lactogenic hormone 促乳泌素lactoglobulin 乳球朊lactometer 乳比重计lactone 内酯lactone bond 内酯键lactonic ring 内酯环lactonitrile 乳腈lactonization 内酯化lactophenine 乳吩咛胺lactoscope 乳酪计lactose 乳糖ladder polymer 梯形聚合物lagrange's equation of motion 拉格朗日运动方程lagrange's method of undetermined multipliers 拉格朗日不定乘子法laguerr's polynomial 拉盖尔多项式lake 色淀颜料lake red c 色淀红clalande cell 拉兰电池lambert beer's law 朗伯波特比尔定律lambert's law 朗伯特定律lamella 薄板lamina 薄板laminar film 片状膜laminar flow 层流laminar furnace 层怜laminate 层压材料laminated coal 叠层煤laminated glass 夹层玻璃laminated paper 层压纸laminated wood 胶合板lamination 层压lamp 灯lamp black 灯黑lamp oil 灯油lamp test 灯泡试验lanatoside 毛花甙langbeinite 无水钾镁矾langmuir's adsorption isotherm 朗格缪尔吸附等温线lanolin 羊毛脂lanoline 羊毛脂lanosterol 羊毛醇lanthanide 镧系元素lanthanide contraction 镧系收缩lanthanoid 镧系元素lanthanum 镧lanthanum acetate 乙酸镧lanthanum bromate 溴酸镧lanthanum bromide 溴化镧lanthanum carbonate 碳酸镧lanthanum chloride 氯化镧lanthanum oxide 氧化镧lanthionine 羊毛硫氨酸lap welding 叠式焊接lapachoic acid 拉帕醇lapachol 拉帕醇lapidification 石化酌laplace equation 拉普拉斯方程laplace transformation 拉普拉斯变幻lard 猪脂large aromatic molecule 大芳香族分子large scale gas chromatography 制备级气相色谱法laser 激光last heat of dissolution 溶解终热latence 埋伏latency 埋伏latent catalyst 埋伏催化剂latent heat 潜热latent heat of fusion 熔化潜热latent heat of sublimation 升华热latent image 潜像latent period 埋伏期latent valency 潜化合价lateral axis 横轴线lateral chain 侧链lateral face 侧面lateral magnification 横扩大率lateral secretion 侧分泌laterite 红土latex 胶乳latex cement 胶乳结合剂latex paint 胶乳漆latex thickener 胶乳增稠剂latexometer 胶乳比重计lather 肥皂泡lathering number 起泡值lathering soap 泡沫lattice constant 晶格常数lattice defect 点阵缺陷lattice distance 晶格间距lattice energy 晶格能lattice model 点阵模型lattice plane 晶格面laudanidine 劳丹尼定laudanine 劳丹碱laudanosine 劳丹素laue method 劳厄法laue photograph 劳厄照相laughing gas 笑气laundry soap 家用皂lauraldehyde 月桂醛laurate 月桂酸盐laurel 月桂laurel oil 月桂油lauric acid 月桂酸lauroleate 月桂酸盐lauroleic acid 月桂烯酸lauroyl chloride 月桂酰氯lauroyl peroxide 过氧化月桂酰lauryl alcohol 月桂醇lauryl chloride 月桂基氯lauryl mercaptan 月桂硫醇lauryl methacrylate 甲基丙烯酸月桂酯lava 熔岩lavazeck viscometer 拉巴切克粘度计lavender oil 熏衣草油lavender water 熏衣水law of chemical equivalent 化学当量定律law of conservation and conversion of energy 能量守恒及能量转换定律law of conservation of energy 能量守恒律law of conservation of mass 质量守恒定律law of conservation of momentum 动量守恒定律law of constant proportion 定比律law of corresponding states 对应态原理law of definite proportion 定比律law of equipartition of energy 能量均分律law of gaseous reaction 气体反应定律law of ideal gases 理想气体定律law of independent ionic mobilities 独立离子怜定律law of ionic strength 离子强度定律law of isomorphism 类质同晶定律law of mass action 质量酌定律law of multiple proportions 倍比律law of partition 分配定律law of photochemical equivalent 光化学当量定律law of radioactive decay 放射性蜕变定律law of reciprocal proportion 互比定律law of reciprocity 互反律law of velocity distribution 速度分布定律lawrencium 铹laxative 轻泻剂layer built cell 积层电池layer lattice 层形点阵layer structure 层状构造lazulite 天蓝石le chatelier braun's principle 勒夏特利埃布劳董理leachability 可浸出性leachate 浸出液leaching 浸析leaching agent 溶浸剂lead 铅lead accumulator 铅蓄电池lead acetate 醋酸铅lead arsenate 砷酸铅lead azide 叠氮化铅lead bath 铅浴lead carbonate 碳酸铅lead chamber 铅室lead chamber process 铅室法lead chloride 氯化铅lead chromate 铬酸铅lead compound 铅化合物lead cyanamide 氰氨化铅lead cyanide 氰化铅lead dioxide 二氧化铅lead glance 方铅矿lead glass 铅玻璃lead glaze 铅釉lead hydrogen citrate 氢柠檬酸铅lead hydroxide 氢氧化铅lead lining 铅内衬lead linoleate 亚油酸铅lead molybdate 钼酸铅lead nitrate 硝酸铅lead oxide 氧化铅lead paper 乙酸铅试纸lead peroxide 过氧化铅lead poisoning 铅中毒lead resinate 尸酸铅lead silicate 硅酸铅lead stearate 硬脂酸铅lead storage battery 铅蓄电池lead suboxide 一氧化二铅lead sulfate 硫酸铅lead sulfide 硫化铅lead susceptibility 受铅性lead telluride 碲化铅lead tetraacetate 醋酸高铅lead tetrachloride 四氯化铅lead tungstate 钨酸铅lead vanadate 钒酸铅leaded gasoline 加铅汽油leaf condenser 箔电容器leaf filter 叶片式过滤器leak detector 漏电指示器leak test 泄漏试验leakage 泄漏leakage current 漏电流lean coal 贫煤lean gas 贫气lean lime 贫石灰leather 皮革leather substitute 人造革lecithase 卵磷脂酶lecithin 卵磷脂lecithinase 卵磷脂酯leclanche cell 勒克朗谢电池ledeburite 菜德布尔体lederer manasse reaction 菜德勒曼讷斯反应legumin 豆球蛋白lehre 退火炉lemon oil 柠檬油lemongrass oil 柠檬草油lenacil 环草定length 长度lens 透镜lenticular film 凹凸式胶片leonite 钾镁矾lepidine 勒皮啶lepidolite 鳞云母lethal dose 致死量leucic acid 白氨酸leucine 白氨酸leucite 白榴石leuckart reaction 洛卡特氐反应leucoalizarin 去氧茜素leucobase 路易克碱leucocompound 无色化合物leucocyte 白血球leucocytolysin 白细胞溶素leucoscope 光学高温计leucosol 白色溶胶levan 果聚糖level dyeing 均匀染色level gage 液面计level meter 液面仪leveling 均匀染色leveling agent 匀染剂leveling tube 水准管levigation 水磨levo form 左旋体levo rotary matter 左旋性物质levorotation 左旋性levorotatory compound 左旋化合物levulinaldehyde 乙酰丙醛levulinic acid 乙酰丙酸levulosan 左旋聚糖levulose 果糖lewis langmuir's theory of valency 路易斯兰格穆尔原子价理论lewisite 路易氏气liberation 游离lichen starch 地衣多糖lichenase 地衣聚糖酶lichenin 地衣多糖licopene 茄玉红lidocaine 利多卡因liebermann's reaction 李伯曼反应liebig condenser 李比希氏冷凝器liesegang ring 李四光环life of decay 半衰期lifetime 寿命lift 水头ligancy 配位数ligand 配位体ligand field 配位场ligand field absorption band 配位场汲取带ligand field theory 配位场理论ligand membrane 配位体膜ligand migration reaction 配位体移动反应light alloy 轻合金light burned magnesia 轻质煅烧镁氧light emitting diode 发光二极管light end 轻馏分light fastness 耐光性light filter 滤光器滤光片light fire brick 轻质耐火砖light fog 光灰雾light induced proton pump 光诱致质子泵light metal 轻金属light meter 曝光计light oil 轻油light pressure 光压light quantum 光子light rare earth element 轻稀土元素light resistance 耐光性light ruby silver 淡红银矿light scattering method 光散射法light scattering photometer 光散射光度计light sensitivity 感光度light soils 轻质土light source 光源light velocity 光速light weight concrete 轻质混凝土lignification 木质化lignin 木素lignocaine 利多卡因lignocellulose 木质纤维素lignoceric acid 廿四酸lignosulfonic acid 木素磺酸ligroin 里格苦因lime 石灰lime burning 煅烧石灰lime cream 石灰乳lime hydrate 消石灰lime kiln 石灰窑lime kilning 煅烧石灰lime milk 石灰乳lime mortar 石灰浆lime nitrate 硝酸钙lime nitrogen 石灰氮lime oil 梨莓油lime pozzolanic cement 石灰火山灰水泥lime rosin 石灰松香lime salpeter 硝酸钙lime saturation degree 石灰饱和度lime silica ratio 石灰硅石比lime slag cement 石灰炉渣水泥lime slaker 石灰熟化器lime soap 石灰皂lime sulfur mixture 石硫合剂lime water 石灰水limestone 石灰石liming 用石灰处理limit dextrin 有限糊精limit of error 误差极限limit of identification 证实限度limit of inflammability 可燃限度limiting concentration 极限浓度limiting current 极限电流limiting current density 极限电淋度limiting value 极限值limonene 二戊烯limonite 褐铁矿limpidity 透迷linaloe oil 沉香油linalool 里哪醇linalyl acetate 醋酸里哪酯lindane 林丹linde air liquefier 林德空气液化器line density 线密度line spectrum 线性光谱line width 线宽度linear accelerator 直线加速器linear condensation polymer 线型缩合聚合物linear differential equation 线性微分方程linear expansion 线膨胀linear expansivity 线膨胀性linear macromolecule 线型大分子linear molecule 线型分子linear ordinary differential equation of first order 一阶线性常微分方程linear polymer 线状聚合物linear transformation 线性变幻linear viscoelasticity 线性粘弹性lining 内衬lining brick 砌壁砖linkage 键合linking 键合linnaeite 硫钴矿linoleic acid 亚麻仁油酸linolenic acid 亚麻酸linoleum 油地毡linoleum cement 油毡胶粘剂linoleum oil 漆布油linolic acid 亚麻仁油酸linolin 亚麻精linoxylin 氧化亚麻油linoxyn 氧化亚麻油linseed oil 亚麻子油lint 皮棉linter 棉绒lipase 脂肪酶lipid 脂质lipid metabolism 脂类代谢lipid peroxide 脂类过氧化物lipoamino acid 脂氨基酸lipochrome 脂色素lipoic acid 硫辛酸lipolysis 脂类分解lipoprotein 脂蛋白liposome 脂质体lipoxidase 脂肪氧化酶liquefaction 液化liquefaction of air 空气液化liquefaction of coal 煤的液化liquefied gas 液化气liquefied natural gas 液化天然气liquefied petroleum gas 液化石油气liquid 液体liquid air 液态空气liquid ammonia 液态氨liquid calorimeter 液体量热计liquid carbon dioxide 液态二氧化碳liquid chlorine 液态氯liquid chromatography 液相谱liquid cooling 液体冷却liquid crystal 液晶liquid crystalline polymers 液晶聚合物liquid culture 液体培养liquid cyclone 湿式旋风除尘器liquid drier 液体催干剂liquid drop model 液滴模型liquid fertilizer 液体肥料liquid film technology 液膜技术liquid filter 液体过滤器liquid fuel 液体燃料liquid gold 金水liquid grease 液体钙基脂liquid heat exchanger 液体热交换器liquid hydrocarbon 液烃liquid insulator 液体绝缘体liquid ion exchanger 液体离子交换剂liquid junction cell 液体接界电池liquid junction potential 液体接界电势liquid level indicator 液面仪liquid liquid chromatography 液液色谱法liquid liquid extraction 液液提取liquid liquid partition chromatography 液液分配色谱法liquid manometer 液体压力计liquid medium 液体培养基liquid membrane 液体膜liquid nitrogen 液态氮liquid oxygen 液态氧liquid oxygen explosive 液氧炸药liquid paraffin 液体石蜡liquid phase 液相liquid phase cracking 液相分解liquid phase cracking process 液相过程liquid phase hydrogenation 液相氢化liquid rubber 液态橡胶liquid seal 液封liquid soap 液体肥皂liquid solid chemical reaction 液固化学反应liquid solid equilibrium 固液平衡liquid sulfur dioxide benzene process 液态二氧化硫苯抽提过程liquid thermometer 液体温度计liquidus 液线liquor ratio 液比liquorice 甘草litharge 密陀僧lithia porcelain 氧化锂瓷lithium 锂lithium aluminium hydride 氢化铝锂lithium aluminium hydride reduction 氢化铝锂还原lithium carbonate 碳酸锂lithium chlorate 氯酸锂lithium chloride 氯化锂lithium hydroxide 氢氧化锂lithium nitrate 硝酸锂lithium oxide 氧化锂lithium silicate 硅酸锂lithium sulfate 硫酸锂lithium tartrate 酒石酸锂lithochemistry 岩石化学lithocholic acid 石胆酸lithogeochemistry 岩石地球化学lithographic ink 石印墨lithographic varnish 石印清漆lithography 石印术lithol red 立遂lithophile element 亲岩元素lithopone 立德粉lithosphere 岩石圈litmus 石蕊litmus paper 石蕊纸live steam 直接蒸汽liver oil 肝油living coordination polymerization 活性配位聚合living polymer 活性聚合物lixiviation 浸析load test 负荷试验loading hopper 进料漏斗loading material of rubber 橡胶填料loam 亚粘土lobeline 洛贝林local analysis 局部分析local cell 局部电池local corrosion 局部腐蚀local current 局部电流local equilibrium 局部平衡local magnetic moment 局部磁矩locally limit theorem 局部极限定理lode 矿脉loess 黄土log mean temperature difference 对数平均温差logarithmic function 对数函数logarithmic mean 对数平均logic element 逻辑元件logical circuit 逻辑电路logwood 苏木lone pair 非共有电子对long flame coal 长焰煤long oil varnish 长油性清漆long tube vertical evaporator 长管竖式蒸发器longitudinal flow reactor 纵向连续反应器loop strength ratio 钩接强力比lorentz's force 洛伦兹力lorenz lorentz's formula 洛伦茨洛伦兹公式loretin 试铁灵loss 损失loss angle 损耗角loss of weight 失重lossen reaction 洛森反应lost heat 废热loudness 音量lovibond tintometer 拉维邦德油品色度计low alloy 低合金low angle scattering of x ray x线小角散射low energy neutron 低能中子low expansion glass 低膨胀玻璃low fired porcelain 低温瓷器low frequency induction furnace 低频感应电炉low grade bituminous coal 低级沥青炭low heat cement 低热水泥low melting glass 低熔点玻璃low molecular weight hydrocarbon 低分子量烃low polymer 低聚物low pressure gauge 低压计low pressure molding 低压模塑low pressure resin 低压尸low pressure tyre 低压轮胎low temperature carbonization 低温干馏low temperature coke 低温焦炭low temperature fractionation 低温精馏low temperature polymerization 低温聚合low temperature processing 低温分开法low temperature resistance 耐寒性low temperature tar 低温焦油lower calorific power 低热值lower calorific value 低热值lower homologue 低级同系物lowering of melting point 熔点降低loxygen 液氧lubricant 润滑剂lubricating grease 润滑脂lubricating oil 润滑油lubricating property 润滑性lubrication 润滑lucas reagent 卢卡斯试药luciferase 荧光素酶luciferin 荧虫光素lumen 流luminance temperature 发光温度luminescence 发光luminescence analysis 发光分析luminescence center 发光中心luminescent dye 荧光染料luminescent lamp 荧光灯luminescent plastics 发光塑料luminescent screen 荧光屏luminol 鲁米诺luminophore 发光体luminosity 亮度luminous flame 光焰luminous flux 光束luminous paint 发光油漆luminous pigment 发光颜料lumisterol 光照甾醇lump coal 块煤lump coke 块焦炭lunge's test 伦格试验lupanine 羽扇烷宁lupinidine 司巴丁lurgi low temperature carbonization oven 鲁奇的低温焦化烘炉luster 光泽lusterless paint 无光漆lutecium 镥lutein 叶黄素luteo salt 黄络盐luteol 黄示醇luteolin 黄色素lutetium 镥lutidine 卢剔啶lux 勒克斯luxmeter 照度计lyase 裂合酶lycopene 番茄烯lycopin 番茄烯lycopodium 石松子lycopodium spores 石松子lycoremine 加兰他敏lye 碱液lyogel 液凝胶lyolysis 液解lyophilic 亲液的lyophilic colloid 亲液胶体lyophilic polymer 亲液性聚合体lyophilization 冻干lyophobic 疏水的lyophobic colloid 蔬液胶体lyosol 液溶胶lyotropic liquid crystal 易溶液晶lyotropic series 感胶离子序列lysergic acid 赖瑟酸lysine 赖氨酸lysol 来苏lysosomotropic drug 擒酶体药lysozyme 溶菌酶lysyloxidase 赖氨酰氧化酶lyxonic acid 来苏糖酸lyxose 来苏糖m acid m 酸m.w.分子量macaroni rayon 空心人造丝macassar gum 琼脂mace oil 肉豆蔻油maceration 浸渍machine bleaching 机械漂白machine dyeing 机凭色machine oil 机油machine printing 机啤花macle 双晶macleod gage 麦克劳计maclurin 桑橙素macroanalysis 常量分析macrochemistry 常量化学macrocrystal 大晶体macrogeochemistry 宏观地球化学macroglobulin 巨球蛋白macromolecular chemistry 大分子化学macromolecular colloid 高分子胶质macromolecular compound 高分子化合物macromolecular grating 大分子格子macromolecular rupture 大分子破裂macromolecule 大分子macropolymerization 巨聚合macroscopic structure 宏观结构macrosis 庞大macrostate 宏观状态macrostructure 宏观结构macula lutea 黄斑madder lake 茜草色淀madder red 茜草红magenta 品红色magic mirror 半透玫magma 岩浆magma glassashes 岩浆玻璃灰magmatic assimilation 岩浆同化酌magmatic ore 岩浆矿石magmatic water 岩浆水magnalium 镁铝合金magnesia 氧化镁magnesia brick 镁砖magnesia cement 镁氧水泥magnesia clinker 镁熔块magnesia mixture 镁氧混合剂magnesia porcelain 镁质瓷器magnesia portland cement 氧化镁一般水泥magnesite 菱镁矿magnesite chrome brick 铬镁砖magnesium 镁magnesium acetate 乙酸镁magnesium borate 硼酸镁magnesium calcium carbonate 碳酸镁钙magnesium cell 镁电池magnesium chloride 氯化镁magnesium hydrate 氢氧化镁magnesium hydroxide 氢氧化镁magnesium nitrate 硝酸镁magnesium oxide 氧化镁magnesium peroxide 过氧化镁magnesium powder 镁细粉magnesium sulfate 硫酸镁magneson 试镁灵magnet 磁铁magnetic analysis 磁力分析magnetic anisotropy 磁蛤异性magnetic crystal group 磁晶群magnetic crystal structure 磁晶体结构magnetic field 磁场magnetic filter 磁性过滤器magnetic induction 磁感应magnetic iron ore 磁铁矿magnetic iron oxide 磁性氧化铁magnetic needle 磁针magnetic permeability 磁导率magnetic quantum number 磁量子数magnetic relaxation 磁性弛豫magnetic resonance 磁共振magnetic semiconductor 磁性半导体magnetic separator 磁力分开器magnetic stirrer 磁力搅拌器magnetic substance 磁性体magnetic susceptibility 磁化率magnetism 磁magnetite 磁铁矿magnetization 磁化magnetochemical analysis 磁化学分析magnetochemical investigation 磁化学甸magnetochemistry 磁化学magnetometer 磁强计magneton 磁子magnetosonic wave 磁声波magnetron 磁控管magnification 扩大率magnifier 扩大镜magnifying glass 扩大镜main alloying component 合金稚分main constituent 知组分main fermentation 知发酵酌main group 皱main group element 皱元素main reaction 知反应main valence 汁子价maintenance costs 维持费maize oil 玉米油maize starch 玉米淀粉majolika 马略尔卡陶器make up water 补充水malachite 孔雀石malachite green 孔雀绿malachite green actinometer 孔雀石绿光量计malate 苹果酸盐malathion 马拉松male sex hormone 雄激素maleamic acid 马来酰胺酸maleate 马来酸盐maleic acid 马来酸maleic acid ester 马来酸酯maleic anhydride 马来酐maleic ester resin 马来酯尸maleic hydrazide 马来酰肼maleic resin 马来尸malic acid 苹果酸malleability 展性malleable cast iron 可锻铸铁malonamide 丙二酰胺malonate 丙二酸盐malonic acid 丙二酸malonic ester 丙二酸酯malonic ester synthesis 丙二酸酯合成malonylurea 巴比土酸malt 麦芽malt agar 麦芽琼脂malt extract 麦芽抽出物malt sugar 麦芽糖maltase 麦芽糖酶maltha 软沥青malting 麦芽制造maltol 麦芽醇maltose 麦芽糖malvidin chloride 氯化二甲花翠man made fiber 人造纤维man made rubber 人造橡胶mandarin oil 橘子油mandelic acid 孟德立酸mandelonitrile 扁桃腈mandrel test 心轴试验法manganate 锰酸盐manganese 锰manganese blende 硫锰矿manganese chloride 氯化锰manganese dioxide 二氧化锰manganese sulfate 硫酸锰manganese sulfide 硫化锰manganin 锰镍铜合金manganite 亚锰酸盐mangrove 红树manipulator 操纵器机械手manna 吗哪mannan 甘露聚糖mannich reaction 曼尼期反应manninotriose 甘露三糖mannite 甘露糖醇mannitol 甘露糖醇mannitol hexanitrate 六硝酸甘露醇mannonic acid 甘露糖酸mannose 甘露糖manocryometer 融解压力计manometer 压力计manostat 恒压器manufacture 制造manufacture of common salt 食盐制造法manufactured gas 人造煤气manufacturing cost 造价manufacturing in series 成批生产manufacturing method 制造法manufacturing process 制造法manure 肥料manure salts 肥料盐manuring 施肥maple sugar 槭糖marble 大理石marcasite 白铁矿margarate 十七酸盐margaric acid 十七酸margarine 人造奶油margarite 珍珠云母marine animal oil 海生动物油marine clay 海成粘土marine engine oil 船用机油marine soap 海水皂mariotte bottle 马利欧特瓶marjoram oil 马郁兰油mark 标记marked line 标线market bleach 一般漂白marking ink 打印墨水markovnikov's rule 马尔科夫尼科夫规则marseille soap 马赛皂marsh gas 沼气marsh test 马希氏试验marshall's acid 马歇尔酸martens hardness tester 马氏硬度试验器martens heat resistance test 马腾斯耐热试验martensite 马氏体maser 微波激射器mash 麦芽汁mask 面具masking 掩蔽masking agent 掩蔽剂masking reagent 掩蔽剂mason's hydrated lime 砖石用熟石灰masonry cement 砌筑水泥mass acceleration 质量加速度mass action 质量酌mass balance 物料平衡mass concentration 质量浓度mass defect 质量筐mass number 质量数mass polymerization 本体聚合mass production 大量生产mass radiation 质量辐射mass spectrograph 质谱仪mass spectrometer 质谱仪mass spectrometry 质谱测定法mass spectroscopy 质谱分析mass spectrum 质谱mass stopping power 质量阻止本领mass to charge ratio 质荷比mass transfer 物质传递mass unit 质量单位mass velocity 质量速度massecuite 糖膏massicot 铅黄massive coal 块煤masterbatch 母体混合物mastic 乳香mastication 捏炼masticator 素炼机masut 重油mat finish 消光整理mat glaze 无光泽釉mat gold 消光金mat paint 消光油漆match 火柴material 物质material balance 物料平衡material point 质点material wave 物质波mathematical induction 数学归纳法matrine 苦参碱matrix 基质matrix effect 基体效应matter 物质maturation 成熟酌maturative 催脓药maturing 成熟酌maturing temperature 成熟温度mauvein 苯胺紫maximal dose 极大剂量maximal observable 最大观测量maximal work 最大功maximum and minimum thermometer 最高最低温度计maximum current 最大电流maximum deflection 最大偏转maximum effective work 最大有效功maximum fiber stress 最大纤维应力maximum flexural strength 最大抗挠强度maximum load 最大负荷maximum output 最高产率maximum permissible dose 最大同意剂量maximum phenomenon 极大现象maximum suppressor 畸峰抑制剂maximum thermometer 最高温度计maximum wave 极大波maximum work 最大功maxivalence 最高价maxwell boltzmann statistics 麦克斯韦玻耳兹曼统计maxwell boltzmann's law of energy distribution 麦克斯韦玻耳兹曼能量分布定律maxwell boltzmann's law of velocity distribution 麦克斯韦玻尔兹曼速度分配定律mazout 重油meal 粉状物mean activity 平均活度mean boiling point 平均沸点mean degree of polymerization 平均聚合度mean deviation 平均偏差mean dispersion 平均分散mean error 平均误差mean free path 平均自由程mean life 平均寿命mean temperature difference 均温差mean value 平均值measurable set 可测集measurement 测定measurement deviation 测定偏差measurement error 测量误差measurement of molecular weight 分子量测定measurement of radioactivity 放射能测定measuring 测定measuring accuracy 测量精度measuring apparatus 计量仪器measuring bottle 量瓶measuring cylinder 量筒measuring flask 量瓶measuring glass 量杯measuring instrument 计量仪器measuring pipet 莫尔吸量管measuring tank 量槽mecazine 密哌嗪mechanical draft 机械通风mechanical energy 机械能mechanical equivalent of heat 热功当量mechanical impedance 机械阻抗mechanical mixture 机械混合物mechanical properties 机械性能mechanical pulp 机碎木浆mechanical rectifier 机械整流mechanical scrubber 机械滤净器mechanical test 机械试验mechanical weathering 机械风化mechanization 机械化mechanochemistry 机械化学meconic acid 袂康酸meconine 袂康宁meconium 鸦片mediasilicic rock 中硅质岩medical chemistry 医化学medical durable yeast 医药耐久酵母medicated soap 药用皂medium 介质medium boiler 中沸溶剂medium oil 中油medium oil varnish 中油清漆medium tone 中间色调meker burner 梅克尔灯melamine 蜜胺melamine resin 蜜胺尸melamine resin varnish 三聚氰胺尸清漆melanin 黑素melanogen 黑素原melibiase 蜜二糖酶melibiose 蜜二糖melinite 苦味酸melissic acid 蜂花酸melissyl alcohol 蜂花醇melitose 棉子糖mellic acid 苯六酸mellitate 苯六甲酸酯mellophanic acid 苯偏四甲酸melt 溶融物melt spinning 熔体纺丝melt spinning device 熔融纺丝装置melt viscosity 熔解粘度melting 熔融melting heat 熔化热melting method 熔融法melting point 熔点melting point diagram 熔点线图melting zone 熔化带membrane 隔膜membrane electrode 膜电极membrane equilibrium 膜平衡membrane filter 薄膜过滤器membrane potential 膜电位membrane simulation 膜模拟memory 存储器menadiole 甲萘二酚menadione 甲萘醌mendelev periodic law of elements 门捷列夫元素周期律mendelevium 钔meniscus 弯液面menshutkin reaction 门秀金反应menthadiene 薄荷二烯menthane 薄荷烷menthol 薄荷醇menthone 薄荷酮menthyl acetate 三萜醇乙酸酯mepazine 密哌嗪mephobarbital 普罗米那mephosfolan 二噻磷meralluride 汞鲁来merbromin 汞溴红mercaptal 缩硫醛mercaptan 硫醇mercaptide 硫醇盐mercaptobenzothiazole 巯基苯并噻唑mercaptoethanol 巯基乙醇mercaptol 缩硫醇mercaptopurine 巯基嘌呤mercaptothiazoline 巯基噻唑啉mercerization 丝光处理mercerizing assistant 丝光加工助剂mercerizing machine 丝光处理机mercocresol 汞甲酚剂mercuration 汞化mercurial barometer 水银气压计mercurial column 水银柱mercurial ointment 汞制油膏mercuric arsenate 砷酸汞mercuric chloride 氯化正汞mercuric compound 正汞化合物mercuric cyanide 氰化汞mercuric fluoride 氟化汞mercuric nitrate 硝酸汞mercuric oleate 油酸汞mercuric oxide 氧化汞mercuric oxide electrode 氧化汞电极mercuric salt 正汞盐mercuric stearate 硬脂酸汞mercuric sulfate 硫酸汞mercuric sulfide 硫化汞mercurimetric titration 汞液滴定法mercurimetry 汞液滴定法mercurochrome 汞溴红mercurol 核酸汞mercurometric titration 亚汞滴定法mercurometry 亚汞滴定法mercurous nitrate 硝酸亚汞mercurous salt 亚汞盐mercury 汞mercury arc rectifier 汞汽整流mercury bridge 水银电桥mercury cathode cell 汞阴极电池mercury cell 水银电池mercury chloride 氯化汞mercury cyanide 氰化汞mercury electrode 水银电极mercury fulminate 雷酸汞mercury iodide 碘化汞mercury lamp 水银灯mercury manometer 水银压力计mercury nitrate 硝酸汞mercury oxide 氧化汞mercury pool 水银槽mercury process 水银法mercury pump 水银真空泵mercury rash 汞皮疹mercury thermometer 水银温度表mercury vapour rectifier 汞汽整流mercury volumeter 汞容积计meromyosin 酶解肌球蛋白meroplankton 暂时性浮游生物mesaconic acid 甲基反丁烯二酸mescaline 墨斯卡灵mesh 筛眼mesityl oxide 异丙叉丙酮mesitylene 均三甲基苯meso form 内消旋式mesobilirubin 中胆红素mesobilirubinogen 中胆红原mesobiliverdin 中胆绿素mesochemistry 介子化学mesocolloid 近胶体mesomeric effect 内消旋效应mesomerism 稳变异构mesomorphic phase 中间相mesomorphism 液晶态meson 介子mesophase 中间相mesorcin 均三甲苯二酚mesotartaric acid 内消旋酒石酸mesothorium 新钍mesoxalic acid 中草酸mesoxalylurea 中草酰脲messenger ribonucleic acid 信使核糖核酸meta acid 偏酸metaarsenic acid 偏砷酸metabiosis 后继共生metabolism 代谢酌metabolite 代谢物metaboric acid 偏硼酸metachemistry 超化学metachromasia 异染色metachromasy 异染色metachromatic stain 异染性染料metachromatism 变色现象metadiazine 嘧啶metaisomerism 位变异构现象metal alkyl 金属烷基metal analysis 金属分析metal arc 金属电弧metal bath 金属浴metal carbonyl 羰络金属metal cluster 金属团簇metal complex 金属络合盐metal complex dye 金属配位染料metal encased brick 铁皮砖metal film resistor 金属薄膜电阻器metal fog 金属雾metal glass 金属玻璃metal indicator 金属指示剂metal line 液面线metal mist 金属雾metal nonmetal transition 金属非金属过渡metal plating 金属镀层metal spray gun 金属喷雾器metal spraying 金属喷涂metalation 金属化metaldehyde 多聚乙醛metallic block calorimeter 金属热量计metallic bond 金属键metallic complex salt 金属络合盐metallic element 金属元素metallic luster 金属光泽metallic oxide 金属氧化物metallic paint 金属涂料metallic poison 金属毒metallic powdery pigment 金属粉末颜料metallic soap 金属皂metallic thermometer 金属温度计metallic tin 金属锡metallocene 金属茂络合物metallocycle 金属循环物metalloenzyme 金属酶。

大环多胺

大环多胺

New1H-Pyrazole-Containing Polyamine Receptors Able ToComplex L-Glutamate in Water at Physiological pH ValuesCarlos Miranda,†Francisco Escartı´,‡Laurent Lamarque,†Marı´a J.R.Yunta,§Pilar Navarro,*,†Enrique Garcı´a-Espan˜a,*,‡and M.Luisa Jimeno†Contribution from the Instituto de Quı´mica Me´dica,Centro de Quı´mica Orga´nica Manuel Lora Tamayo,CSIC,C/Juan de la Cier V a3,28006Madrid,Spain,Departamento de Quı´mica Inorga´nica,Facultad de Quı´mica,Uni V ersidad de Valencia,c/Doctor Moliner50, 46100Burjassot(Valencia),Spain,and Departamento de Quı´mica Orga´nica,Facultad deQuı´mica,Uni V ersidad Complutense de Madrid,A V plutense s/n,28040Madrid,SpainReceived April16,2003;E-mail:enrique.garcia-es@uv.esAbstract:The interaction of the pyrazole-containing macrocyclic receptors3,6,9,12,13,16,19,22,25,26-decaazatricyclo-[22.2.1.111,14]-octacosa-1(27),11,14(28),24-tetraene1[L1],13,26-dibenzyl-3,6,9,12,13,16,-19,22,25,26-decaazatricyclo-[22.2.1.111,14]-octacosa-1(27),11,14(28),24-tetraene2[L2],3,9,12,13,16,22,-25,26-octaazatricyclo-[22.2.1.111,14]-octacosa-1(27),11,14(28),24-tetraene3[L3],6,19-dibenzyl-3,6,9,12,13,-16,19,22,25,26-decaazatricyclo-[22.2.1.111,14]-octacosa-1(27),11,14(28),24-tetraene4[L4],6,19-diphenethyl-3,6,9,12,13,16,19,22,25,26-decaazatricyclo-[22.2.1.111,14]-octacosa-1(27),11,14(28),24-tetraene5[L5],and 6,19-dioctyl-3,6,9,12,13,16,19,22,25,26-decaazatricyclo-[22.2.1.111,14]-octacosa-1(27),11,14(28),24-tetra-ene6[L6]with L-glutamate in aqueous solution has been studied by potentiometric techniques.The synthesis of receptors3-6[L3-L6]is described for the first time.The potentiometric results show that4[L4]containing benzyl groups in the central nitrogens of the polyamine side chains is the receptor displaying the larger interaction at pH7.4(K eff)2.04×104).The presence of phenethyl5[L5]or octyl groups6[L6]instead of benzyl groups4[L4]in the central nitrogens of the chains produces a drastic decrease in the stability[K eff )3.51×102(5),K eff)3.64×102(6)].The studies show the relevance of the central polyaminic nitrogen in the interaction with glutamate.1[L1]and2[L2]with secondary nitrogens in this position present significantly larger interactions than3[L3],which lacks an amino group in the center of the chains.The NMR and modeling studies suggest the important contribution of hydrogen bonding andπ-cation interaction to adduct formation.IntroductionThe search for the L-glutamate receptor field has been andcontinues to be in a state of almost explosive development.1 L-Glutamate(Glu)is thought to be the predominant excitatory transmitter in the central nervous system(CNS)acting at a rangeof excitatory amino acid receptors.It is well-known that it playsa vital role mediating a great part of the synaptic transmission.2However,there is an increasing amount of experimentalevidence that metabolic defects and glutamatergic abnormalitiescan exacerbate or induce glutamate-mediated excitotoxic damageand consequently neurological disorders.3,4Overactivation ofionotropic(NMDA,AMPA,and Kainate)receptors(iGluRs)by Glu yields an excessive Ca2+influx that produces irreversible loss of neurons of specific areas of the brain.5There is much evidence that these processes induce,at least in part,neuro-degenerative illnesses such as Parkinson,Alzheimer,Huntington, AIDS,dementia,and amyotrophic lateral sclerosis(ALS).6In particular,ALS is one of the neurodegenerative disorders for which there is more evidence that excitotoxicity due to an increase in Glu concentration may contribute to the pathology of the disease.7Memantine,a drug able to antagonize the pathological effects of sustained,but relatively small,increases in extracellular glutamate concentration,has been recently received for the treatment of Alzheimer disease.8However,there is not an effective treatment for ALS.Therefore,the preparation of adequately functionalized synthetic receptors for L-glutamate seems to be an important target in finding new routes for controlling abnormal excitatory processes.However,effective recognition in water of aminocarboxylic acids is not an easy task due to its zwitterionic character at physiological pH values and to the strong competition that it finds in its own solvent.9†Centro de Quı´mica Orga´nica Manuel Lora Tamayo.‡Universidad de Valencia.§Universidad Complutense de Madrid.(1)Jane,D.E.In Medicinal Chemistry into the Millenium;Campbell,M.M.,Blagbrough,I.S.,Eds.;Royal Society of Chemistry:Cambridge,2001;pp67-84.(2)(a)Standaert,D.G.;Young,A.B.In The Pharmacological Basis ofTherapeutics;Hardman,J.G.,Goodman Gilman,A.,Limbird,L.E.,Eds.;McGraw-Hill:New York,1996;Chapter22,p503.(b)Fletcher,E.J.;Loge,D.In An Introduction to Neurotransmission in Health and Disease;Riederer,P.,Kopp,N.,Pearson,J.,Eds.;Oxford University Press:New York,1990;Chapter7,p79.(3)Michaelis,E.K.Prog.Neurobiol.1998,54,369-415.(4)Olney,J.W.Science1969,164,719-721.(5)Green,J.G.;Greenamyre,J.T.Prog.Neurobiol.1996,48,613-63.(6)Bra¨un-Osborne,H.;Egebjerg,J.;Nielsen,E.O.;Madsen,U.;Krogsgaard-Larsen,P.J.Med.Chem.2000,43,2609-2645and references therein.(7)(a)Shaw,P.J.;Ince,P.G.J.Neurol.1997,244(Suppl2),S3-S14.(b)Plaitakis,A.;Fesdjian,C.O.;Shashidharan,S Drugs1996,5,437-456.(8)Frantz,A.;Smith,A.Nat.Re V.Drug Dico V ery2003,2,9.Published on Web12/30/200310.1021/ja035671m CCC:$27.50©2004American Chemical Society J.AM.CHEM.SOC.2004,126,823-8339823There are many types of receptors able to interact with carboxylic acids and amino acids in organic solvents,10-13yielding selective complexation in some instances.However,the number of reported receptors of glutamate in aqueous solution is very scarce.In this sense,one of the few reports concerns an optical sensor based on a Zn(II)complex of a 2,2′:6′,2′′-terpyridine derivative in which L -aspartate and L -glutamate were efficiently bound as axial ligands (K s )104-105M -1)in 50/50water/methanol mixtures.14Among the receptors employed for carboxylic acid recogni-tion,the polyamine macrocycles I -IV in Chart 1are of particular relevance to this work.In a seminal paper,Lehn et al.15showed that saturated polyamines I and II could exert chain-length discrimination between different R ,ω-dicarboxylic acids as a function of the number of methylene groups between the two triamine units of the receptor.Such compounds were also able to interact with a glutamic acid derivative which has the ammonium group protected with an acyl moiety.15,16Compounds III and IV reported by Gotor and Lehn interact in their protonated forms in aqueous solution with protected N -acetyl-L -glutamate and N -acetyl-D -glutamate,showing a higher stability for the interaction with the D -isomer.17In both reports,the interaction with protected N -acetyl-L -glutamate at physiological pH yields constants of ca.3logarithmic units.Recently,we have shown that 1H -pyrazole-containing mac-rocycles present desirable properties for the binding of dopam-ine.18These polyaza macrocycles,apart from having a highpositive charge at neutral pH values,can form hydrogen bonds not only through the ammonium or amine groups but also through the pyrazole nitrogens that can behave as hydrogen bond donors or acceptors.In fact,Elguero et al.19have recently shown the ability of the pyrazole rings to form hydrogen bonds with carboxylic and carboxylate functions.These features can be used to recognize the functionalities of glutamic acid,the carboxylic and/or carboxylate functions and the ammonium group.Apart from this,the introduction of aromatic donor groups appropriately arranged within the macrocyclic framework or appended to it through arms of adequate length may contribute to the recognition event through π-cation interactions with the ammonium group of L -glutamate.π-Cation interactions are a key feature in many enzymatic centers,a classical example being acetylcholine esterase.20The role of such an interaction in abiotic systems was very well illustrated several years ago in a seminal work carried out by Dougherty and Stauffer.21Since then,many other examples have been reported both in biotic and in abiotic systems.22Taking into account all of these considerations,here we report on the ability of receptors 1[L 1]-6[L 6](Chart 2)to interact with L -glutamic acid.These receptors display structures which differ from one another in only one feature,which helps to obtain clear-cut relations between structure and interaction(9)Rebek,J.,Jr.;Askew,B.;Nemeth,D.;Parris,K.J.Am.Chem.Soc.1987,109,2432-2434.(10)Seel,C.;de Mendoza,J.In Comprehensi V e Supramolecular Chemistry ;Vogtle,F.,Ed.;Elsevier Science:New York,1996;Vol.2,p 519.(11)(a)Sessler,J.L.;Sanson,P.I.;Andrievesky,A.;Kral,V.In SupramolecularChemistry of Anions ;Bianchi,A.,Bowman-James,K.,Garcı´a-Espan ˜a,E.,Eds.;John Wiley &Sons:New York,1997;Chapter 10,pp 369-375.(b)Sessler,J.L.;Andrievsky,A.;Kra ´l,V.;Lynch,V.J.Am.Chem.Soc.1997,119,9385-9392.(12)Fitzmaurice,R.J.;Kyne,G.M.;Douheret,D.;Kilburn,J.D.J.Chem.Soc.,Perkin Trans.12002,7,841-864and references therein.(13)Rossi,S.;Kyne,G.M.;Turner,D.L.;Wells,N.J.;Kilburn,J.D.Angew.Chem.,Int.Ed.2002,41,4233-4236.(14)Aı¨t-Haddou,H.;Wiskur,S.L.;Lynch,V.M.;Anslyn,E.V.J.Am.Chem.Soc.2001,123,11296-11297.(15)Hosseini,M.W.;Lehn,J.-M.J.Am.Chem.Soc.1982,104,3525-3527.(16)(a)Hosseini,M.W.;Lehn,J.-M.Hel V .Chim.Acta 1986,69,587-603.(b)Heyer,D.;Lehn,J.-M.Tetrahedron Lett.1986,27,5869-5872.(17)(a)Alfonso,I.;Dietrich,B.;Rebolledo,F.;Gotor,V.;Lehn,J.-M.Hel V .Chim.Acta 2001,84,280-295.(b)Alfonso,I.;Rebolledo,F.;Gotor,V.Chem.-Eur.J.2000,6,3331-3338.(18)Lamarque,L.;Navarro,P.;Miranda,C.;Ara ´n,V.J.;Ochoa,C.;Escartı´,F.;Garcı´a-Espan ˜a,E.;Latorre,J.;Luis,S.V.;Miravet,J.F.J.Am.Chem.Soc .2001,123,10560-10570.(19)Foces-Foces,C.;Echevarria,A.;Jagerovic,N.;Alkorta,I.;Elguero,J.;Langer,U.;Klein,O.;Minguet-Bonvehı´,H.-H.J.Am.Chem.Soc.2001,123,7898-7906.(20)Sussman,J.L.;Harel,M.;Frolow,F.;Oefner,C.;Goldman,A.;Toker,L.;Silman,I.Science 1991,253,872-879.(21)Dougherty,D.A.;Stauffer,D.A.Science 1990,250,1558-1560.(22)(a)Sutcliffe,M.J.;Smeeton,A.H.;Wo,Z.G.;Oswald,R.E.FaradayDiscuss.1998,111,259-272.(b)Kearney,P.C.;Mizoue,L.S.;Kumpf,R.A.;Forman,J.E.;McCurdy,A.;Dougherty,D.A.J.Am.Chem.Soc.1993,115,9907-9919.(c)Bra ¨uner-Osborne,H.;Egebjerg,J.;Nielsen,E.;Madsen,U.;Krogsgaard-Larsen,P.J.Med.Chem.2000,43,2609-2645.(d)Zacharias,N.;Dougherty,D.A.Trends Pharmacol.Sci.2002,23,281-287.(e)Hu,J.;Barbour,L.J.;Gokel,G.W.J.Am.Chem.Soc.2002,124,10940-10941.Chart 1.Some Receptors Employed for Dicarboxylic Acid and N -AcetylglutamateRecognitionChart 2.New 1H -Pyrazole-Containing Polyamine Receptors Able To Complex L -Glutamate inWaterA R T I C L E SMiranda et al.824J.AM.CHEM.SOC.9VOL.126,NO.3,2004strengths.1[L1]and2[L2]differ in the N-benzylation of the pyrazole moiety,and1[L1]and3[L3]differ in the presence in the center of the polyamine side chains of an amino group or of a methylene group.The receptors4[L4]and5[L5]present the central nitrogens of the chain N-functionalized with benzyl or phenethyl groups,and6[L6]has large hydrophobic octyl groups.Results and DiscussionSynthesis of3-6.Macrocycles3-6have been obtained following the procedure previously reported for the preparation of1and2.23The method includes a first dipodal(2+2) condensation of the1H-pyrazol-3,5-dicarbaldehyde7with the corresponding R,ω-diamine,followed by hydrogenation of the resulting Schiff base imine bonds.In the case of receptor3,the Schiff base formed by condensation with1,5-pentanediamine is a stable solid(8,mp208-210°C)which precipitated in68% yield from the reaction mixture.Further reduction with NaBH4 in absolute ethanol gave the expected tetraazamacrocycle3, which after crystallization from toluene was isolated as a pure compound(mp184-186°C).In the cases of receptors4-6, the precursor R,ω-diamines(11a-11c)(Scheme1B)were obtained,by using a procedure previously described for11a.24 This procedure is based on the previous protection of the primary amino groups of1,5-diamino-3-azapentane by treatment with phthalic anhydride,followed by alkylation of the secondary amino group of1,5-diphthalimido-3-azapentane9with benzyl, phenethyl,or octyl bromide.Finally,the phthalimido groups of the N-alkyl substituted intermediates10a-10c were removed by treatment with hydrazine to afford the desired amines11a-11c,which were obtained in moderate yield(54-63%).In contrast with the behavior previously observed in the synthesis of3,in the(2+2)dipodal condensations of7with 3-benzyl-,3-phenethyl-,and3-octyl-substituted3-aza-1,5-pentanediamine11a,11b,and11c,respectively,there was not precipitation of the expected Schiff bases(Scheme1A). Consequently,the reaction mixtures were directly reduced in situ with NaBH4to obtain the desired hexaamines4-6,which after being carefully purified by chromatography afforded purecolorless oils in51%,63%,and31%yield,respectively.The structures of all of these new cyclic polyamines have been established from the analytical and spectroscopic data(MS(ES+), 1H and13C NMR)of both the free ligands3-6and their corresponding hydrochloride salts[3‚4HCl,4‚6HCl,5‚6HCl, and6‚6HCl],which were obtained as stable solids following the same procedure previously reported18for1‚6HCl and2‚6HCl.As usually occurs for3,5-disubstituted1H-pyrazole deriva-tives,either the free ligands3-6or their hydrochlorides show very simple1H and13C NMR spectra,in which signals indicate that,because of the prototropic equilibrium of the pyrazole ring, all of these compounds present average4-fold symmetry on the NMR scale.The quaternary C3and C5carbons appear together,and the pairs of methylene carbons C6,C7,and C8are magnetically equivalent(see Experimental Section).In the13C NMR spectra registered in CDCl3solution, significant differences can be observed between ligand3,without an amino group in the center of the side chain,and the N-substituted ligands4-6.In3,the C3,5signal appears as a broad singlet.However,in4-6,it almost disappears within the baseline of the spectra,and the methylene carbon atoms C6and C8experience a significant broadening.Additionally,a remark-able line-broadening is also observed in the C1′carbon signals belonging to the phenethyl and octyl groups of L5and L6, respectively.All of these data suggest that as the N-substituents located in the middle of the side chains of4-6are larger,the dynamic exchange rate of the pyrazole prototropic equilibrium is gradually lower,probably due to a relation between proto-tropic and conformational equilibria.Acid-Base Behavior.To follow the complexation of L-glutamate(hereafter abbreviated as Glu2-)and its protonated forms(HGlu-,H2Glu,and H3Glu+)by the receptors L1-L6, the acid-base behavior of L-glutamate has to be revisited under the experimental conditions of this work,298K and0.15mol dm-3.The protonation constants obtained,included in the first column of Table1,agree with the literature25and show that the zwitterionic HGlu-species is the only species present in aqueous solution at physiological pH values(Scheme2and Figure S1of Supporting Information).Therefore,receptors for(23)Ara´n,V.J.;Kumar,M.;Molina,J.;Lamarque,L.;Navarro,P.;Garcı´a-Espan˜a,E.;Ramı´rez,J.A.;Luis,S.V.;Escuder,.Chem.1999, 64,6137-6146.(24)(a)Yuen Ng,C.;Motekaitis,R.J.;Martell,A.E.Inorg.Chem.1979,18,2982-2986.(b)Anelli,P.L.;Lunazzi,L.;Montanari,F.;Quici,.Chem.1984,49,4197-4203.Scheme1.Synthesis of the Pyrazole-Containing MacrocyclicReceptorsNew1H-Pyrazole-Containing Polyamine Receptors A R T I C L E SJ.AM.CHEM.SOC.9VOL.126,NO.3,2004825glutamate recognition able to address both the negative charges of the carboxylate groups and the positive charge of ammonium are highly relevant.The protonation constants of L 3-L 6are included in Table 1,together with those we have previously reported for receptors L 1and L 2.23A comparison of the constants of L 4-L 6with those of the nonfunctionalized receptor L 1shows a reduced basicity of the receptors L 4-L 6with tertiary nitrogens at the middle of the polyamine bridges.Such a reduction in basicity prevented the potentiometric detection of the last protonation for these ligands in aqueous solution.A similar reduction in basicity was previously reported for the macrocycle with the N -benzylated pyrazole spacers (L 2).23These diminished basicities are related to the lower probability of the tertiary nitrogens for stabilizing the positive charges through hydrogen bond formation either with adjacent nonprotonated amino groups of the molecule or with water molecules.Also,the increase in the hydrophobicity of these molecules will contribute to their lower basicity.The stepwise basicity constants are relatively high for the first four protonation steps,which is attributable to the fact that these protons can bind to the nitrogen atoms adjacent to the pyrazole groups leaving the central nitrogen free,the electrostatic repulsions between them being therefore of little significance.The remaining protonation steps will occur in the central nitrogen atom,which will produce an important increase in the electrostatic repulsion in the molecule and therefore a reduction in basicity.As stated above,the tertiary nitrogen atoms present in L 4-L 6will also contribute to this diminished basicity.To analyze the interaction with glutamic acid,it is important to know the protonation degree of the ligands at physiological pH values.In Table 2,we have calculated the percentages ofthe different protonated species existing in solution at pH 7.4for receptors L 1-L 6.As can be seen,except for the receptor with the pentamethylenic chains L 3in which the tetraprotonated species prevails,all of the other systems show that the di-and triprotonated species prevail,although to different extents.Interaction with Glutamate.The stepwise constants for the interaction of the receptors L 1-L 6with glutamate are shown in Table 3,and selected distribution diagrams are plotted in Figure 1A -C.All of the studied receptors interact with glutamate forming adduct species with protonation degrees (j )which vary between 8and 0depending on the system (see Table 3).The stepwise constants have been derived from the overall association constants (L +Glu 2-+j H +)H j LGlu (j -2)+,log j )provided by the fitting of the pH-metric titration curves.This takes into account the basicities of the receptors and glutamate (vide supra)and the pH range in which a given species prevails in solution.In this respect,except below pH ca.4and above pH 9,HGlu -can be chosen as the protonated form of glutamate involved in the formation of the different adducts.Below pH 4,the participation of H 2Glu in the equilibria has also to be considered (entries 9and 10in Table 3).For instance,the formation of the H 6LGlu 4+species can proceed through the equilibria HGlu -+H 5L 5+)H 6LGlu 4+(entry 8,Table 3),and H 2Glu +H 4L 4+)H 6LGlu 4(entry 9Table 3),with percentages of participation that depend on pH.One of the effects of the interaction is to render somewhat more basic the receptor,and somewhat more acidic glutamic acid,facilitating the attraction between op-positely charged partners.A first inspection of Table 3and of the diagrams A,B,and C in Figure 1shows that the interaction strengths differ markedly from one system to another depending on the structural features of the receptors involved.L 4is the receptor that presents the highest capacity for interacting with glutamate throughout all of the pH range explored.It must also be remarked that there are not clear-cut trends in the values of the stepwise constants as a function of the protonation degree of the receptors.This suggests that charge -charge attractions do not play the most(25)(a)Martell,E.;Smith,R.M.Critical Stability Constants ;Plenum:NewYork,1975.(b)Motekaitis,R.J.NIST Critically Selected Stability Constants of Metal Complexes Database ;NIST Standard Reference Database,version 4,1997.Table 1.Protonation Constants of Glutamic Acid and Receptors L 1-L 6Determined in NaCl 0.15mol dm -3at 298.1KreactionGluL 1aL 2aL 3bL 4L 5L 6L +H )L H c 9.574(2)d 9.74(2)8.90(3)9.56(1)9.25(3)9.49(4)9.34(5)L H +H )L H 2 4.165(3)8.86(2)8.27(2)8.939(7)8.38(3)8.11(5)8.13(5)L H 2+H )L H 3 2.18(2)7.96(2) 6.62(3)8.02(1) 6.89(5)7.17(6)7.46(7)L H 3+H )L H 4 6.83(2) 5.85(4)7.63(1) 6.32(5) 6.35(6) 5.97(8)L H 4+H )L H 5 4.57(3) 3.37(4) 2.72(8) 2.84(9) 3.23(9)L H 5+H )L H 6 3.18(3) 2.27(6)∑log K H n L41.135.334.233.634.034.1aTaken from ref 23.b These data were previously cited in a short communication (ref 26).c Charges omitted for clarity.d Values in parentheses are the standard deviations in the last significant figure.Scheme 2.L -Glutamate Acid -BaseBehaviorTable 2.Percentages of the Different Protonated Species at pH 7.4H 1L aH 2LH 3LH 4LL 11186417L 21077130L 3083458L 4083458L 51154323L 6842482aCharges omitted for clarity.A R T I C L E SMiranda et al.826J.AM.CHEM.SOC.9VOL.126,NO.3,2004outstanding role and that other forces contribute very importantly to these processes.26However,in systems such as these,which present overlapping equilibria,it is convenient to use conditional constants because they provide a clearer picture of the selectivity trends.27These constants are defined as the quotient between the overall amounts of complexed species and those of free receptor and substrate at a given pH[eq1].In Figure2are presented the logarithms of the effective constants versus pH for all of the studied systems.Receptors L1and L2with a nonfunctionalized secondary amino group in the side chains display opposite trend from all other receptors. While the stability of the L1and L2adducts tends to increase with pH,the other ligands show a decreasing interaction. Additionally,L1and L2present a close interaction over the entire pH range under study.The tetraaminic macrocycle L3is a better(26)Escartı´,F.;Miranda,C.;Lamarque,L.;Latorre,J.;Garcı´a-Espan˜a,E.;Kumar,M.;Ara´n,V.J.;Navarro,mun.2002,9,936-937.(27)(a)Bianchi,A.;Garcı´a-Espan˜a,c.1999,12,1725-1732.(b)Aguilar,J.A.;Celda,B.;Garcı´a-Espan˜a,E.;Luis,S.V.;Martı´nez,M.;Ramı´rez,J.A.;Soriano,C.;Tejero,B.J.Chem.Soc.,Perkin Trans.22000, 7,1323-1328.Table3.Stability Constants for the Interaction of L1-L6with the Different Protonated Forms of Glutamate(Glu) entry reaction a L1L2L3L4L5L6 1Glu+L)Glu L 3.30(2)b 4.11(1)2HGlu+L)HGlu L 3.65(2) 4.11(1) 3.68(2) 3.38(4) 3Glu+H L)HGlu L 3.89(2) 4.48(1) 3.96(2) 3.57(4) 4HGlu+H L)H2Glu L 3.49(2) 3.89(1) 2.37(4) 3.71(2)5HGlu+H2L)H3Glu L 3.44(2) 3.73(1) 2.34(3) 4.14(2) 2.46(4) 2.61(7) 6HGlu+H3L)H4Glu L 3.33(2) 3.56(2) 2.66(3) 4.65(2) 2.74(3) 2.55(7) 7HGlu+H4L)H5Glu L 3.02(2) 3.26(2) 2.58(3) 4.77(2) 2.87(3) 2.91(5) 8HGlu+H5L)H6Glu L 3.11(3) 3.54(2) 6.76(3) 4.96(3) 4.47(3) 9H2Glu+H4L)H6Glu L 2.54(3) 3.05(2) 3.88(2) 5.35(3) 3.66(4) 3.56(3) 10H2Glu+H5L)H7Glu L 2.61(6) 2.73(4) 5.51(3) 3.57(4) 3.22(8) 11H3Glu+H4L)H7Glu L 4.82(2) 4.12(9)a Charges omitted for clarity.b Values in parentheses are standard deviations in the last significantfigure.Figure1.Distribution diagrams for the systems(A)L1-glutamic acid, (B)L4-glutamic acid,and(C)L5-glutamicacid.Figure2.Representation of the variation of K cond(M-1)for the interaction of glutamic acid with(A)L1and L3,(B)L2,L4,L5,and L6.Initial concentrations of glutamate and receptors are10-3mol dm-3.Kcond)∑[(H i L)‚(H j Glu)]/{∑[H i L]∑[H j Glu]}(1)New1H-Pyrazole-Containing Polyamine Receptors A R T I C L E SJ.AM.CHEM.SOC.9VOL.126,NO.3,2004827receptor at acidic pH,but its interaction markedly decreases on raising the pH.These results strongly suggest the implication of the central nitrogens of the lateral polyamine chains in the stabilization of the adducts.Among the N-functionalized receptors,L4presents the largest interaction with glutamate.Interestingly enough,L5,which differs from L4only in having a phenethyl group instead of a benzyl one,presents much lower stability of its adducts.Since the basicity and thereby the protonation states that L4and L5 present with pH are very close,the reason for the larger stability of the L4adducts could reside on a better spatial disposition for formingπ-cation interactions with the ammonium group of the amino acid.In addition,as already pointed out,L4presents the highest affinity for glutamic acid in a wide pH range,being overcome only by L1and L2at pH values over9.This observation again supports the contribution ofπ-cation inter-actions in the system L4-glutamic because at these pH values the ammonium functionality will start to deprotonate(see Scheme2and Figure1B).Table4gathers the percentages of the species existing in equilibria at pH7.4together with the values of the conditional constant at this pH.In correspondence with Figure1A,1C and Figure S2(Supporting Information),it can be seen that for L1, L2,L5,and L6the prevailing species are[H2L‚HGlu]+and[H3L‚HGlu]2+(protonation degrees3and4,respectively),while for L3the main species are[H3L‚HGlu]+and[H4L‚HGlu]2+ (protonation degrees4and5,respectively).The most effective receptor at this pH would be L4which joins hydrogen bonding, charge-charge,andπ-cation contributions for the stabilization of the adducts.To check the selectivity of this receptor,we have also studied its interaction with L-aspartate,which is a competitor of L-glutamate in the biologic receptors.The conditional constant at pH7.4has a value of3.1logarithmic units for the system Asp-L4.Therefore,the selectivity of L4 for glutamate over aspartate(K cond(L4-glu)/K cond(L4-asp))will be of ca.15.It is interesting to remark that the affinity of L4 for zwiterionic L-glutamate at pH7.4is even larger than that displayed by receptors III and IV(Chart1)with the protected dianion N-acetyl-L-glutamate lacking the zwitterionic charac-teristics.Applying eq1and the stability constants reported in ref17,conditional constants at pH7.4of 3.24and 2.96 logarithmic units can be derived for the systems III-L-Glu and IV-L-Glu,respectively.Molecular Modeling Studies.Molecular mechanics-based methods involving docking studies have been used to study the binding orientations and affinities for the complexation of glutamate by L1-L6receptors.The quality of a computer simulation depends on two factors:accuracy of the force field that describes intra-and intermolecular interactions,and an adequate sampling of the conformational and configuration space of the system.28The additive AMBER force field is appropriate for describing the complexation processes of our compounds,as it is one of the best methods29in reproducing H-bonding and stacking stabiliza-tion energies.The experimental data show that at pH7.4,L1-L6exist in different protonation states.So,a theoretical study of the protonation of these ligands was done,including all of the species shown in5%or more abundance in the potentiometric measurements(Table4).In each case,the more favored positions of protons were calculated for mono-,di-,tri-,and tetraprotonated species.Molecular dynamics studies were performed to find the minimum energy conformations with simulated solvent effects.Molecular modeling studies were carried out using the AMBER30method implemented in the Hyperchem6.0pack-age,31modified by the inclusion of appropriate parameters. Where available,the parameters came from analogous ones used in the literature.32All others were developed following Koll-man33and Hopfinger34procedures.The equilibrium bond length and angle values came from experimental values of reasonable reference compounds.All of the compounds were constructed using standard geometry and standard bond lengths.To develop suitable parameters for NH‚‚‚N hydrogen bonding,ab initio calculations at the STO-3G level35were used to calculate atomic charges compatible with the AMBER force field charges,as they gave excellent results,and,at the same time,this method allows the study of aryl-amine interactions.In all cases,full geometry optimizations with the Polak-Ribiere algorithm were carried out,with no restraints.Ions are separated far away and well solvated in water due to the fact that water has a high dielectric constant and hydrogen bond network.Consequently,there is no need to use counteri-ons36in the modelization studies.In the absence of explicit solvent molecules,a distance-dependent dielectric factor quali-tatively simulates the presence of water,as it takes into account the fact that the intermolecular electrostatic interactions should vanish more rapidly with distance than in the gas phase.The same results can be obtained using a constant dielectric factor greater than1.We have chosen to use a distance-dependent dielectric constant( )4R ij)as this was the method used by Weiner et al.37to develop the AMBER force field.Table8 shows the theoretical differences in protonation energy(∆E p) of mono-,bi-,and triprotonated hexaamine ligands,for the (28)Urban,J.J.;Cronin,C.W.;Roberts,R.R.;Famini,G.R.J.Am.Chem.Soc.1997,119,12292-12299.(29)Hobza,P.;Kabelac,M.;Sponer,J.;Mejzlik,P.;Vondrasek,put.Chem.1997,18,1136-1150.(30)Cornell,W.D.;Cieplak,P.;Bayly,C.I.;Gould,I.R.;Merz,K.M.,Jr.;Ferguson,D.M.;Spelmeyer,D.C.;Fox,T.;Caldwell,J.W.;Kollman,P.A.J.Am.Chem.Soc.1995,117,5179-5197.(31)Hyperchem6.0(Hypercube Inc.).(32)(a)Fox,T.;Scanlan,T.S.;Kollman,P.A.J.Am.Chem.Soc.1997,119,11571-11577.(b)Grootenhuis,P.D.;Kollman,P.A.J.Am.Chem.Soc.1989,111,2152-2158.(c)Moyna,G.;Hernandez,G.;Williams,H.J.;Nachman,R.J.;Scott,put.Sci.1997,37,951-956.(d)Boden,C.D.J.;Patenden,put.-Aided Mol.Des.1999, 13,153-166.(33)/amber.(34)Hopfinger,A.J.;Pearlstein,put.Chem.1984,5,486-499.(35)Glennon,T.M.;Zheng,Y.-J.;Le Grand,S.M.;Shutzberg,B.A.;Merz,K.M.,put.Chem.1994,15,1019-1040.(36)Wang,J.;Kollman,P.A.J.Am.Chem.Soc.1998,120,11106-11114.Table4.Percentages of the Different Protonated Adducts[HGlu‚H j L](j-1)+,Overall Percentages of Complexation,andConditional Constants(K Cond)at pH7.4for the Interaction ofGlutamate(HGlu-)with Receptors L1-L6at Physiological pH[H n L‚HGlu]an)1n)2n)3n)4∑{[H n L‚HGlu]}K cond(M-1)L13272353 2.44×103L2947763 4.12×103L31101324 3.99×102L423737581 2.04×104L51010222 3.51×102L6121224 3.64×102a Charges omitted for clarity.A R T I C L E S Miranda et al. 828J.AM.CHEM.SOC.9VOL.126,NO.3,2004。

阿司匹林的制备反应混合物的分离流程

阿司匹林的制备反应混合物的分离流程

阿司匹林的制备反应混合物的分离流程The separation process of the reaction mixture for the preparation of aspirin can be divided into several key steps.Firstly, after the completion of the reaction, it is necessary to quench the excess reactants and by-products. This is typically achieved by adding a suitable quenching agent, such as water or a dilute acid, to neutralize any remaining unreacted acetic anhydride. The addition of water also helps in solubilizing some impurities.Following this, extraction is performed to separate the crude product from the aqueous phase. Commonly usedsolvents for extraction include ethyl acetate or dichloromethane. These solvents are immiscible with water and can effectively extract aspirin from the reaction mixture due to its higher affinity towards organic solvents.After extraction, it is necessary to remove any remaining impurities and organic solvents. One way to achieve this isby washing the organic layer with a suitable wash solution, such as sodium bicarbonate or sodium hydroxide solution. These wash solutions help in removing acidic impurities and residual acetic acid.Next, drying agents like anhydrous sodium sulfate or magnesium sulfate are added to remove any trace amounts of water present in the organic layer. These drying agents serve as desiccants and absorb any water molecules remaining.Upon completion of these steps, filtration or decantation can be employed to separate solid impurities that may have formed during the reaction process. Filtration techniques such as vacuum filtration or gravity filtration can be used depending on the nature and quantity of solids present.Finally, evaporation is carried out under reduced pressure using a rotary evaporator or by gentle heating using a distillation setup to remove excess solvent and obtain purified aspirin crystals. Care should be taken during this step to avoid overheating or excessive loss of product dueto volatilization.Overall, the separation process for preparing aspirin involves various techniques such as quenching, extraction, washing, drying, filtration, and evaporation. Each step is crucial for obtaining a pure and high-yield product.分离制备阿司匹林反应混合物的流程可以分为几个关键步骤。

三元生物塔格糖技术

三元生物塔格糖技术

三元生物塔格糖技术英文回答:Tripartite Biotic System (TBS) Targeting Glycomics.The Tripartite Biotic System (TBS) is a novel approach to glycomics research that integrates three distinct biological systems:Microbiota: The complex community of microorganisms that inhabit the human body.Host: The human organism itself.Environment: The external factors that influence the relationship between the microbiota and the host.The TBS approach recognizes that the microbiota plays a crucial role in the development, function, and regulation of the host's glycome, which is the collection of allglycans (carbohydrates) in the body.By studying the interactions between the microbiota, host, and environment, TBS aims to:Unravel the mechanisms by which the microbiota influences the host's glycome.Explore the potential for manipulating the microbiota to modulate glycomic pathways.Identify new diagnostic and therapeutic targets for glycan-related diseases.Several research projects have utilized the TBS approach to investigate the role of the microbiota in glycomic processes. For example, one study found that the gut microbiota of obese mice exhibited alterations in the expression of genes involved in glycan synthesis and degradation.Another study demonstrated that probiotics (beneficialbacteria) could modulate the host's glycome, reducing inflammation and improving glucose tolerance. Thesefindings highlight the potential of TBS to advance our understanding of glycomics and develop novel therapies for glycan-related diseases.中文回答:三元生物塔格糖技术。

硫化钨纳米花的制备及其在染料降解中的应用

硫化钨纳米花的制备及其在染料降解中的应用

2021年第1期有色金属(冶炼部分)(h ttp://)• 67 •doi:10. 3969/j. issn. 1007-7545. 2021. 01. 012硫化钨纳米花的制备及其在染料降解中的应用郭家旺,赖兰萍,陈东英,周洁英(赣州有色冶金研究所,江西贛州341000)摘要:以钨酸钠、硫脲、草酸为原料,采用水热法制备出由纳米薄膜组装而成的WS2纳米花(WS2N F)。

反应过程中,硫脲的包覆作用和草酸的偶联作用,协同控制WS2的增长,最终形成花瓣状结构。

所制备的WS2N F具有形变能力强、机械能捕获面积大、传质效率高和活性位点丰富的优点,有效提高了w s2材料的压电催化性能,在5 m in内可将难降解有机染料完全降解,且该材料多次重复使用后依然保持高活性。

关键词:硫化钨;纳米花;纳米薄膜;有机物降解;压电催化中图分类号:X75;TB34 文献标志码:A 文章编号:1007-7545(2021 )01-0067-05 P rep aratio n of Tungsten D isulfide and Its A pplication in Dye D egradationGUO Jia-w an g,LAI Lan-p in g,C H E N Dong-y ing,Z H O U Jie-ying(G a n z h o u N o n f e r r o u s M e t a l l u r g y I n s t i t u t e»G a n z h o u341000,J i a n g x i,C h i n a)Abstract:Tungsten disulfide nanoflowers(WS2N F)with nanosheets was prepared by hydrothermal method applying sodium tu n g state,thiourea and oxalic acid as raw materials.Capping effects of thiourea and coupling effects of oxalic acid synergistically controlled growth of WS2 »which resulted in flower-like structure.WS2NF prepared with this process has advantages of excellent flexibility,large area for mechanical energy capture,high mass transfer efficiency and rich active sites.These greatly improve piezo­degradation activity of WS2materials.The results show that refractory organics dyes can be completely degraded within 5 min with WS2NF as catalyst,and high activity remained after several recycles.Key words:tungsten disulfide;nanoflower;nanosheet;dye degradation;piezo-catalyst工业中产生的难降解有机物,例如染料、农药、药物等,往往会进人地表水[1]。

氧化石墨烯-壳聚糖复合膜修饰电极测定尿酸

氧化石墨烯-壳聚糖复合膜修饰电极测定尿酸
(1.商洛学院化学工程与现代材料学院,陕西商洛 726000; 2.西安工业大学材料与化学工程学院,陕西西安 710021)
摘 要:通过自组装技术,制备了氧化石墨烯-壳聚糖复合膜修饰电极,并研究了尿酸在该
修饰电极上的电化学行为。实验表明:该修饰电极对尿酸有较V 和0.446V 处出现一氧化峰和还原峰。利用差分脉冲伏安技术测定,尿酸浓度
第 37 卷 第 3 期 Vol.37 No.3
分析科学学报 JOURNAL OF ANALYTICALSCIENCE
DOI:10.13526/j.issn.1006-6144.2021.03.016
2021 年 6 月 June 2021
氧化石墨烯-壳聚糖复合膜修饰电极测定尿酸
樊 雪 梅1,2,王 书 民*1,李 哲 建1,王 毅 梦1, 刘 萍1,范新会1,2
2 结果与讨论
2.1 氧化石墨烯的表征
采 用 扫 描 电 镜 (SEM)对 制 备 的 氧 化 石 墨 烯 进 行 表 征 。
由图1可以看到氧化 石 墨 烯-壳 聚 糖 具 有 相 对 比 较 光 滑 的
层 状 结 构 ,是 小 而 轻 的 薄 片 。
2.2 氧化石墨烯-壳聚糖修饰电极的电化学表征
采用循环伏安法对 氧 化 石 墨 烯-壳 聚 糖 复 合 膜 修 饰 电
N···H···O 和 O···H···O 传递,降低了尿酸的过电位,促进了其氧化还原。
2.4 条件的优化
考察了氧化石墨烯-壳聚 糖 分 散 液 用 量 对 实 验 的 影 响。 发 现 当 氧 化 石 墨 烯-壳 聚 糖 分 散 液 量 比 较 小
时,尿酸峰电流比较小,当滴加量为5.0μL 时,峰电流最大,继续增加分散液量,电流基本趋于稳定。说明 5.0μL 已经达到电极饱和。故实验采用5.0μL 作为氧化石墨烯-壳聚糖分散液滴加量。

高硅MFI分子筛膜的合成与低温脱除膜内有机模板剂_赵淑蘅

高硅MFI分子筛膜的合成与低温脱除膜内有机模板剂_赵淑蘅
Key Words: High-silica MFI zeolite membrane; Template removal; Low-temperature hydrocracking; Gas permeation; Support
Received: September 24, 2015; Revised: November 23, 2015; Publishen on Web: November 24, 2015. *Corresponding author. Email: langlin@; Tel:+86-20-37218289. The project was supported by the National Natural Science Foundation of China (51202245, 51106165) and Natural Science Foundation of Guangdong Province, China (S2013010014896, 10251007006000000). 国家自然科学基金(51202245, 51106165)和广东省自然科学基金(S2013010014896, 10251007006000000)资助项目
低温加氢裂解脱除分子筛膜内有机模板剂的
按照摩尔比为 1TEOS : 0.36TPAOH : 60H2O 的 比例配制合成液,室温下搅拌 5 h,将合成液倒入 以聚四氟乙烯为内衬的不锈钢反应釜中,密封, 150 °C 下晶化 20 h;冷却后取出,并反复经过去离 子水超声清洗、离心分离得到晶种分子筛,置于 105 °C 烘箱中干燥备用;所制备的分子筛晶种大小 均匀,粒径约为 250 nm。 2.2.2 晶种层的制备
采用旋涂法在载体片表面预涂晶种 41。配制一 定浓度的晶种液,并超声 15 min,将载体片固定于 匀胶机上,涂覆适量晶种液,迅速打开旋转按 钮,在较低转速(500 r∙min-1)下停留 6 s,之后在较 高转速(2000 r∙min-1)下停留 20 s,均匀涂覆晶种, 最后置于 60 °C 烘箱中烘干备用。 2.2.3 分子筛膜的制备

【CN110055288A】一种用新型酶固定化技术合成多酚类化合物的方法【专利】

【CN110055288A】一种用新型酶固定化技术合成多酚类化合物的方法【专利】

(19)中华人民共和国国家知识产权局(12)发明专利申请(10)申请公布号 (43)申请公布日 (21)申请号 201910198895.7(22)申请日 2019.03.15(71)申请人 深圳大学地址 518060 广东省深圳市南山区学苑大道1066号(72)发明人 杨缜 魏一雄 (74)专利代理机构 深圳市君胜知识产权代理事务所(普通合伙) 44268代理人 王永文 刘文求(51)Int.Cl.C12P 7/22(2006.01)C12P 7/42(2006.01)C12P 13/04(2006.01)C12N 11/14(2006.01)(54)发明名称一种用新型酶固定化技术合成多酚类化合物的方法(57)摘要本发明公开了一种用新型酶固定化技术合成多酚类化合物的方法,其中,包括步骤:将过渡金属离子、磷酸缓冲液及酪氨酸酶溶液低温混合后静置,使酪氨酸酶固定在过渡金属离子与磷酸根离子结合生成的复合物上,形成酪氨酸酶纳米花;将酪氨酸酶纳米花加入单酚化合物溶液中,并加入金属螯合剂及还原剂形成酶促反应体系,在预定温度下进行酶促反应,合成多酚类化合物。

本发明解决了现有技术中通过酪氨酸酶催化合成多酚类化合物产率不高的问题。

权利要求书1页 说明书7页 附图8页CN 110055288 A 2019.07.26C N 110055288A1.一种用新型酶固定化技术合成多酚类化合物的方法,其特征在于,包括步骤:将过渡金属离子、磷酸缓冲液及酪氨酸酶溶液低温混合后静置,使酪氨酸酶固定在过渡金属离子离子与磷酸根离子结合生成的复合物上,形成酪氨酸酶纳米花;将酪氨酸酶纳米花加入单酚化合物溶液中,并加入金属螯合剂及还原剂形成酶促反应体系,在预定温度下进行酶促反应,合成多酚类化合物。

2.根据权利要求1所述的用新型酶固定化技术合成多酚类化合物的方法,其特征在于,所述过渡金属离子、磷酸缓冲液及酪氨酸酶溶液的混合液中,过渡金属离子的浓度为0~100mM,磷酸缓冲液的浓度为0~100mM。

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and
Chang-Hee
Lee’ and Jonathan S. Lindemistry, Carnegie Mellon University, 4400 Fifth Avenue, Pittsburgh, Pennsylvania 15213 USA
Abstract: The reaction at room temperature of an aldehyde with excess pyrrole in the absence of solvent affords the meso-substituted dipyrromethane. The reaction is catalyzed with trifluoroacetic acid or with BF9,0(Et)2. The dipyrromethaue is purified by crystallixation or by flash chromatography on silica with eluants containing 1% triethylamine. The reaction is compatible with aliphatic or aromatic aldehydes, including 2,6disubstituted benraklehydes. Nine dipyrromethanes have been prepared in this manner in yields of 47-865, indicating the broad scope of tbe reaction. The dipyrromethanes are stable in the purified form in the absence of light and air. Similar reaction with terephthalaldehyde and pyrrole affords the correspondmg bis-dipyrromethane. The reaction of a mesosubstituted dipyrrometbane with an aldehyde muter the conditions of the two-step one-flask porphyrin synthesis affords a direct route to trans-substituted meso-porphyrins. Acidolysis of the dipyrromethane is negligible under the conditions of the porphyrin-forming reaction. Four porphyrins bearing peripheral functional groups and faciallyencumbering groups have been prepared which serve as key building blocks in the synthesis of linear porphyrin aoays.
0040-4020(94)007 18-7
One-Flask Synthesis of Meso-Substituted Dipyrromethanes Their Application in the Synthesis of Trans-Substituted Porphyrin Building Blocks
RESULTS AND DISCUSSION Dipyrromethane formation: Aldehydes and pyrrole readily undergo acid-catalyzed condensation at room temperature.15-17 In solution at equimolar concentrations, the condensation yields oligomers and the cyclic porphyrinogen. In order to achieve a direct synthesis of dipyrromethanes without continued oligomerization, we have performed the pyrrole-aldehyde condensation in the presence of a large excess of pyrrole. Pyrrole serves as the reactant in excess and as the solvent for the reaction, giving direct formation of the dipyrromethane (Scheme 2).
i”etrahedronVol. 50, No. 39, pp. 11427-11440,1994 Copyright0 1994 Elsevier Science Ltd Printedin GreatBritain.All rights reserved 0040-4020/94$7.oo+o.00
As part of a building block approach toward porphyrin model systems?-4 we had need of a direct synthesis of truns-substituted porphyrins. Trans-substituted porphyrins can be prepared by mixed aldehyde condensations, but tlte cis and rruns-substituted porphyrins usually am difficult to separate. Direct approaches to trans-substituted porphyrins are provided by condensation of dipyrromethanes with aldehydes. Four such routes, each distinguished by the type of dipyrromethane employed, ate shown in Scheme 1. In Route 1, reaction of a g-substituted, meso-substituted dipyrromethane with an aldehyde affords a porphyrin bearing substituents at the eight g and four meso-positions. 56 In Route 2. reaction of a ~-substituted dipyrromethane (lacking a meso-substituent) with an aldehyde affords a porphyrin bearing substituents at the eight p and two meso-positions.7 Steric interactions of the p and meso-substituents cause such porphyrins to be ruffled, and syntheses of h-substituted dipyrromethanes have often required laborious syntheses, yet these routes have been widely utilized due to lack of better alternatives. In Route 3, reaction of dipyrromethane (lacking p and meso-substituents) with an aldehyde affords the truns-substituted porphyrin bearing only two meso-substituents.* However, the synthesis of dipyrrometbane involves a three-step procedure starting from pyrrole and thiophosgene. For our purposes rrans-substituted meso-porphyrins without g-pyrrole substituents were the most desirable for model systems applications. As shown in Route 4, these porphyrins require access to meso-substituted dipyrrometbanes.
a mese and P_substiMad dipyrromethane
Route
a @&stiiuted dipyrromethane
Route
Route
a mes~substituted dipyrromethane
dipyrromethane
ArCHO
i
R2
R3
R2
Scheme 1. Use of dipyrromethanes in routes to four types of trans-substituted porphyrins.
11427
11428
C.-H. LEE and J. S. LINDSEY
The chemistry of meso-substituted dipyrromethanes has been rather undeveloped. With the exception of the work by Nagarkatti and Ashley.9 who showed that condensation of 4-pyridine carboxaldehyde with pyrrole in acidified methanol afforded crystals of the hydrochloride salt of meso-(4pyridyl)dipyrromethane, direct syntheses of meso-substituted dipyrromethanes have emerged only recently. Casiraghi et al. prepared dipyrromethanes by reaction of aliphatic aldehydes with the bromomagnesium reagent of pyrrole in tbe presence of TiClq.lu Recently Vigmond et al. published a direct synthesis of meso-substituted dipyrromethanes involving reaction of pyrrole and an aryl aldehyde in tetrahydrofuran/acetic acid.11 A similar synthesis employing reaction in acidified methanol was described by Mizutani er ~1.1~ In addition to these direct syntheses, two stepwise syntheses of meso-substituted, g-unsubstituted dipyrromethanes have been developed.l3,14 We also have developed a one-flask synthesis of meso-substituted dipyrromethanes. We now present our approach, which appears to offer advantages for application in porphyrin chemistry. Route
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