Adsorption of oxygen and nitrogen on surface-modified carbons 1976 57 233-9

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Adsorption of nitrogen carbon monoxide carbon dioxide and nitic oxide on molecular sieves

Adsorption of nitrogen carbon monoxide carbon dioxide and nitic oxide on molecular sieves

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Adsorption
of N2, CO, COZ and NO: R. Ml Triebe and F: H. Tezel
common separations include those of CO., and NO, from impure air streams at approximately ambient conditions (i.e. pollutant removal from flue gases). A study was undertaken to screen some molecular sieves for potential separation of CO?, CO and NO from Nz. Many synthetic zeolites have been tested for possible separation of the mentioned compounds from N2. Haq and Ruthven studied adsorption of CO?. CH4, O2 and N2 on 4A and 5A zeo1ites8,9. and Ruthven studied single and binary gasbehaviour of CO. CH4, 0: and N2 adsorption on 5A zeolite”. Tezel and Apolonatos reported on the adsorption and diffusion of CO, CH4 and N2 in various synthetic zeolites’8. Adsorption of CO*, NO, NO* and SO2 on natural and synthetic mordenites and on 5A and 13X zeolites was studied by Ma and Mancell’, and NO adsorption on a large variety of metal impregnated and untreated activated carbons and zeolites was examined by Kaneko and Inouye16. Anderson has taken part in studies of CO, COz, OZ and N2 on 4A zeolite”.“, and Danner et trl. have studied combinations of the COiN2/02 systemson 5A and 10X zeo1ites”.‘4.‘5. The vast amount of data available on these systems demonstrates their significance in air purification applications. However, natural zeolites have not been examined in such great detail due to industrial disadvantages, such as inconsistency of composition and cost of possible purifications and modifications. A study of adsorption of COZ on various natural (mordenite, ferrierite, clinoptilolite and chabazite) and synthetic zeolites showed chabazite to be a more promising adsorbent for COz separation from Nl than 4A and 5A zeolite$. Adsorption of COz. SO? and NH3 on Hungarian clinoptilolites and mordenites has been studied by Kallo et ~1.“. An excellent review 01 the general structural and adsorptive properties of clinoptilolite has also been published in a series of articles20~33~36. These articles include experimental results comparing ion exchanged clinoptilolites to 4A zeolite for the separation of CH4 from Nz. Again the natural zeolites showed great promise and versatility for the specified separation. and the use of clinoptilolite for the CHd/Nz separation has been independently supported through a PSA separation study”. Despite such promising results, the data available on natural zeolite adsorption properties are scarce relative to results for synthetic zeolites. The advantages of natural zeolites can only be realized through detailed studies of their adsorption properties and of the roles of various exchangeable cations in the adsorption of gases. The molecular sieves chosen for screening studies were 4A and 5A zeolites, a synthetic H-Mordenite, a Turkish clinoptilolite and a high surface area activated carbon. The gas chromatographic method was used to determine the Henry’s law constants of each system over various temperature ranges between 243 and 473 K. The separation factors (ratios of Henry’s law constants) for NO. CO and COz from Nz on each molecular sieve were then calculated and compared to determine a favourable molecular sieve for separation of these common contaminants from N2. A favourable system, that of CO and Nz on the natural clinoptilolite, was then examined to determine the significance of various mass transfer resistances in a clinoptilolite packed column.

氧化镓基宽禁带材料退火研究

氧化镓基宽禁带材料退火研究

摘要摘要32O Ga -β是一种新型宽禁带氧化物半导体材料,禁带宽度大约为4.9eV ,具有良好的化学和热稳定性,在紫外探测器、功率器件等领域应用前景广阔。

由于蓝宝石与氧化镓的晶格常数、热膨胀系数不同,外延薄膜中存在大量的点缺陷、位错等,直接影响到后期制备器件的工作效率和可靠性。

本文采用在蓝宝石(0006)晶面上外延的32O Ga -β和32x -1x O )Ga Al -(β薄膜进行退火实验,研究了退火气氛、温度、时间等退火工艺参数对薄膜结晶质量、光学特性、表面组分等特性的影响。

同时,在氧化镓薄膜上制备了紫外日盲探测器,对比分析了在不同气氛中退火的薄膜上制备的探测器的性能及其微观机理。

共得到如下结论:第一,700C 条件下,随着退火时间的增长,晶体择优取向变好,表面平整度基本不变,吸收带边持续蓝移,光学带隙变大。

900C 条件下,衍射峰峰位随退火时间延长向小角度偏移,这是因为较高的退火温度引入的应力使得晶体内部发生了晶格畸变,且应力对于晶格常数的贡献大于高温衬底互扩散的贡献。

而1000C 条件下,铝镓氧的衍射峰先是在6h 时向小角度移动,然后随着退火时间的增长向大角度方向移动,这是因为较高的退火温度加上较长的退火时间使得衬底Al 原子向外延膜的扩散已经充分进行。

对于光学特性,随着退火时间的增加,薄膜的透过率均先增高后降低,这与薄膜表面粗糙度变化规律一致。

第二,800C 下对不同气氛中退火的氧化镓薄膜的研究发现,退火气氛对氧化镓的晶体结构影响整体上不明显,相比较而言,氮气退火效果较好。

对于表面形貌,退火后,薄膜表面小晶峰大量减小,粗糙度降低,平整度明显改善。

对于透射谱,氮气和空气中退火的样品光学带隙有所增加。

氧气中的薄膜的吸收带边则轻微红移,这可能是因为氧气气氛给薄膜引入了较多的间隙原子,形成了点缺陷,而缺陷能级吸收较低频率的光。

第三,探测器的I-V 曲线显示,氮气气氛中退火的样品制备的器件的光电流最大,其他气氛中退火后的电流则比参考片弱,因为结晶质量较高的晶体更有利于载流子的迁移,电导更大。

氧分子筛 吸附 回收率

氧分子筛 吸附 回收率

氧分子筛吸附回收率英文回答:Oxygen molecular sieves are highly efficient materials used for the adsorption and recovery of oxygen from various gas mixtures. These sieves are composed of porous materials, such as zeolites, which have a high affinity for oxygen molecules. The adsorption process involves the selective trapping of oxygen molecules within the pores of the sieve, while allowing other gases, such as nitrogen, to pass through.The adsorption capacity and recovery rate of oxygen molecular sieves are crucial factors in determining their effectiveness. The adsorption capacity refers to the amount of oxygen that the sieve can adsorb, while the recoveryrate measures the efficiency of the sieve in releasing the adsorbed oxygen. Higher adsorption capacity and recoveryrate are desirable as they allow for more efficient oxygen separation and purification processes.To illustrate this, let's consider an example of using oxygen molecular sieves in a medical oxygen concentrator. This device is used to extract oxygen from ambient air and deliver it to patients with respiratory conditions. The concentrator contains oxygen molecular sieves that selectively adsorb oxygen from the air, while allowing nitrogen and other gases to pass through. The adsorbed oxygen is then released and collected for use.In this scenario, a high adsorption capacity is necessary to ensure that sufficient oxygen can be extracted from the air. If the sieve has a low adsorption capacity,it would require a longer time to generate an adequate amount of oxygen, resulting in slower oxygen delivery to the patient.Additionally, a high recovery rate is important to maximize the efficiency of the oxygen concentrator. A low recovery rate would mean that a significant amount of adsorbed oxygen remains trapped within the sieve and cannot be released. This would result in a lower overall oxygenoutput and increased energy consumption, as theconcentrator would need to work harder to compensate forthe lost oxygen.中文回答:氧分子筛是一种高效的材料,用于从各种气体混合物中吸附和回收氧气。

(整理)污水处理英语词汇

(整理)污水处理英语词汇

污水处理英语词汇 AA/A/O 法anaerobic-anoxic-oxicprocess(厌氧-缺氧-好氧法)A-A-O 生物脱氮除磷工艺 A-A-O biological nitrogen andphosphorus removal process A-O 脱氮工艺 A-Onitrogen removal process A-O 除磷工艺 A-Ophosphorus removal process AB 法 Adsorption Biodegradation process(吸附生物降解法)总a 放射线 Total a radioactivity氨氮 ammonia-nitrogen 氨基酸 amino acid氨化反应 Nitragen铵盐 ammonium saltA/O 法(厌氧-好氧法)anaerobic-oxic process奥贝尔(Orbal)型氧化沟Orbal oxidation ditchB巴登福脱氮除磷工艺Bardenpho nitrogen and phosphorus removal process白水(漂洗废水) whitewater(bleaching water) 板框压滤 plate pressure filtration离心机 centrifugal machine半渗透膜semi-permeable membrane棒状杆菌属corynebacterium薄膜式淋水填料 filmpacking饱和常数(Ks) saturationconstant 暴雨公式 storm flowformula 暴雨径流 storm runoff溢流井 overflow well苯 benzene苯胺 aniline总B 放射性 Total Bradioactivity泵型叶轮暴气器 paddleimpeller aerator泵站 pumping stationBMTS 型一体化氧化沟BMTS intrachannel clarifieroxidation ditch 闭路循环 closed loop表面冲洗 surfacewashing表面负荷 surface load表面过滤 surfacefiltration 表面活性剂 surfactant表面活性物质 surface active additive agent表面曝气 surface aeration表面曝气器 surface aerator表面淹灌 surface flood irrigation表面冲洗装置 surface washing facility丙烯酸 acrylic acid 丙烯腈 acrylonitrile病毒 virus病原菌(致病菌) pathogen 病原微生物 pathogen microorganismBOD-污泥负荷BOD-sludge load补充水 make-up water 布朗运动 Brownian movement C财务评价 financial evaluation配水系统 distribution system侧渠型一体化氧化沟 integrated oxidation ditchwith side ditch产氢气乙酸菌 Rydrogenes and acetic aidgenes产甲烷细菌methanogenes产率系数 yield coefficient常规给水处理工艺 conventional water treatmentprocesses敞开式循环冷却水系统 opened recirculating coolingwater system超高纯水ultra-high-purify water超过滤 ultrafiltration超过滤膜法ultrafiltration membrane process沉淀 precipitation, sedimentation沉淀池 sedimentationtank沉砂池 grit chamber城市废水 municipalwastewater城市废水处理 municipal wastewater treatment澄清 clalification可持续发展 sustainable development充满度 degree of fullness重现期 exceedion interval, period of recurrence抽风式机械通风冷却塔 induced draft mechanical cooling tower臭氧发生器 ozone generator臭氧法 ozonation process臭氧消毒 ozonedisinfection 初次(级)沉淀池 primary clarifier, primarysedimentation tank除水器 drift eliminator除铁除锰 iron and manganese removal 除盐水(脱盐水) desalted water,demineralized water 除渣 desilication, silica removal除藻 algal removal 除氟 algal fluorine穿透曲线 penetration curve活性污泥法 activatedsludge process 生物脱氮工艺 biological nitrogen remo process船型一体化氧化沟 BoatType in intrachannelclarifier oxidation ditc纯(富)氧曝气法pure-oxygen aeration pro磁凝结 magnetic coagulation磁盘法 magnetic diskprocess 磁过滤法 magneticfierration process萃取 extraction萃取剂 extractant D 达西定律 Darcy ’s law大肠菌群Coliform-group bacteria大气泡曝气装置 large bubble aerator代谢 metabolism带式过滤 belt press filtration]单级传统消化池 single-stage conventional digester单螺旋式曝气装置single spiral aerator 氮 nitrogen氮循环 nitrogen cycle 蛋白质 protein倒虹管 inverted siphon 低放射性废物 low-level radio active waste 制浆废水 kraft mill wastewater敌百虫 dipterex敌敌畏 dichlorvos 涤纶纤维 polyester fiber地表漫流系统 overland flow system(OF)地表水 surface water地面(表)水环境质量标准 environmental quality standard for surface water地下滤场 underground filtration field地下渗漏 underground percolation地下渗滤系统 subsurface infiltrationsystem地下水 groundwater人工湿地系统artificial(constructed)wetland再生水回流地下水质标准water quality standard forrecharging parifiedwastewater water into groundwateraquifer地下水位 underground water level淀粉生产废水 starch producing wastewater点滴-薄膜式淋水填料splash-film packing点滴式淋水填料 splash packing 点污染源 pointpollufion source 电动电位electromotance potential电镀废水electroplating wastewater电极 electrode电解法 electrolyticalprocess电流密度 eletronic density电渗析 electrodialysis 电渗析器electrodialyzer电晕放电 brush discharge动态年成本 dynamic annual cost动植物油 oil and grease 对硫磷 parathion 多层床 multibed 多环芳烃 polycyclichydracarban 多氯联苯polychlorinated biphenyls(PCBs) E二次(级)沉淀池secondary clarifier, secondary sedimentation 二级处理 secondarytratament F 乏燃料 spent fuel 反冲洗 black washing反渗透(逆渗透)reverse osmosis 反渗透法 reverseosmosis process反渗透膜 reverse osmosis membrane反硝化,脱氮denitrification防止腐蚀 corrosion prevention纺丝 spining 纺织废水 textile wastewater放射性半衰期radioactive half-life放射性废水处理 radioactive wastewatertreatment放射性排出物radioactive effluent非点源污染(面源污染)non-point source pollution非离子氨 non-ionic ammonia废水处理 wastewater treatment废水中和neutralization of wastewaters分离 separation分流制 separate system分流排水系统separated sewer system酚 phenol焚烧 incineration 风吹损失 windageloss风筒式冷却塔chimmey cooling tower封闭循环系统 closedrecirculation system氟化物 fluoride辐射流沉淀池 radial flow sedimentation tank浮盖式消化池floating-cover digester气浮 flotation 福斯特利帕除磷工艺 Phostrip phosphorus removal process福列德克斯脱氮除磷工艺 Phoredox nitrogen and phosphorus removal process 腐蚀 corrosion富营养化eutrophication富营养化湖泊、水库 eutrophic lake,eutrophicreservoirGr 射线 gamma rays 甘蔗废水 sugarcanewastewater 干化 drying干化床 drying bed冷却塔 cooling tower钢铁工业废水 iron and steel mill wastewater高纯水 ultrapure water 高放废物 high-level radio active wastes高份子电解质polymolecular electrolye高份子絮凝剂polymolecular floc高负荷活性污泥法 high-loading activatedsludge method高负荷生物滤池 high loading biological filte高炉煤气洗涤水wastewater produced fromscrubbing blast furnacegas高锰酸盐指数 potassium permanganate index高速消化池 high-rate digester高梯度磁分离器(HGMS) high grade magnegic separator高浊度水 high turbiditywater 格栅 bar screen 隔板反应池 bafflereaction tank隔板式混合槽 baffle mixer隔油池 oil separator 镉 cadmium铬 chromium给水泵站 water pumping station给水处理 water treatment给水网管系统 water supply system工业水处理与循环系统industrial water treatment and recirculation system工业废水 industrial wastewater汞 mercury鼓风曝气 blast aeration 鼓风式机械通风冷却塔 forced draft mechanicalcooling tower固定螺旋式曝气装置fixed spiral aerator景观、娱乐水体landscape and recreation waterbody管道接口 conduit joint 给水配水系统 watersupply piping distribution system网管平差 balancingnetwok 罐头生产废水 Cannerywastewater硅藻土 cilicious mar H海水淡化demineralization of sea water含酚废水 phenol contained wastewater含水量 moisture content含盐量 saline capacity 含油废水 oily wastewater旱流污水量(DWF)dry-weather flow 好氧生物处理 aerobicbiological treatment 好氧塘 aerobic pond 好氧稳定 aerobic stabilization合成洗涤剂 synthetic detergent合成纤维 synthetic fiber合成纤维废水 synthetic fiber wastewater 合成橡胶 synthetic rubber合流城市废水 combinedmunicipal wastewater合流制排水系统combined sewer system水体功能分类 waterbodyfunction classification核能工厂 nuclear power station核燃料循环 nuclear fuel cycle核素 nuclide冶金工业废水metallurgical industrywastewater黑液 black liquor 黑液除硅sillica-elimination fromblack liquid虹吸滤池 siphon filter 化学处理 chemicaltreatment化学工业 chemicalindustry化学吸附 chemicaladsorption 化学纤维 chemical fiber化学需氧量 chemicaloxygen demand (COD)环状管网系统 grid pipe network system缓蚀 corrosion inhibition缓蚀剂 corrosion inhibitor磺化煤 sulfonated coal 挥发酚 volatile phenol 回流比 recycle ratio 回流污泥率 return sludge ratio汇水面积 catchment area, collection area混合 mixing混合床 miced bed 混合液挥发性悬浮固体mixed liquor volatile suspended solids(MLVSS) 混合液悬浮固体 mixed liquor suspended solids(MLSS)混凝 coagulation 混凝沉淀coagulation-sedimentation 混凝剂 coagulant 浑浊度 tubidity活化产物 activation products硅酸钠 sodium silicate 活性剂 activator活性染料 active dye 活性炭 activated carbon活性炭的再生re-generation of activated carbon活性炭吸附 activecarbon adsorption活性污泥 activated sludge 活性污泥法 activatedsludge process 活性污泥负荷 activatedsludge loading活性污泥驯化acclimation of activatedsludge J机械反应池 mechanicalreactor机械剪切曝气装置mechanical shearing aerator机械搅拌 mechanicalmixing机械搅拌澄清池accelerator机械曝气 mechanicalaeration机械通风冷却塔mechanical draft cooling tower 机械脱水 mechanicaldewatering极化现象 polarization级配 granularcomposition集水池 collection well集中处理(合并处理)joint treatment计算机 computer 计算机辅助设计computer aid design加速过滤器accelo-filter加压气化 pressure-gasification甲基对硫磷 parathion methyl甲醛 formaldehyde甲烷 methane甲烷发酵 methane fermentation 甲烷气体 methane gas间歇式活性污泥系统sequencing batch reactoractivated sludge system(蒹性塘 facultative pond检查井 manhole 减压薄膜蒸发法decreasing pressure andthin-film evaporation process碱法制浆 soda pulping process浆粕 pulp降雨历时 duration of rainfall降雨量,降水precipitation浇洒道路用水 street flushing water焦化废水 coking wastewater交替工作式氧化沟alternative operating oxidation ditch交替运行的生物滤池alternative operating trickling filter胶体 colloid阶段曝气 step aeration 接触池 contact chamber 接触氧化法 contactoxidation process 结垢 scale节水 water saving 锦纶纤维 polyamide fiber腈纶纤维 acrylic fiber 精制塘(深度处理塘) polishing pond经济效益 economic benefit径流系数 runoff coefficent静态年成本 static annuity cost景观娱乐用水水质标准 water quality standard forlandscape and recreation area酒精工业 alcoholdistilery就地处理系统(小型处理)on-site treatment systems(small scale facilities)聚丙烯酰胺polyacrylamide聚丙烯酰胺水解体polyacrylamide hydrolysis product聚合 polymerize聚合度 polymerizingdegree聚合氯化铝polyaluminum chloride均衡池(塘) equalizaliontank(basin,lagoon)K卡罗塞式氧化沟Corrousel oxidation ditchK 型叶轮曝气机 K type impeller aerator凯式氮 kjeldahlnitrogen空气驱动式生物转盘aero biological disks孔隙率 porosity快滤池 rapid filter快速渗滤系统 rapid infiltration system(RI) 矿井 shaft(mine)矿区 mining area 矿区环境 mining area environment 矿山废水 minery wasterwater矿山酸性废水 acid minewastewater 扩散板 diffusion plate扩散管 diffusion tube扩散盘(罩) diffusion disc(cover) L乐果 dimethoate冷凝 condensation 冷凝水 condensate water 冷却 cooling冷却池 cooling pond 冷却塔 cooling tower 冷却塔配水系统 coolingtower distribution system 冷却循环水 circulated cooling water冷轧 cold steel -rolling离心泵 centrifugal pump 离心 centrifugation force离心机 centrifugal machine离心脱水 centrifugal dewatering离心作用centrifugation离子交换 ion exchange离子交换剂 ion exchanger离子交换膜 ion exchangemembrane离子交换树脂 ion exchange resin粒径 grain size砾石承托层 gravel support炼钢厂废水steel-making process wastewater炼铁 iron-smelting 炼铁(高炉)废水 blast furnace wastewater炼油厂废水 refineryprocessing waserwater淋滤 leaching淋水密度 waterdrenching density淋水面积 waterdrenching aera淋水填料 packing磷 phosphorus 磷酸盐 phosphate生物流化床 Biologicalfluidized bed硫化物 sulphide硫化物沉淀法 precipitation with sulphide硫酸铵 ammonium sulfate硫酸钙 Calcium sulfate 硫酸铝 aluminum sulfate 硫酸镁 magnesiumsulfate硫酸铁 ferric sulfate 硫酸亚铁 ferrous sulfate硫酸盐 sulfate 硫循环 sulphur cycle 铝酸钠 sodium aluminate 滤层 filter layer滤池冲洗水量 filter washing water consumptio滤池配水系统 filterunderdrain system滤池运行周期 filtercycle time滤床 filter bed 滤料 filtering medium滤速 filtration rate 滤液 filtrate 氯 chlorine氯-氨法chlorine-ammonia process氯化,加氯处理 chlorination氯化物 Chlorides螺旋桨式快速搅拌机 propeller-type high speeagitatorM马拉硫磷 malathion脉冲澄清池 pulsator慢滤池 slowfilter慢速渗滤系统 slow rate infiltration system (SR) 煤气 coal gas 煤气厂 gas work煤气发生器 coal gas generator煤气发生站 gasgeneration station 煤气净化 coal gas purification煤炭 coal 锰 manganse米门公式 Michaelis - Menten equation莫诺德公式 Monod equation密闭式循环冷却水系统closed recirculating cooling water system密集多喷嘴曝气装置compact multinozzle aerator 面污染源 non-point pollution source敏感性分析 sensitivity analysis膜分离装置 membrane seperator膜选择性 membrane selectivity膜污染 membrane foulting膜中毒 membrane poisoningN难生物降解有机物nonbiodegradable organies 尼龙 nylon逆流漂洗counter-current washing 逆流式冷却塔counterflow cooling tower逆流再生counter-current regeneration粘胶 rayon酿酒废水 winery wastewater酿造与发酵工业废水 brewery and fermentation industrial wastewater凝结 coagulation凝结剂 coagulant牛奶生产废水 dairywastewater 浓缩 concentration浓缩倍数 cycle of concentration浓缩池 thickening tank浓缩污泥 concentrated sludge农田灌溉水质标准 standards for irrigationwater quality农用污泥中污染物控制标准 contaminants controlstandard for sludge farm农药 pesticide 农药厂废水 pesticideplant wastewaterP排泥系统 sludge - discharge system排水量 discharge排水管 drain pipe排水口 outlet排水系统 sewer system排污 blowdown泡沫分离 foam phaseseparation配水网管 distributionsystem ,pipe system 喷灌 spray irrigation喷水池 spray pond 皮革 leather 啤酒废水 brewery wastewater啤酒废水处理 brewery wastewater treatment漂白 bleaching平板式膜 plate membrane平板式叶轮曝气器 plate impellar aerator平衡吸附容量equilibrium adsorption capacity平流式沉砂池 horizontal flow grlt removal tank平流式沉淀池horizontal flow sedimentation tank 普通生物滤池biological filter,trickling filter曝气 aeration曝气沉砂池 aerationgrit chamber曝气池 aeration tank曝气栅 aeration boom曝气设备 aerationequipment曝气时间 aeration time曝气装置,曝气机aerator居民生活垃圾 HouseholdWaste庫底平整線 bottom flattingline of the site庫區填埋邊線 landfill sideline of the site庫容 Storage capacity垃圾 Waste ,Solid Waste 垃圾壩 waste dam 垃圾殘渣 residue垃圾槽 waste chute 垃圾層 waste layer 垃圾產量 Waste output垃圾堆肥場 waste compostingfield 垃圾堆體 waste pile 垃圾副壩 secondary waste dam 垃圾揀選場 Waste Sorting Site垃圾氣化 waste gasification垃圾采集車 waste collector垃圾桶 garbage ,rubbishbarrel垃圾箱 garbage container 垃圾壓實系統 wastecompactor system垃圾衍生燃料 Refuse-derivedfuel (RDF)垃圾衍生燃料 waste derivedfuel垃圾轉運車 waste transfer truck垃圾轉運站 waste transferstation垃圾裝卸坡 waste loadingramp離心脫水機 centrifugaldewaterer鈉基膨潤土 sodium bentonite農業廢棄物 AgriculturalWaste 濃縮池 thickening tank 排放 discharge排泥閥 sludge valve排水口 Drain Outlet 膨潤土 bentonite熱解 Pyrolysis 溶解氧測定儀(DO 計) dissolved oxygen meter (DO meter ) 砂水分離機 grit-water splitter 商業垃圾 Commercial Waste 上橫沖填埋場 ShanghengchongLandfill Site上清液 supernatant liquor設備選型 Type selection of equipment 滲濾液(垃圾滲濾液) leachate 滲濾液處理 leachatetreatment滲濾液處理站 Leachate Treatment Station滲濾液采集及導排氣系統平面圖 Plan of Leachate Collection and Guiding a Exhaust System 滲濾液采集盲溝 blind drain for leachate collection精品文档精品文档 生活垃圾 Domestic waste 生活垃圾焚燒污染控制標准 Standard for Pollution Control on the Municipal Solid Waste Incineration 剩余污泥 excess sludge 剩余污泥泵 excess sludge pump 輸渣機 clinker conveyer 豎向石籠 vertical stone cage雙層防滲結構 double-linersystem水位 water level提升泵站 lift pumpingstation填埋(垃圾) Landfill填埋場 Landfill site填埋場封場 seal of landfillsite填埋場總體布置圖 GeneralLayout of Landfill Site填埋場縱斷面示意圖 SketchMap of Landfill Site VerticalSection填埋庫區 Landfill Area填埋庫區平面布置圖 PlaneLayout of Landfill Area1:1000填埋氣 Landfill gas砼 concrete圖例 legend土工合成材料黏土墊層Geosynthetics Clay Liner(GCL)土工膜 geomembrane脫水機 dewaterer脫水機房 dewatering house衛生填埋 sanitary landfill渦流沉砂池(旋流沉砂池)vortex grit tank污泥泵房 sludge pumping room污泥處理 sludge treatment污泥處理流程示意圖 FlowChart of Sewage TreatmentProcess污泥管線 sludge pipeline 污泥濃度計(MLSS 計) sludge concentration meter (MLSS meter ) 污泥濃縮及脫水機房 Sludge Thickening & Dewatering House污泥脫水車間 sludge dewatering workshop 污水泵 sewage pump 污水處理 sewage treatment 污水處理厂 Wastewater Treatment Plant 污水處理流程示意圖 Sewage Treatment Process Sketch Map 污水管線 sewage pipeline 污水水面 wastewater surface 無線傳輸 wireless transmission 吸水井 suction well 消毒池 disinfecting tank 新聯村熊家窯 Xiongjiayao, Xinliancun 序批式活性污泥法(SBR 法) Sequence Batch Reactor 選型 Type selection 壓縮式垃圾車 waste compactors 厭氧、缺氧、好氧 Anaerobic, Anoxic, Aerobic Underwater Blender 厭氧堆肥 anaerobic composting 厭氧發酵 methane fermentation; anaerobic fermentation 厭氧流化床反應器 anaerobic fluidized bed 厭氧流化床反應器 anaerobic fluidized bed 氧化溝 oxidation ditch 氧化溝 oxidation ditch 葉輪曝氣機 impeller aerator 一級發酵(初級發酵) primary fermentation醫院垃圾 Hospital Waste 營養土層 nutritious soil layer預留垃圾綜合利用生產用地Reserved Waste Comprehensive Utility and Production L再生 reclamation 柵渣 sediment 黏土層 clay layer 支盲溝 blind sub-drain 至垃圾填埋場 to the waste landfill site 終期覆土 terminal earth covering 主盲溝 main blind drain 自控系統 autonomous system 自然土層 natural soil layer。

空分双塔制氮流程原理

空分双塔制氮流程原理

空分双塔制氮流程原理The principle of pressure swing adsorption (PSA) technology is to separate nitrogen from air by using the difference in adsorption capacity of nitrogen and oxygen on the surface of the adsorbent. 压力摆动吸附(PSA)技术的原理是利用氮气和氧气在吸附剂表面的吸附能力差异来从空气中分离氮气。

In the twin tower nitrogen generation process, two adsorption towers are used to produce nitrogen gas.在双塔制氮过程中,使用两座吸附塔来生产氮气。

During the first step, compressed air is driven into one of the towers where the oxygen is captured by the adsorbent material, allowing the nitrogen to pass through for collection.在第一步骤中,压缩空气被送入其中一座塔,氧气被吸附剂材料捕获,允许氮气通过以便收集。

As the first tower reaches its adsorption capacity, the process switches to the second tower, allowing for continuous production of nitrogen.当第一座塔达到吸附容量时,过程切换到第二座塔,允许连续生产氮气。

The twin tower nitrogen generation process is a reliable and efficient method for producing high-purity nitrogen gas for a wide range of industrial applications.双塔制氮过程是一种可靠高效的方法,可以用于各种工业应用中生产高纯度氮气。

Adsorption of Nitrogen, Oxygen and Argon on Na-CeX Zeolites

Adsorption of Nitrogen, Oxygen and Argon on Na-CeX Zeolites

Adsorption8:271–278,2002c 2002Kluwer Academic Publishers.Manufactured in The Netherlands.Adsorption of Nitrogen,Oxygen and Argon on Na-CeX ZeolitesAMBALA V ANAN JAY ARAMAN AND RALPH T.Y ANG∗Department of Chemical Engineering,University of Michigan,Ann Arbor,MI48109-2136,USAyang@SOON-HAENG CHOKorea Institute of Energy Research,71-2,Jangdong,Yusongku,Taejon305-343,KoreaTHIRUMALESHWARA S.G.BHAT AND VENKATESHW ARLU N.CHOUDARYResearch Centre,Indian Petrochemicals Corporation Limited,Vadodara391346,IndiaReceived September19,2001;Revised June20,2002;Accepted October1,2002mercial type X zeolites(Linde13X)are nitrogen selective.Oxygen is the less abundant component in air;hence oxygen selective sorbents are desired for air separation.Mixed Na-Ce type X zeolites containingdifferent ratios of Ce3+/Na+ions are prepared by partial ion exchange of commercial X zeolite.The adsorptionisotherms of nitrogen,oxygen and argon are measured and the pure-component selectivity ratios are compared andanalyzed against commercial zeolites(13X)for air separation.Oxygen selectivity over nitrogen(∼1.5)and argon(∼4.0)are seen for mixed Na-Ce type X zeolite(Si/Al=1.25;Ce3+/Na+<4.0)from Henry’s constant determined from low pressure adsorption measurements.The oxygen and nitrogen isotherms cross over for mixed Na-Cetype X zeolite(Si/Al=1.25;Ce3+/Na+<4.0),and the pressure at which cross they over increases as Ce3+/Na+ approaches1.The oxygen selectivity as claimed in the patent by N.V.Choudary,R.V.Jasra,and S.G.T.Bhat(US Patent no.6,087,289,2000)is seen only at very low pressures in the volumetric adsorption measurement and the hydrogen treatment of the Ce-exchanged samples have no effect on the adsorption characteristics.Keywords:Ce-X zeolite,nitrogen sorbent,sorbent for air separation,Ce-ion exchangeIntroductionNitrogen and Oxygen are two of the most widely pro-duced chemicals in the world,ranked the second and third in quantities of production.Cryogenic distilla-tion of air is the primary technology used for the pro-duction of these gases.There are other processes now being employed successfully.Among them adsorp-tion based systems have improved by leaps over the last two decades and have been an alternative technol-ogy for industrial production of nitrogen and oxygen (Yang,1997).Approximately20%of air separation is ∗To whom correspondence should be addressed.presently through adsorption based separation systems (Rege and Yang,1997).Synthetic zeolites(A,X and Y)have been used in commercial pressure swing adsorption(PSA)systems for air separation.These zeolites are nitrogen selective, i.e.,adsorbing N2more strongly than O2at a ratio of approximately4:1due to the interaction between the N2and the charge compensating cation present in the zeolites.Among the cations,Li+gives strong interac-tions with N2(McKee,1964),and its use was greatly increased in recent years with the following advances in LiX sorbents:(1)Li+ion exchange must exceed 70%occupancy threshold to have any effect on the N2 adsorption(Chao,1989;Chao et al.,1992;Coe et al.,272Jayaraman et al.1992),and(2)there is a significant increase in N2ad-sorption for Li+ion-exchanged low silica X-type ze-olites over commercial LiX zeolite.The best N2se-lective zeolite now used commercially is the Li-LSX (Si/Al=1.0)(Rege and Yang,1997;Yang,1997).It is also known that the addition of small amounts of Ag+ (e.g.,1–3cations/cavity)can further improve both the sorbent selectivity and N2capacity(Yang and Hutson, 1998;Hutson et al.,1999).Separation of air by adsorption of the less abundant component(O2)is more desirable,and active research is being carried out to produce a material that adsorbs oxygen preferentially to nitrogen for use in industrial adsorption systems.Carbon molecular sieves(CMS) are oxygen selective in the case of kinetic separation of air in a PSA system(Juntgen et al.,1981;Chen et al., 1994).4A zeolite has also been used for kinetic separa-tion of air(Yang,1997).Oxygen binding complexes of cobalt remain the only possible oxygen selective sor-bents(based on equilibrium)with a potential for air sep-aration(Li and Govind,1994;Ramprasad et al.,1995; Jones et al.,1979;Niederhoffer et al.,1994;Hutson and Yang,2000).Air contains0.94mole%argon which serves as a limiting factor for the maximum oxygen purity achieved(∼95%).Some applications like welding and cutting processes,plasma chemistry,Ozone generator, breathing oxygen at high altitudes in pressurized space suits and laboratory applications require oxygen purity greater than99%.This necessitates argon-oxygen sep-aration through cryogenic distillation(Egoshi et al., 1999,2000)or kinetic separation using molecular sieves(Miller and Theise,1989).The crude argon produced during cryogenic distillation of air contains nitrogen and oxygen(3–5%).The argon purity can be enriched by catalytic hydrogen combustion or low temperature oxygen adsorption in an oxygen selec-tive synthetic zeolite(Choudary et al.,2000).Some Ag-zeolites have been shown to have a selectivity for Ar over O2(Hutson et al.,1999;Knaebel and Kandybin, 1993),hence can be used for this separation(Knaebel and Kandybin,1993).Several hybrid membrane-PSA systems have also been considered for producing high purity O2by using the higher permeability of Ar. Choudary et al.(2000)disclosed interesting air sepa-ration properties of CeX zeolites based onfirst-moment analyses of chromatography data.In this work,mixed Na-Ce type X zeolites contain-ing different ratios of Ce3+/Na+ions were prepared by partial ion exchange of a commercial X zeolite.The adsorption isotherms of nitrogen,oxygen and argon were measured and the pure-component selectivity ra-tios(KN2/KO2)were compared and analyzed against commercial zeolites for air separation. Experimental DetailsMaterialsCommercial X-type zeolite with a Si/Al ratio of1.25 (Linde13X,lot945084060002)in the form of binder less,hydrated powders was used.Helium(99.995%, prepurified,Cryogenic Gases),oxygen(99.6%,extra dry,Cryogenic Gases),nitrogen(99.998%,prepuri-fied,Cryogenic Gases)and argon(99.998%,prepuri-fied)were used as obtained.Cerium chloride hydrate (CeCl3·6H2O,99%,Strem Chemicals)and deionized water were used for the preparation of cerium(III) chloride solution for ion exchange.Deionized waterwere was used for sample washing and silver nitrate (AgNO3),99.9%Strem Chemicals)was used to con-firm the absence of Cl−ions in the washings.Preparation of SorbentsThe mixed Na-Ce zeolites were prepared by conven-tional batch ion-exchange of X type zeolite using 0.085M(2.1wt%)aqueous solution of cerium(III) chloride at95◦C for24h.Three different samples of Na-CeX zeolites were prepared each using10X(Na-CeX#10),5X(Na-CeX#5)and1X(Na-CeX#1)the the-oretical(100%)Ce3+needed for ion exchange.The samples werefiltered and washed with hot deionized water until the solution showed the absence of chlo-ride(i.e.,no precipitation upon treatment with AgNO3). The adsorbents were dried overnight at100◦C in air. For comparison against the oxygen selective cerium exchanged X type zeolites produced by Choudary et al.(2000),a sample of Na-CeX zeolite(sample id. CeXP-1)containing Ce3+/Na+ratio of3.3was pre-pared following similar procedure.Composition of Na-CeX ZeolitesThe zeolite samples were compositionally analyzed us-ing neutron activation analysis(NAA)in the research nuclear reactor of the Phoenix Memorial Laboratory at the University of Michigan.The samples were exposed sequentially to1-minute coreface irradiation deliveredAdsorption of Nitrogen,Oxygen and Argon on Na-CeX Zeolites273via pneumatic tube to a location with an average ther-mal neutronflux of2.13×1012n/cm2/s.Two separate counts of the resulting gamma ray activity were made, one after a13-minute decay and a second count after 1h and56min decay;both were for500s.Element concentrations for Al and Na were determined based on comparison with three replicates of the standard reference material NIST1633A(coalfly ash)while CeO2was used as basis for determining Ce content.A fourth replicate of each material was included as a check standard.Hydrogen TreatmentThe absorbent samples were loaded into reaction tubes (TPR tubes)and heated from ambient to400◦C and held at400◦C for12h with60cc/min of hydrogen.The sam-ple was cooled to room temperature and the samples were quickly transferred to the Micromeritics analysis glass tubes and sealed for isotherm measurements. Adsorption IsothermsThe adsorption isotherms were measured using a static volumetric system(Micromeritics ASAP-2010) (Hutson et al.,2000).Prior to measurement of isotherms,the samples were treated with hydrogen and then activated in a vacuum at300–400◦C for a mini-mum of4h.Results and DiscussionChemical AnalysesAs mentioned in the experimental section,the samples were analyzed for their composition using neutron ac-tivation analysis(NAA).In this analysis the Si concen-tration were pre-specified.Results of these analyses are given Table1.The unit cell composition for those ana-lyzed samples are calculated using a basis of86Al/u.c. and the results are tabulated in Table2.The ratios of Ce3+/Na+ions for the samples are listed in Table3. As seen from the results it could be said that the extent of Ce exchange accomplished depends on the amount of excess cerium(III)chloride solution used and100% Ce-exchange is difficult to achieve and needs consec-utive exchanges.Table1.Elemental composition of Na-CeX(Si/Al=1.25)zeolite samples.CeX#10CeX#5CeX#1Comp.wt%+/−wt%+/−wt%+/−Al12.5770.08612.2080.08112.3720.081 Ce22.1260.42922.4520.47017.3470.458 Na0.6270.0160.8850.022 2.4880.056Table2.Unit cell composition for the Na-CeX(Si/Al=1.25) zeolite samples.Comp.CeX#10(atm/uc)CeX#5(atm/uc)CeX#1(atm/uc)Al86.086.086.0Si107.5107.5107.5Ce27.026.522.0Na 5.0 6.520.0O387.0387.0387.0Adsorption IsothermsThe Na-CeX sorbent samples after the hydrogen treat-ment are degassed in vacuum at400◦C for4hours. The equilibrium isotherms of nitrogen and oxygen on the various sorbent samples prepared in this study were measured using Micromeritics ASAP2010unit as men-tioned earlier.Figure1shows the nitrogen and oxygen isotherms measured at22◦C for NaX(commercial type X zeolite).Figures2through4show the adsorption isotherms of nitrogen and oxygen for various samples prepared in this study.The isotherms arefitted with both Langmuir equation(Yang,1997)and Virial equa-tion(Reid et al.,1998;Sun et al.,1998).Langmuir equation:q=KP1+BP(1) Virial equation:lnPq=A0+A1q+A2q2+ (2)andK=exp(−A0)(3)where q is the amount adsorbed per unit weight of the sorbent and K is the Henry’s constant.Both Langmuir equation(1)and Virial expansion(2)reduce to Henry’s274Jayaraman et al.Table ngmuir isotherm parameters for N 2/O 2on Na-CeX from volumetric measurement.NitrogenOxygenSorbent a Ce 3+/Na +Degas temp (◦C)K (mmolg −1atm −1)B (atm −1)K (mmolg −1atm −1)B (atm −1)Pure-componentadsorption selectivity O 2/N 2NaX 04000.5900.2810.1620.2570.27CeX#10 5.84000.2310.4580.1560.4260.68CeX#5 4.24000.2200.5310.1870.3940.85CeX#11.14000.2370.2970.2990.7531.26a Referto text for preparation condition for thesorbents.Figure 1.Nitrogen and oxygen adsorption isotherms on NaX (Linde —13X)zeolite at 22◦C after degassing at 400◦C for 4hours.Figure 2.Nitrogen and oxygen adsorption isotherms on CeX#10(Na-CeX;Si/Al =1.25;Ce 3+/Na +=5.8)zeolite at 22◦C after de-gassing at 400◦C for 4hours.Law (q =KP )in the low pressure region.The fit-ted Langmuir and Virial parameters are provided in Tables 3and 4,respectively.The adsorption isotherms were also measured without hydrogen treatment of the samples and found to give identical results to those measured after hydrogen treatment within the limits of experimental error.With hydrogen treatment we ex-pect the Ce 3+to be reduced and the adsorption resultsshow that either the reduction of Ce 3+is minimal or did not have any effect on both N 2and O 2adsorption isotherms.Figures 2and 3show equilibrium selectivity (q N 2/q O 2)towards nitrogen while Fig.4has a cross-over point and the equilibrium selectivitychangesFigure 3.Nitrogen and oxygen adsorption isotherms on CeX#5(Na-CeX;Si/Al =1.25;Ce 3+/Na +=4.2)zeolite at 22◦C after de-gassing at 400◦C for 4hours.Figure 4.Nitrogen and oxygen adsorption isotherms on CeX#1(Na-CeX;Si/Al =1.25;Ce 3+/Na +=1.1)zeolite at 22◦C after de-gassing at 400◦C for 4hours.Adsorption of Nitrogen,Oxygen and Argon on Na-CeX Zeolites275Table4.Virial parameters for N2/O2adsorption isotherms on Na-CeX(Si/Al=1.25)from volumetric measurement.Virial parametersKN2O2(mmol g−1atm−1)Sorbent a A0A1A2A0A1A2N2O2Pure-component adsorption selectivity O2/N2NaX0.5540.3020.397 1.772 3.113−8.2840.5750.1700.30 CeX#10 1.243 6.564−18.482 1.54012.262−58.7890.2880.2140.74 CeX#5 1.366 5.888−13.861 1.4088.415−30.7480.2550.2450.95 CeX#1 1.329 3.351−7.5750.74810.810−29.5120.2650.474 1.79a Refer to text for preparation condition for the sorbents.Table5.N2/O2/Ar adsorption on Na-CeX from gas chromatography data(Choudary et al.,2000).Henry constant Pure-component adsorptionK(mmol g−1atm−1)selectivity ratiosAdsorbent a Ce3+/Na+O2N2Ar O2/Ar O2/N2N2/ArNaXP00.16210.48430.1510 1.10.3 3.2 CeXP-1 3.30.32120.21780.0780 4.1 1.5 2.8 CeXP-38.00.15200.26650.0730 2.10.6 3.6 CeXP-416.50.26850.26340.0719 3.8 1.0 3.7 CeXP-1b 3.30.21580.18140.0567 3.8 1.2 3.2a Refer to Choudary et al.(2000)for detail sample preparation conditions.b Low pressure adsorption isotherm measured in a volumetric apparatus in this study using the sample preparedsimilar to CeXP-1sample of Choudary et al.(2000).Henry constant determined using Virial equation.from oxygen to nitrogen as the pressure increases.Choudary et al.(2000)have prepared oxygen selectivecerium exchanged X zeolites.Table5gives a summaryof nitrogen,oxygen and argon adsorption on mixedNa-Ce type X zeolite measured by gas chromatogra-phy by Choudary et al.(2000).The best oxygen selec-tive X zeolite from the work of Choudary et al.(2000)is prepared in this study and low pressure adsorptionisotherms of nitrogen,oxygen and argon are measured.The Henry’s constants determined from virial expan-sion along with adsorption selectivity are provided inTable5.The values of Henry’s constant obtained fromvolumetric adsorption data are slightly lower than thevalues from Choudary et al.(2000)These selectiv-ity ratios are comparable to gas chromatography data(Choudary et al.,2000).Figure5shows the adsorp-tion isotherms of nitrogen,oxygen and argon on mixedNa-Ce type X zeolite(Na+:Ce3+=1:3.3).Figure6 shows the very low pressure region of the isothermsshown in Fig.5.From thesefigures it is seen thatthe equilibrium adsorption selectivity changes fromoxygen to nitrogen and there is a cross over pointseen Figure5.Nitrogen,oxygen and argon adsorption isotherms on CeXP-1∗(Ce3+/Na+=3.3)zeolite at30◦C after degassing at300◦C for several hours.(∗sample preparation condition refer to Choudary et al.,2000).in the oxygen,nitrogen isotherms(Fig.6).Similar effect is also seen in the volumetric adsorption data of nitrogen and oxygen on mixed Na-Ce type X zeolite (Na+:Ce3+=1:1.1)shown in Fig.4.Quantitative comparisons of the O2/N2selectivity ratios for the276Jayaraman etal.Figure 6.Nitrogen,oxygen and argon adsorption isotherms on CeXP-1∗(Ce 3+/Na +=3.3)zeolite at 30◦C after degassing at 300◦C for several hours (low pressure data from Fig.5).various samples used in this study are given in Tables 3and 4.The selectivity ratios from Langmuir equation and Virial expansion are comparable except for the sample —CeX#1(i.e.,low Ce)because of the reversal in selectivity seen at higher pressure.The equilibrium adsorption selectivity (O 2/N 2)decreases as the cerium exchange increases and it is greater than one for mixed Na-Ce type X zeolites with Ce 3+/Na +<4.The com-mercial X zeolite which has Ce 3+/Na +=0is nitrogen selective.This implies that very small Ce 3+/Na +ratio per unit cell is needed for the oxygen nitrogen isotherms to cross over.Figure 7shows the variations of the Henry constant and pure-component adsorption selectivity ra-tios as a function of Ce 3+/Na +ratio per unit cell.The Henry constant for N 2adsorption decreases as the Ce 3+Figure 7.Pure-component adsorption selectivity ratios and Henry constant plotted against Ce 3+/Na +ratio per unit cell.increases while that of O 2adsorption increases and then decreases towards higher Ce 3+/Na +ratio.The commercial X zeolite has 86Al −ions thereby 86charge compensating Na +ions on the extra-framework sites.Sixteen Na +ions are located in the hexagonal prism or in the sodalite cage,thirty-two of the Na +are located in the large cavities,almost in the plane of the 6MR rings,which connect the supercages and the sodalite cages.The remaining thirty-eight are in constant motion in the large cavities (Sherry,1966).The N 2Na +interactions are stronger than O 2Na +interactions giving rise to nitrogen selectivity.Ce 3+are trivalent ions hence exchanging Na +with Ce 3+re-duces the number of charge compensating cations and thereby reducing the adsorption amount for nitrogen and bringing it to the levels of oxygen.Ce 3+being trivalent will take up different site locations compared Na +hence bringing about the changes in adsorption characteristic.In a fully exchanged Ce-X zeolite four Ce 3+cations are found to be in the center of the hexag-onal prism,twenty-four are found to be within the sodalite cage near the 6MR comprising the hexag-onal prism and at most one in the center of the 12-membered ring (Hunter and Scherzer,1971).The pres-ence of mixed cations on extra-framework sites may re-sult in partial occupancy of sites and these will change as the Ce 3+/Na +ratio changes.With partial Cerium exchange there could be more Ce 3+ions occupying the 12-membered ring sites there by exposing them-selves for adsorption.This could be due to Na +ions occupying the inner sites in the hexagonal prism andAdsorption of Nitrogen,Oxygen and Argon on Na-CeX Zeolites277the sodalite cages(Barrer,1978).From the adsorp-tion data measured on the samples prepared here wefind a threshold ratio of Ce3+/Na+per unit cell tobe3.3below which we see oxygen selectivity in thelow pressure region.There is also a lower limit tothis ratio since NaX zeolite with Ce3+/Na+=0does not show oxygen selectivity and it is obvious that asthe ratio goes down so does the absolute number ofCe3+ions present per unit cell and there by bring-ing down the Ce3+number in the main cavity too.Inthis study a lower limit to Ce3+/Na+ratio of1.1waslocated.ConclusionsAdsorption characteristics of nitrogen,oxygen andargon on mixed Na-Ce type X zeolites are studied.The hydrogen treatment of Ce-exchanged samples isfound to have no effect on the adsorption character-istics of nitrogen and oxygen.Oxygen selectivity isseen for mixed Na-Ce type X zeolite(Si/Al=1.25;Ce3+/Na+<4.0)from Henry’s constant determined from low pressure adsorption measurements.Oxy-gen and nitrogen isotherms cross over for mixed Na-Ce type X zeolite(Si/Al=1.25;Ce3+/Na+<4.0) and the pressure at which they cross over increases as Ce3+/Na+approaches1.The oxygen selectivity described by Choudary et al.(2000)is seen only at very low pressures in the volumetric adsorption measurement.NomenclatureA0,A1,A2Virial parametersK Henry’s constant(mmol g−1atm−1)P Pressure(atm)q Molar adsorbed amount(mmol/g) AcknowledgmentsNeutron Activation Analysis(NAA)was conducted in the Ford nuclear Reactor of the Phoenix Memo-rial Laboratory at the University of Michigan.Leah Minc of the Michigan Memorial Pheonix Project coor-dinated the Analyses.This work was supported by NSF CTS-9819008.ReferencesBarrer,R.M.,Zeolites and Clay Minerals as Sorbents and Molecular Sieves,Academic Press,London,1978.Chao, C.C.,“Process for Separating Nitrogen from Mixtures Thereof with Less Polar Substances,”US Patent no.4,859,217, 1989.Chao,C.C.,J.D.Sherman,J.T.Mullhaupt,and C.M.Bolinger,“Mixed Ion-Exchanged Zeolites and Processes for the Use Thereof in Gas Separations,”US Patent no.5,174,979,1992.Chen,Y.D.,R.T.Yang,and P.Uawithya,“Diffusion of Oxygen,Ni-trogen and Their Mixtures in Carbon Molecular Sieve,”AIChE J. 40,557(1994).Choudary,N.V.,R.V.Jasra,and S.G.T.Bhat,“Process for the Prepa-ration of a Molecular Sieve Adsorbent for Selectively Adsorb-ing Oxygen from a Gaseous Mixture,”US Patent no.6,087,289, 2000.Coe,C.G.,J.F.Kirner,R.Pierantozzi,and T.R.White,“Nitrogen Adsorption with a Ca and/or Sr Exchanged Lithium X-Zeolite,”US Patent no.5,152,813,1992.Egoshi,N.,H.Kawakami,and K.Asano,“Mass Transfer in Ternary Distillation of Nitrogen-Argon-Oxygen System in Wetted-Wall Column,”J Chem.Eng.of Japan,32,409(1999).Egoshi,N.,H.Kawakami,and K.Asano,“Mass Transfer in Binary Distillation of Nitrogen-Oxygen and Argon-Oxygen Systems by Packed Column with Structured Packings,”J Chem.Eng.of Japan, 33,245(2000).Hunter,F.D.and J.Scherzer,“Cation Positions in Cerium X Zeoli-ties,”J.Catalysis,20,246(1971).Hutson,N.D.,S.U.Rege,and R.T.Yang,“Mixed Cation Zeolites: Li x Ag y-X as a Superior Adsorbent for Air Separations,”AIChE J.,45,724(1999).Hutson,N.D.and R.T.Yang,“Synthesis and Characterization of the Sorption Properties of Oxygen-Binding Cobalt Complexes Immo-bilized in Nanoporous Materials,”Ind.Eng.Chem.Res.,39,2252 (2000).Hutson,N.D.,S.C.Zijic,and R.T.Yang,“Influence of Residual Water on the Adsorption of Atmospheric Gases in Li-X Zeo-lite:Experiment and Simulation,”Ind.Eng.Chem.Res.,39,1775 (2000).Jones,R.D.,D.A.Summerville,and F.Basolo,“Synthetic Oxygen Carriers Related to Biological Systems,”Chem.Rev.,79,139 (1979).Juntgen,H.,K.Knoblauch,and K.Harder,Fuel,60,817(1981). Knaebel,K.S.and A.Kandybin,“Pressure Swing Adsorption System to Purify Oxygen,”US Patent no.5,226,933,1993.Li,G.Q.and ind,“Separation of Oxygen from Air Using Coordination Complexes:A Review,”Ind.Eng.Chem.Res.,33, 755(1994).McKee,D.W.“Separation of an Oxygen-Nitrogen Mixture,”US Patent no.3,140,933,1964.Miller,G.W.and C.F.Theise,“Secondary Oxygen Purifier for Molec-ular Sieve Concentrator,”US Patent no.4,813,979,1989. Niederhoffer,E.C.,J.H.Timmons,and A.E.Martell,“Thermody-namics of Oxygen Binding in Natural and Synthetic Dioxygen Complexes,”Chem.Rev.,84,137(1994).Ramprasad, D.,G.P.Pez, B.H.Toby,T.J.Markley,and R.M. Pearlstein,J.Am.Chem.Soc.,117,10694(1995).Rege,S.U.and R.T.Yang,“Limits of Air Separation by Adsorption with LiX Zeolite,”Ind.Eng.Chem.Res.,36,5358(1997).278Jayaraman et al.Reid,C.R.,I.P.O’koye,and K.M.Thomas,“Adsorption of Gases on Carbon Molecular Sieves Used for Air Separation.Spherical Adsorptives as Probes for Kinetic Selectivity,”Langmuir,14,2415 (1998).Sherry,H.S.,“The Ion-Exchange Properties of Zeolites.I.Univalent Ion Exchange in Synthetic Faujasite,”J.Phys.Chem.,70,1158 (1996).Sun,M.S.,D.B.Shah,H.H.Xu,and O.Talu,“Adsorption Equilibria of C1to C4Alkanes,CO2,and SF6on Silicalite,”J.Phys.Chem.B.,102,1466(1998).Yang,R.T.,Gas Separation by Adsorption Processes,Butterworth,Boston,1987;reprinted(in paperback)by Imperial College Press: London and World Scientific Publishing,River Edge,NJ,1997. Yang,R.T.,“Recent Advances and New Horizons in Gas Adsorption—with a Focus on New Sorbents,”in Preprints Top-ical Conference on Separation Science Technology,and W.S.W. Ho and R.G.Luo(Eds.),p.14,AIChE,New York,1997. Yang,R.T.and N.D.Hutson,“Superior Zeolite Sorbent for Air Separation,”US Patent pending.Yang R.T.and N.D.Hutson,“Lithium-Based Zeolites Containing Silver and Copper and Use Thereof for Selective Adsorption,”US Patent Pending,Serial Number60/114371,filed Dec.30,1998.。

科技文献的阅读及翻译方法4

科技文献的阅读及翻译方法4

2. Fundamentals in ChE
2.1 Chemistry (inorganic, organic)
Preliminary knowledge
Inorganic chemistry is a branch of chemistry concerned with the properties and reactions of inorganic compounds. Organic chemistry is the scientific study of the structure, properties, composition, and reactions of organic compounds Chemical reactions are known as chemical changes - changes in the structure of molecules-molecules attaching to each other to form larger molecules, molecules breaking apart to form two or more smaller molecules, or rearrangements of atoms within molecules. Chemical reactions usually involve the making or breaking of chemical bonds. Molecules: can be either polyatomic or monoatomic. Polyatomic molecules are electrically neutral clusters of two or more atoms joined by shared pairs of electrons (covalent bonds). A substance that is made up of molecules is called a molecular substance. Many familiar substances are made of molecules (e.g. table sugar, water, most gases) while many other equally familiar substances are not molecular in their structure (e.g. metals).

英语学习幼儿入门1315版

英语学习幼儿入门1315版

And management. 3, ex situ protection: species to move out of the place, human zoo, the aquarium and endangered animals breeding center for intensive care and management. To strengthen the education and management of the legal system, biological diversity of rational use of.Statement: 1, biological diversity value: direct use value: medicinal value, industrial raw materials, scientific value, aesthetic value. Indirect use value: biological diversity has important ecological functions. Third, the potential value: our use of a large number of wildlife value has not been found, not research, undeveloped part of the utilization. 2, China Biodiversity of overview of our biological diversity of characteristics: rich in species, endemic species and ancient species, species rich in economic, ecological system diversity. The biodiversity is threatened by: world and a decrease in species diversity; the species diversity and genetic diversity threatened; diverse ecosystems in our country is threatened. , biodiversity facing the threat of reason: change and destruction of the living environment, predatory exploitation and utilization, environmental pollution, rogue species invasion or introduction to the lack of natural enemies of the area of the original species survival is threatened. 3, biodiversity protection: in situ conservation: A, is mainly to create nature reserves; B, the protection object mainly: representative natural ecosystems and rare and endangered animals and plants of the natural distribution area; Jilin Changbai Mountain Nature Reserve: protecting the integrity of the temperate forest ecosystems. Bird island in Qinghai Lake Nature Reserve - protection bar headed goose, brown Headed Gull birds and their living environment. The ex situ conservation is a supplement to the in situ conservation, which provides the final opportunity for the survival of the extinct species. 4, our country has been extinct wild animals such as rhino, wild horse and Xinjiang tiger, etc.. There are a lot of animals have not been discovered or identified. 5, the giant panda, golden monkey, wild camels, silver fir, Davidia involucrata, life of wild animals are in endangered state the number of plants. 6, panda, dolphins, alligators, fir, Metasequoiaglyptostroboides is China's endemic species. 7, Liriodendron, leaf magnolia, alligator and so is China's oldest species.Second section, the harm of environmental pollutionNoun: 1 biological enrichment: refers to the some pollutants (such as heavy metals, chemical pesticides), through the food chain in the organisms in the accumulation of a large number of process. The general characteristics of these pollutants are chemically stable and not easy to decompose, accumulated in the body is not easy to discharge. Therefore, the biological enrichment will be strengthened with the extension of the food chain. 2, eutrophication due to nitrogen and phosphorus in water plant essential elements in too much lead to algae blooms. Algal respiration and the death of algae decomposition consume large amounts of oxygen, and decomposition of toxic substances, resulting in water at severe hypoxia, caused by the deterioration of water quality and fish death phenomenon. 3, bloom: in freshwater lakes occur rich nutrition phenomenon. 4, red tide: the phenomenon of eutrophication in the sea.Statement: 1, environmental pollution mainly include: air pollution, water pollution, soil pollution, solid waste pollution and noise pollution. 2, the harm of atmospheric pollution: Chinese air pollution is coal pollution, the main pollutants are soot, sulfur dioxide,. In addition, nitrogenoxides and carbon monoxide. The hazard: direct harm to human and other organisms, resulting in respiratory system diseases (such as bronchitis, asthma, emphysema, etc.. 3) there are 3 main carcinogens, 4 - benzo pyrene and Pb containing compounds. Especially in 3, 4, the strongest effect of BaP induced lung cancer. 4. Through the water, soil and plant and thus endanger human and animal 0.3, water pollution hazards: Minamata disease incident: Mercury in water transformed into methylmercury (MeHg), enriched in fish, shrimp body, if the long-term eating these foods will damage the central nervous system, movement disorders, spasm, paralysis, language and hearing occurred symptoms and even death. The agricultural water in water excess N, P mainly from fertilizers, city sewage and industrial wastewater. The formation of red tide and water bloom are the result of eutrophication. 4, the harm of soil pollution: "cadmium rice events: the soil is cadmium pollution, after biological enrichment into people, livestock, bone pain, natural fracture, bone defect, resulting in systemic nerve pain and disease, and ultimately death. Effects of plant growth and development on the prevention and control of environmental pollution in animals and people in third sectionsNoun: 1 biological purification: organisms through absorption and decomposition and conversion, ecological environment pollutant concentration decreased or disappeared.Statement: 1, the prevention and control of environmental pollution countermeasures: strengthen legal consciousness, in accordance with the law to protect the environment; enhance people's awareness of environmental protection; use of prevention and control of high-tech; the biological sciences application in environmental protection. 2, green plants and microorganisms play an important role in biological purification. 3, green plant purification function: absorb harmful gases: Cryptomeria fortunei monthly can absorb sulfur dioxide 60kg II adsorption dust: 1hm2 beech woods, within one year of the adsorption of dust is 68T. Thirdly, kill bacteria, some plants can secrete powerful antibiotics, such as sycamore, orange, juniper, and other plants, strong bactericidal. 4 microbial purification: purification effects of microorganisms in nature: A, is easy to be decomposed, feces; B. is difficult to decompose: cellulose and pesticides; C, does not decompose: plastic and nylon. Use of microbial purification of sewage. Survival. 5, noise pollution hazards: damage to hearing, interfere with sleep, induce a variety of diseases, affect the psychological health.The new high school curriculum planBiologySenior high school threeTomorrow pressJuly 2012The new high school curriculum plan in the third grade high school #! "Yin Yin Yin Yin YinYin YinYin Yin Yin Yin YinYin YinYinYinYinYinRequired 1Molecular and cell first chapters approach cellFirst case studyThis sort of knowledge1 (1) living cell (2) single cell (protoplast) various differentiation2 cells, tissues, organs, systems, individuals, populations, communities and ecosystems. The individual, population, community and ecosystem of the ECSystem and biosphere3. Comparison of eukaryotic and prokaryotic cellsprojectSizeessenceCell wall cellqualityCellskernelDNA depositIn formproliferationmodeCan inheritmodedifferencequalityUnifiedqualityprokaryotic cellNon nuclearMembrane boundedLimit of finekaryonThere are, the main ingredients Sugar and eggswhite matterThere is aBody, noOther finecell organQuasi kernel,No nuclear envelope And the kernelQuasi core: Large Ring, exposed Plasmid: smallRing, exposed dichotomycrackgenemutationeukaryotic cellWith nuclear Membrane bounded Limit of finekaryonPlant cells have,The main components are Cellulose and fruitAnimal cells; adhesiveNo cell wall; trueThe germ cell has, the LordTo the composition of a number of sugarThere is aBody and itsHis cellorganA nuclear envelopeAnd the kernelNuclear: andProtein formation Chromosome; cellQuality: Online grainBody and chloroplastBare existenceNon silkCrack, haveWire pointsCrack, reductionNumber splittingGene mutationVariable, baseBecause of the heavyGroup and dyeingColor changedifferentProkaryotic fineCell and truthkaryocyteCompared with noNuclear membranechromosomeisostructuralAll haveCellsThin filmCytoplasm andDNA molecule4 cell Schleiden and Schwann cell theory cells byNew cell division5 cell and cell products are relatively independent of the old cell To enhance the ability.Cases of DSelf evaluation.1 B3. D2. C4. D5. C6. D7. D8 (1) C non cellular host (Live) cells (2) A, BNo nuclear B cyanobacterial cells surrounded by a membrane by blue algae Pigment and chlorophyll (3) autotrophic D genetic material mainly exists Nucleus of, E, F, and D on chromosome9 (1) of chloroplast, vacuole centrosome(2) C, D fine?。

杂原子掺杂碳材料用于氧还原反应催化剂的研究

杂原子掺杂碳材料用于氧还原反应催化剂的研究

文章编号:1001-9731(2021)02-02098-11杂原子掺杂碳材料用于氧还原反应催化剂的研究*魏家崴,李平,强富强,王焕磊(中国海洋大学材料科学与工程学院,山东青岛266100)摘要:氧还原反应存在于多种储能设备如空气电池和燃料电池的反应过程中,通常以商业铂碳作为催化剂,但铂基催化剂的高昂价格和易中毒的缺点限制了其广泛应用㊂碳基材料被认为是贵金属催化剂最有希望的替代物,引起了众多研究者的兴趣㊂这是因为某些杂原子掺杂于碳基体中会因为其与碳原子的物理化学性质的差异而在基体中形成缺陷,形成催化的活性位点,亦可提高材料的电导率和氧传输能力,从而提高了碳材料的氧还原反应催化能力㊂为此,本文首先介绍了氧还原反应的过程,然后介绍了多种杂原子掺杂的碳基氧还原催化剂的制备以及它们的优点和创新性㊂关键词:氧还原反应;无金属;掺杂碳材料;缺陷;催化能力中图分类号: T B34文献标识码:A D O I:10.3969/j.i s s n.1001-9731.2021.02.0120引言煤㊁石油㊁天然气等化石燃料的开采与消耗引起了能源枯竭和环境污染等问题,迫使我们需要发展效率高㊁环境友好的新型能源技术㊂燃料电池[1]和空气电池[2]是拥有高比容量和高能量密度的环保型便携器件,拥有很高的研究价值和广阔的应用市场㊂然而,阴极动力学缓慢的氧还原反应(O R R)极大地限制了电池的总反应速度,也因此影响了电池性能的进一步提升,所以提高电池效率的一个方法是改善阴极的氧还原反应,即在阴极材料中添加氧还原反应催化剂[3-5]㊂目前市面上的氧还原反应催化剂为P t/C贵金属[6],催化能力高但也面临着许多问题,比如储量稀少带来的高价格以及循环稳定性差和耐甲醇等燃料的毒副作用能力不佳等[7-9]㊂碳基材料催化剂被认为是最有希望的贵金属替代物,碳基材料不仅拥有低廉的成本,也有优异的导电能力㊁良好的化学稳定性和较大的比表面积等,易于氧还原反应中氧的吸脱附和电子的传输[10-11]㊂对碳材料进一步掺杂以提高碳材料的催化能力㊁稳定性等是近年来研究的热点[12]㊂如图1所示,杂原子掺杂无金属碳材料用于O R R反应催化剂的研究逐年增加,因此本文简要讨论了氧还原反应的机理并总结了用于氧还原反应催化剂的杂原子掺杂碳材料,给出了用于掺杂的杂原子的类型以及掺杂提高催化性能的可能原因,最后,展望了碳基氧还原催化剂的发展方向㊂图1近几年关于无金属杂原子掺杂碳材料O R R催化剂发表论文数量F i g1T h en u m b e ro f p a p e r s r e l a t e dw i t h m e t a l-f r e eh e t e r o a t o m-d o p e dc a r b o n m a t e r i a l sf o r O R Rc a t a l y s t s p u b l i s h ed i n re c e n t y e a r s1氧还原反应相关理论氧还原反应一般发生于固㊁液㊁气三相界面上,可分为分为4e-转移和2e-转移㊂2e-转移会产生大量的过氧化物,过氧化物的强氧化作用会破坏电池的隔膜而降低电池的寿命,所以对于电池反应的氧还原过程而言,4e-转移是理想的还原过程㊂1.1氧还原反应过程1.1.1在碱性条件下的4e-转移直接4e-转移,氧与水㊁电子生成氢氧根的过程:O2+2H2O+4e-ң4O H-,E0=0.401V或分两步进行:O2+H2O+2e-ңHO-2+O H-,E0=0.065VHO-2+H2O+2e-ң3O H-,E0=0.867V 1.1.2在碱性条件下的2e-转移第一步与4e-转移两步方式的第一步相同:890202021年第2期(52)卷*基金项目:山东省重点研发计划(公益类科技攻关)资助项目(2019G G X102038);中央高校基本科研业务费专项资助项目(201822008,201941010);青岛市应用基础研究计划资助项目(19-6-2-77-c g)收到初稿日期:2020-08-01收到修改稿日期:2020-12-23通讯作者:王焕磊,h u a n l e i w a n g@o u c.e d u.c n作者简介:魏家崴(1997 ),男,济南人,硕士,师承王焕磊教授,从事碳基催化剂材料研究㊂O2+H2O+2e-ңHO-2+O H-,E0=0.065V第二步为分解反应,不再获取电子:2HO-2ң2O H-+O21.1.3在酸性条件下的4e-转移直接4e-转移,氧与质子㊁电子生成水的过程:O2+4H++4e-ң2H2O,E0=1.229V或分两步进行,生成中间产物过氧化氢:O2+2H++2e-ң2H2O2,E0=0.670VH2O2+2H++2e-ң2H2O,E0=1.277V 1.1.4在酸性条件下的2e-转移第一步与4e-转移两步方式的第一步相同:O2+2H++2e-ң2H2O2,E0=0.670V第二步为分解反应,不再获取电子:2H2O2ң2H2O+O21.2氧吸附模型对于氧还原过程还存在许多争议,为多数研究者所接纳的一种理论为氧在催化剂表面的还原方式与它的吸附方式有关,氧在催化剂表面的吸附模型分为三种,侧基式㊁桥基式和端基式[13]㊂侧基式是氧分子中心的σ键与催化剂相作用,这种吸附方式可以使O O键减弱,有利于使氧分子进行直接4e-转移过程;桥基式是氧的两个原子同时吸附在催化剂的表面,可以使两个氧原子同时得到活化,从而也有利于4e-转移过程;而端基式吸附则不同,端基式为氧分子中的一个与催化剂接触,从而只有一个氧原子得到活化,一般这种吸附方式为2e-转移过程㊂在实际的氧还原过程中存在的反应十分复杂,在还原过程中可能存在着多个反应同时进行的现象,而且对于不同的催化剂也会存在不同的反应过程,甚至对于同种催化剂,在不同的酸碱溶液中也拥有不同的催化能力,分别进行4e-转移和2e-转移过程㊂杂原子进入碳基体之后,会因为自身和碳基体之间的性质差异如电负性㊁原子半径等而引起碳基体的性质发生改变,如提高碳材料的电导率,改善材料对氧的吸附及还原产物的脱附能力等,而对于某些杂原子如氮原子,掺杂后形成的吡啶N和石墨N公认对氧还原反应有催化活性,可以提高碳材料的催化性能㊂对于锌空气电池和燃料电池而言,需要的是4e-转移的氧还原反应,合理的杂原子掺杂可以促进氧以桥基式和端基式的形态吸附,将O2还原为O H-,提高4e-转移的比例,提高电池的效率,同时减少了2e-转移中间产物HO-2的比例,避免了HO-2的强氧化性对电池的损害㊂2杂原子掺杂碳材料碳材料本身在碱性条件下就拥有一定的氧还原催化能力,这可能与碳材料的边缘缺陷有关[14-15],但是它只在碱性条件下有活性且催化能力有限,杂原子掺杂碳材料就是将N㊁P㊁S㊁B等元素掺杂进碳材料从而进一步提高碳材料的催化能力㊁极限电流密度㊁循环稳定性㊁耐毒副能力等㊂可作为碳载体的材料有石墨烯[16]㊁碳纳米管[17]㊁MO F材料[18]和一些生物质材料[19-20]及其衍生物[21]等㊂关于杂原子掺杂提高催化性能的理论还存有争议,但让大多数学者所接受的观点是催化能力的提高与杂原子和碳基体间的化学性质差异有关,杂原子和碳原子之间存在电负性㊁原子尺寸㊁键长键角等方面的差异,将其掺杂入碳原子后会引起周围原子电子密度和自旋等方面性质的改变,且会在碳基体中形成更多的缺陷[22],这可能是催化的活性位点㊂2.1 N单原子掺杂碳材料值得注意的是,N原子是在氧还原催化剂的制备中最常用的,也是最有效果的杂原子,这可能与N原子独特的电负性和原子半径等因素有关,N掺杂进入碳基体以后形成的吡啶N和石墨N常常被认为是氧还原反应的活性位点[23-24],所以大多数用于氧还原反应催化剂的碳材料都会选择N原子掺杂或者N与其他原子的共掺杂㊂N掺杂碳材料可以通过多种方式制备,比如通过将含氮的碳前体或者均匀混合的氮源和碳源热解,或者以化学气相沉积(C V D)的方法将氮原子整合进碳体系中,制备过程中常用双氰胺[23]㊁尿素[25]㊁三聚氰胺[26]㊁氨气铵盐[27-28]㊁丙烯腈[29]等作为额外的N源㊂戴黎明[30]等人首先报道了利用高温下热解酞菁铁的方法制备了垂直排列的氮掺杂碳纳米管(V A-N C-N T),用于碱性条件下的氧还原催化剂,并通过电化学氧化的方法去除了催化剂中的铁原子㊂通过与不掺杂N的碳纳米管(N A-C C N T)和P t/C催化剂的对照结果表明,V A-N C N T的催化能力与P t/C接近且远远超过了N A-C C N T,且V A-N C N T的扩散受限电流密度超过了P t/C,这表明了N掺杂确实可以提高碳材料的催化性能且拥有比P t/C催化剂更优良的性能㊂值得一提的是,V A-N C N T和P t/C都是4e-转移而N A-C C N T是2e-转移,由此提出了氧在催化剂表面的吸附模型(如图2所示):碳基体中的吡啶型N原子拥有较高的电负性,会使相邻碳原子拥有更多正电荷,使氧在催化剂表面的吸附由端吸附变为侧吸附,从而使两个氧原子都得到活化而进行4e-转移过程㊂戴黎明[31]等人进一步用C V D的方法将含氮反应气体混合物(N H3:C H4:H2:A r)沉积到镍薄膜上,再用盐酸蚀刻镍得到了氮掺杂石墨烯薄膜㊂X P S显示,N-石墨烯相较于石墨烯拥有更强的O1s峰,表明N-石墨烯有对氧更强的吸附能力㊂研究表明N-石墨烯表现出与V A-N C N T相同的一步4e-转移途径,极限电流密度是P t/C的3倍;耐交叉和毒性好,计时电流曲线显示加入氢气㊁葡萄糖甲醇和C O后电流密度基本不变,而P t/C电极电流下降明显;循环稳定性好,在200000次循环后没有明显的电流下降㊂99020魏家崴等:杂原子掺杂碳材料用于氧还原反应催化剂的研究图2 V A-N C N T上氧的吸附模型[30]F i g2A d s o r p t i o nm o d e l o f o x y g e no nV A-N C N T[30] N掺杂碳材料的催化性能引起了人们的关注,众多科研工作者通过不同途径制备N掺杂碳催化剂并对其进行研究㊂Z h e nH u a nS h e n g[32]通过将氧化石墨烯(G O)与三聚氰胺研磨混合并在氩气气氛下碳化的方法制备了氮掺杂石墨烯(N G s)(图3(a))㊂电化学表征显示,N G s在碱性条件下拥有良好的氧还原催化活性,与垂直排列的氮掺杂碳纳米管类似㊂通过控制三聚氰胺用量和碳化温度的方法实现了N G s中N元素含量的调节,在G O与三聚氰胺质量比为0.2㊁碳化温度为700ħ时N原子掺杂量可达10.1%(原子分数)㊂但是N G s的催化活性不受N元素含量的影响,主要可能与吡啶N的含量有关,表明提高吡啶N的含量可以进一步提高催化性能㊂W e n Y a n g[33]等以纳米S i O2为模板,通过将核酸碱基溶解在有机离子液体(E m i m-d c a)中形成的凝胶碳化,制备了表面积高达1500m2/g的介孔氮掺杂碳材料,材料中的氮含量达12%(质量分数),拥有接近P t/C催化剂的活性㊂D a-g u oG u[23]等以柠檬酸和双氰胺分别作为碳源和氮源,双氰胺缩合得到的中间体g-C3N4起到了作为热分解模板和原位氮源的作用,在1000ħ下碳化制备了N 掺杂类石墨烯层状碳纳米片N C,如图3(b)所示㊂与市售P t/C催化剂相比,双氰胺/柠檬酸质量比为6时制备的N C片的半波电位(E1/2)相差66~68m V,具有较好的长期稳定性和良好的抗甲醇交叉性能㊂J i n g L i u[25]将廉价炭黑B P与尿素研磨混合并在A r气氛下于950ħ下热解1.5h得到了氮掺杂样品B P N㊂通过实验和量子化学计算的方法揭示了不同含N位对氧还原的催化活性顺序为吡啶N>吡咯N>石墨N>氧化N>C;D h e e r a j K u m a r S i n g h[34]将管状埃洛石粘土和盐酸多巴胺溶于T R I Sb u f f e缓冲液中,生成了聚多巴胺涂层的纳米粘土,将其在800ħ下于A r气氛下热解,得到了N掺杂碳,简称为N D C-800,如图3(c);Y i W a n g[35]以间苯二酚㊁甲醛和碳酸铵聚合并热解的方法制备了大比表面积的N掺杂分级多孔碳(L N-H P C),制备示意图如图3(d),并且通过L N H P C和氨水于180ħ下水热处理增加了材料中的N掺杂含量从而提高了材料的催化性能㊂H e n g c o n g T a o[36]报道了一种制备N掺碳的无碳化方法,即在5ħ的低温下将氧化石墨烯在氨水溶液中超声处理以实现氮的掺杂,控制超声时间和浴温实现了N掺杂水平的有效调节㊂图3(a)三聚氰胺在G O层中掺氮过程[32];(b)N掺杂类石墨烯层状碳纳米片的制备[23];(c)管状N掺杂碳材料的制备[34];(d)大比表面积的N掺杂分级多孔碳制备示意图[35]F i g3(a)T h e p r o c e s s o f n i t r o g e n d o p i n g i nG O l a y e r b y u s i n g m e l a m i n e[32];(b)p r e p a r a t i o n p r o c e s s o fN-d o p e dg r a p h e n e l i k e c a r b o nn a n o s h e e t s[23];(c)p r e p a r a t i o n p r o c e s s o f t u b u l a rN-d o p e d c a r b o nm a t e r i a l s[34];(d)p r e p a r a t i o no fN-d o p e dh i e r a r c h i c a l p o r o u s c a r b o nw i t h l a r g e s p e c i f i c s u r f a c e a r e a[35]2.2双原子掺杂碳材料2.2.1 N,P共掺杂碳材料磷是氮族的一种元素,具有与氮相似的化学性质,由此人们探索了P掺杂对碳材料氧还原性能的影响㊂可以作为P源的物质有三苯基膦[37](T P P)㊁植酸[38]㊁磷酸[39]和六氯环三磷腈[40]等㊂N㊁P的共掺杂可以增加碳材料中缺陷的密度,减少氧还原反应中过氧化物的产生,提高在酸性溶液下的催化性能,氧还原活性的提高可能是由于自旋密度或电子转移的不对称性增强所致㊂N㊁P共掺杂和石墨烯边缘效应是催化活性的关键,J i n t a oZ h a n g[38]通过用三聚氰胺㊁植酸(P A)和氧化001202021年第2期(52)卷石墨烯(G O )的协同组装并热解的方法将N 和P 整合进了石墨烯基体中(如图4(a )所示)㊂所制备的电极电子转移数为3.7,展现出与P t /C 相当的性能㊂将制备的三维多孔N ,P -共掺杂石墨碳网络作为空气阴极组装了锌空电池,其峰值功率密度为310W /g,在90h 内无电位下降,具有优异的耐用性㊂J i n t a oZ h a n g [41]等人随后又将苯胺在植酸水溶液中聚合形成凝胶,在1000ħ下热解制备了N ㊁P 共掺杂介孔泡沫碳(N P M C ,如图4(b )),N P M C -1000的比表面积(1663m 2/g)与N P M C -900相比增加了一倍以上,这很可能是由于聚苯胺气凝胶碳化产生挥发性物质,形成了一个分级多孔结构㊂N P M C -1000对氧还原有良好的电催化性能,L S V 图显示起始电势(E o n s e t )为0.94V ,E 1/2为0.85V ,如图4(c )所示㊂以此制备的一次性电池的开路电位为1.48V ,比容量为735m A h /g ,双电极充电电池在2m A /c m 2下可稳定循环180次,组装的锌空电池示意图如图4(d )所示㊂文中提到热解温度十分重要,高的热解温度可以得到高的石墨化程度,较高的导电性和较大的比表面积,因此具有更好的电催化活性(N P M C -1000优于N P M C -900)㊂但是温度过高(比如1100ħ)可能导致掺杂剂分解从而使性能下降㊂图4 (a )M P S A /G O -1000协同组装热解制备工艺[38];(b )N P M C 泡沫制备工艺示意图[41];(c)不同温度下碳化的碳材料的L S V 曲线[41];(d)组装的锌空电池示意图[41]F i g 4(a )T h e c o l l a b o r a t i v e a s s e m b l yp y r o l y s i s p r o c e s so fM P S A /G O -1000[38];(b )i l l u s t r a t i o no f p r e pa r a t i o n p r o c e s s o fN P M Cf o a m [41];(c )L S Vc u r v e s o fN P M Cc a rb o n i z e d a t d i f f e r e n t t e m pe r a t u r e s [41];(d )s c h e -m a t i c d i a g r a mo f a s s e m b l e d z i n c -a i r b a t t e r y[41]N ㊁P 共掺杂碳材料的优秀催化能力引起了众多科研工作者的关注㊂R o n g L i [42]以热解氧化石墨烯㊁聚苯胺(P A N i)和植酸组成的聚合物凝胶的方式制备了具有分层多孔三明治状结构N ,P -G C N S 纳米片,如图5(a )所示㊂多元素掺杂纳米碳由于协同作用导致反应物的活性中心增多,可以表现出比单元素掺杂纳米碳更好的催化活性㊂大的活性比表面积和有序的孔结构可以保证反应物分子的可接近性和快速的传质过程,集成的石墨烯纳米片可以促进氧化还原过程中的电荷转移㊂J i a n b i n g Zh u [43]等以三聚氰胺-二苯基膦酸配合物晶体(M D P C C )为原料,在高温下热解合成了N ,P 共掺杂催化剂(N P C -X -T ,X 为N /P 比,T 为碳化温度,如图5(b )),并且通过Z n C l 2活化形成了多孔结构(命名为N P C -X -T -Z n ,图5(c)),提高了催化剂的比表面积以提高催化剂的催化性能㊂Z h e n g p i n g Z h a n g [45]通过吡咯和植酸之间的聚合反应㊁以聚苯乙烯球为模板并采用直接热解法制备了N ,P -共掺杂介孔炭(N ,P -M C )㊂N ,P -M C 具有优异的氧还原活性,显著的电化学稳定性和优异的甲醇耐受性,与工业P t /C 催化剂相当甚至更好,这与N ,P -M C 具有介孔结构和大量的N ㊁P 共掺杂形成的活性位点有关㊂M a r ya m B o r gh e i [44]用椰子壳粉于磷酸中浸渍碳化㊁尿素溶液中浸渍碳化实现N 和P 的掺杂,制备示意图如图5(d),生物衍生的电活性炭与P t /C 催化剂标准材料相比,表现出了可媲美的电催化活性,对甲醇交叉效应的耐受性,以及在碱性介质中进行氧还原反应的长期耐久性㊂L i a n w e nZ h u [46]通过将爆米花放置在管式炉的中心部分,并将管式炉一10120魏家崴等:杂原子掺杂碳材料用于氧还原反应催化剂的研究图5(a)N,P-G C N S催化剂的制备工艺和结构示意图[42];(b)N P C-X-T电催化剂的合成示意图[43];(c)N P C-4-1100-Z n的S E M图像[43];(d)由椰子壳合成N,P掺杂多孔碳的原理图[44]F i g5(a)T h e p r e p a r a t i o n p r o c e s s a n d s t r u c t u r e i l l u s-t r a t i o no f N,P-G C N Se l e c t r o c a t a l y s t[42];(b)s c h e m a t i c i l l u s t r a t i o no f t h es y n t h e s i so fN P C-X-Te l e c t r o c a t a l y s t[43];(c)S E Mi m a g eo fN P C-4-1100-Z n[43];(d)T h es y n t h e s i so f N,P-c o-d o pe d p o r o u s c a r b o nf r o mc o c o n u t s h e l l[44]端的针阀关闭,另一端的针阀保持打开状态下直接热解制备N,P共掺杂碳,在碱性电解液中的锌空气电池具有1.44V的开路电压和36.6mW/c m2的峰值功率密度和良好的稳定性,这是由于爆米花中蛋白质与磷酸盐中的含氮和含磷基团与石墨基质缩合形成N-C 和P-C键,而热解副产物(如H2O和C O2)可以刻蚀无序的碳结构区域,形成层次孔隙和边缘碳㊂2.2.2 N,S共掺杂碳材料S比P多一个电子,硫因其取代碳原子的能力和与氮掺杂剂的强协同效应而备受关注,硫原子引起的结构缺陷有利于电荷位错和氧的吸附,另一方面,硫原子的两个孤对电子也有助于掺杂碳与分子氧的相互作用㊂通常用于硫源的物质有硫粉[47]㊁硫脲[48]㊁二苯硫醚[49]和其他含硫物质[50-51]㊂合理设计的形貌和多孔结构有利于获得更高的氧还原性能,有望提供更好的电解液渗透性和更快的电子传输和质量传输㊂X i a o b a oL i[47]以聚丙烯腈和硫为前驱体㊁改性S i O2纳米球为模板,采用热解法制备了氮硫掺杂的空心炭碗(C B-3S),制备方法如图6(a)所示,这是因为去除二氧化硅模板时形成的碳壳破裂而产生碳碗,碳碗的S E M图如图6(b)㊂C B-3S具有较高的氧还原反应性能,其E1/2与P t/C催化剂在碱性介质中的E1/2相当;C B-3S还表现出卓越的耐甲醇性和稳定性,以及对四电子路径的高选择性㊂结合表征结果,认为C B-3S图6(a)N,S掺杂中空碳碗制备方案示意图[47];(b)中空碳碗的S E M图像[47];(c)C P N-N S催化剂的制备示意图[52];(d)C P N-N S和C P N-N中不同种类的N含量[52]F i g6(a)S c h e m a t i c i l l u s t r a t i o no f t h e s y n t h e s i s o fN,Sd o p e dh o l l o wc a r b o nb o w l[47];(b)S E Mi m a g eo f h o l-l o wc a r b o nb o w l[47];(c)s c h e m a t i c i l l u s t r a t i o no f t h e p r e p a r a t i o no f C P N-N S c a t a l y s t[52];(d)t h e c o n t e n t o f d i f f e r e n tN-m o i e t i e s i nC P N-N Sa n dC P N-N[52]201202021年第2期(52)卷性能优异的主要原因有:(1)活性组分含量高,包括石墨/吡啶N组分和-C-S-C-型S,它们被认为可以改变表面电荷分布并产生缺陷和活性位点;(2)高比表面积(1146m2/g),可以提供更多暴露的活性位点;(3)碗状形貌,使碳壳的内表面更容易接触电解质和氧气㊂C h e n g h a n g Y o u[52]以S B A-15为模板㊁通过萘的福瑞德-克拉夫兹反应形成碳基体,再通过其与硫粉研磨并在N H3中热解以实现N㊁S的掺杂,如图6c,催化剂命名为C P N-N S㊂S的引入使催化剂的微孔体积增大,说明S的加入有利于微孔的形成,这应归因于S的掺杂和碳晶格的分解,而且S的加入有助于维持N的含量和调节N的组成,从图6d来看,C P N-N S与C P N-N相比形成了更多含量的吡啶N和石墨N,这有利于提高反应的活性㊂C P N-N S具有较高的氧还原性能,其半波电位(E1/2)为0.868V,比商用P t/C催化剂(E1/2=0.838V)更高㊂M i n g b o W u[53]通过三聚氰胺和三硫氰酸(简称MT)聚合在石油焦(P C)衍生石墨烯纳米片上原位形成的超分子聚合物,不仅可以作为掺杂杂原子的来源,而且可以防止石墨烯纳米片的聚集,从而形成多孔结构的N,S双掺杂碳材料N,S-P G N㊂N,S-P G N具有较高的比表面积和较大的孔体积,这是因为MT聚合物阻止了石墨烯结构的坍塌,使超薄石墨烯层形成了介孔网络,并且MT分解原位释放的气体可以产生更多的孔隙和随机的边缘位置㊂高比表面积㊁大体积和丰富的拓扑缺陷可以促进电解液的进入和反应物的扩散,也可以为氧还原提供额外的活性位点㊂大多数掺杂杂原子通常来自碳源之外的掺杂剂,这给控制催化剂结构和组成的均匀性带来了困难㊂在这方面,含有杂原子的有机材料是制备掺杂碳材料的较佳来源㊂J i n h u iT o n g[54]以甲基橙(F e(I I I))配合物为原料,经高温裂解,除去酸中的金属元素,制备了氮硫双自掺杂的介孔和微孔石墨碳催化剂㊂该催化剂在酸性和碱性介质中均表现出较高的电催化活性㊁长期稳定性和对甲醇的耐受性㊂炭化过程中F e物种的存在有助于增加催化活性N-C位点,如吡啶N和吡咯N 物种,从而更有效地促进氧还原活性㊂铁还可以增加制备的碳的石墨相,从而改善碳骨架的导电性㊂热解温度和酸处理对控制材料的比表面积和催化活性具有重要作用,酸腐蚀不稳定的铁物种,可大大提高催化剂的催化性能㊁耐甲醇性和长期稳定性㊂角蛋白[55]的主要半胱氨酸骨架成分,不仅含有丰富的S和N原子,而且呈现出由大量扁平重叠的鳞片构成的平行螺旋结构,在碳化过程中,由于扁平重叠单元之间的弱相互作用,这种层状结构可以保留下来,形成片状碳㊂J i a w e i Z h u[56]以角蛋白为碳㊁氮㊁硫元素的前驱体,通过碱活化和氨活化巧妙地产生了固有缺陷,设计和制备了一种富缺陷的N/S双掺杂类干酪状多孔碳纳米材料C F-K-A㊂高含量的活性N和S掺杂,在碳基体中含有丰富的本征缺陷,可以有效地提高周围碳原子的电荷密度,减小HOMO-L UMO能隙,从而加速间隙间的电子转移和氧还原反应中间产物的形成,改变其对吸附质的化学反应性,电化学测试表明,该材料具有与工业P t/C催化剂相当的氧还原活性(E1/2=0.835V),并具有优异的耐用性和耐碱性㊂2.2.3 N,B共掺杂碳材料B(x=2.04)的电负性低于C(x=2.55),而N(x= 3.04)的电负性高于C,B㊁N共掺杂产生附加的电子受体和电子给体态,可以通过掺杂体与周围碳原子之间的协同电子转移相互作用来调节能带隙和电荷密度,从而为氧还原提供了潜在的更活跃的位点㊂在N掺杂的碳物种中,氧还原反应增强是由于氮从碳的最高占据分子轨道(HOMO)吸引电子,在具有高自旋密度的相邻碳上诱导部分正电荷并随后降低了O2的吸附能,硼离子可以增强氧的化学吸附,这是由于π-共轭碳体系中空位2p z硼轨道上的电子积聚,从而促进电子转移到吸附的氧并削弱O-O键㊂N和B共掺碳催化剂的性能似乎取决于合成方法㊁掺杂程度以及催化剂中B和N官能团的分布,由于B和N对邻近的碳产生相反的电子效应,来自N的额外电子和B的空位轨道之间发生中和效应,从而不利于O2的化学吸附和随后的还原㊂通常以硼酸[57]或硼酸的衍生物[58-59]作为掺杂B的来源㊂H a s s i n aT a b a s s u m[60]通过硼酸㊁尿素和聚乙二醇(P E G)在水溶液中混合,然后在900ħ下于A r气氛中热解制备了B C N,并且指出P E G的分子量对产物的形貌有着深刻的影响㊂高分子量的P E G(例如P E G-8000)衍生的产物是具有B-N键的2DB C N皱褶纳米片,而低分子量的P E G产物中可以观察到具有B-C和N-C键的理想的一维管状结构,如图7(a)所示,管状结构的碳框架中存在的B-C和N-C键可以通过提高电子自旋密度,产生比B-N键更合适的电子态,从而具有良好的氧还原性能,所制备的N㊁B掺杂管状碳材料对氢电极的E1/2为0.82V,可与P t/C(0.84V)相媲美,B C N纳米管的S E M图像如图7(b)所示㊂R u o p e n g Z h a o[61]提出了一种利用N a C l辅助热解法制备高B,N掺杂量超薄碳纳米片结构(B N/C)的方法,制备过程见图7(c)㊂N a C l晶体在801ħ开始熔化,作为模板来支撑和分散前驱体;H3B O3和C2H10 N6在分解过程中通过层间空隙产生C O㊁C O2和N H3等气体来造孔㊂所制备的B N/C催化剂活性高于氮或者硼单掺杂的碳材料,在碱性介质中E1/2=0.8V,与工业P t/C催化剂相当,具有较好的长期稳定性和较好的甲醇交叉耐受性,B N/C催化剂的L S V曲线和稳定性测试图如图7d㊁e㊂这种优异的性能是由于B N/C 的结构和组成特点,包括大的比表面积(1085m2/g)㊁层次多孔结构㊁B,N共掺杂的协同效应和高含量的氧还原活性物㊂30120魏家崴等:杂原子掺杂碳材料用于氧还原反应催化剂的研究L iQ i n[62]以氮掺杂的多孔石墨烯(N-P G)为基体,使用硝酸氧化石墨烯并采用硼酸直接退火法合成了B,N-P G-O-15催化剂㊂B,N-P G-O-15的E o n s e t和E1/2分别为0.99V和0.86V,具有高的电子转移数(n= 3.84~3.95)和低的H2O2产率(H2O2%<9),与工业P t/C(n=3.87~3.92,H2O2%<7)相当接近㊂B,N-P G-O-15具有优异的耐久性,10000s后电流衰减缓慢,约为5.4%,而商用P t/C的损耗为19.6%㊂加入甲醇后,P t/C催化剂的电流密度明显降低,而B,N-P G-O-15催化剂的电流密度几乎不变㊂M i n g l iZ h a n g[63]以近似的方法,将N/G O在55ħ超声条件下分散在硼酸水溶液中,所得N B/G O复合材料在700ħ的N2气氛中退火1h,得到了N B/G O-55-700催化剂㊂N B/ G O样品显示出较好的氧还原电催化活性,氧还原的催化活性的提高被认为是由于在团簇型量子的基础上降低了HOMO-L UMO㊂较小的HOMO-L UMO间隙意味着向高水平L UMO中添加电子或从低水平HOMO中移除电子更容易,有利于氧还原的进行㊂图7(a)不同分子量的聚乙二醇与形成的不同形态B C N示意图[60];(b)B C N纳米管的S E M图像[60];(c)B N/C 纳米片的合成示意图[61];(d)B N/C催化剂的L S V曲线[61];(e)B N/C催化剂稳定性测试图[61]F i g7(a)D i f f e r e n t f o r m s o f B C Nu n d e r p o l y e t h y l e n e g l y c o lw i t hd i f f e r e n tm o l e c u l a rw e i g h t[60];(b)S E Mi m a-g e s o fB C N n a n o t u b e s[60];(c)p r e p a r a t i o no fB N/Cn a n o s h e e t s[61];(d)L S Vc u r v eo fB N/Cn a n o s h e-e t s[61];(e)s t a b i l i t y t e s t d i a g r a mof B N/Cn a n o s h e e t s[61]T a oS u n[64]以乙基纤维素和高沸点4-(1-萘基)苯硼酸为原料,采用廉价的锌基模板剂,在N H3气氛中热解制备了B,N-碳催化剂,这种碳材料具有丰富的碳缺陷㊂典型的多级孔分布有利于反应物在电催化反应过程中的扩散,也有利于生成更多暴露于电解液中的活性位点㊂在碱性介质中,B,N-碳材料表现出较高的氧还原活性,E o n s e t达到0.98V,E1/2为0.84V,与P t/C 仅相差17m V㊂5000次循环后B,N-碳的E o n s e t降低了大约10m V,表明具有良好的氧还原稳定性㊂2.33种及以上杂原子共掺杂碳材料杂原子掺杂的碳材料在氧还原催化剂领域优异的性能引起了众多科研工作者的关注,因此人们纷纷探索其他的杂原子掺杂对碳材料氧还原性能的影响,这其中除了前文中提到的N㊁P㊁S㊁B原子外,还有F[65]和C l[66]等,多杂原子掺杂碳材料[67-68]开始被众多研究者所探索,学者们选用不同的元素组合掺杂于碳材料中以进一步探索碳掺杂材料的氧还原过程㊂L e iW a n g[65]以聚丙烯腈(P A N)和四氟硼酸铵为401202021年第2期(52)卷。

GBT 3634.2-2011 氢气 第2部分:纯氢、高纯氢和超纯氢 中英 bilingual

GBT 3634.2-2011 氢气 第2部分:纯氢、高纯氢和超纯氢 中英 bilingual

氢气Hydrogen第2部分:纯氢、高纯氢和超纯氢Part 2: Pure hydrogen, high pure hydrogen and ultrapure hydrogen1.范围Scope本部分规定了纯氢、高纯氢和超纯氢的技术要求、试验方法、包装标志、贮运及安全要求。

This section provides the technical requirements, test methods, packing marks and store safety requirements of pure hydrogen, high purity hydrogen and ultra-pure hydrogen.本部分适用于经吸附法、扩散法等制取的瓶装、集装格装和管道输送的氢气。

它主要用于电子工业、石油化工、金属冶炼和科学研究等领域。

This section applies to the bottled, container loaded and pipeline transferred hydrogen making with adsorption and diffusion method. It is mainly used in electronic industry, petrochemical industry, metal smelting and scientific research, etc.分子式:Molecular formula: H2.相对分子质量:2.01588(按2007年国际相对原子质量)。

Molecular weight: 2.01588 (as per 2007 international relative atomic mass)2.规范性引用文件The reference file下列文件对于本文件的应用是必不可少的。

凡是注日期的引用文件,仅注日期的版本适用于本文件。

氮气物理吸附英文

氮气物理吸附英文

氮气物理吸附英文Nitrogen Gas Physical AdsorptionNitrogen gas, with its chemical formula N2, is a colorless, odorless, and inert gas that makes up approximately 78% of the Earth's atmosphere. This ubiquitous gas has a wide range of applications, from industrial processes to medical and scientific research. One of the fundamental properties of nitrogen gas is its ability to undergo physical adsorption, a process that has significant implications in various fields.Physical adsorption, also known as physisorption, is a phenomenon where molecules or atoms of a substance (the adsorbate) accumulate on the surface of another substance (the adsorbent) without forming chemical bonds. This process is driven by the attractive forces between the adsorbate and the adsorbent, such as van der Waals forces and electrostatic interactions. In the case of nitrogen gas, the physical adsorption of N2 molecules onto various adsorbents has been extensively studied and has found numerous applications.One of the primary applications of nitrogen gas physical adsorption is in the field of gas separation and purification. Nitrogen gas can beselectively adsorbed onto specific adsorbents, such as activated carbon, zeolites, or metal-organic frameworks (MOFs), while other gases, such as oxygen or carbon dioxide, are not adsorbed as strongly. This selective adsorption allows for the efficient separation and purification of nitrogen gas from air or other gas mixtures. This process is particularly useful in industrial settings, where high-purity nitrogen gas is required for various applications, such as in the electronics industry, food packaging, or the production of chemicals.Another important application of nitrogen gas physical adsorption is in the area of gas storage and transportation. Nitrogen gas can be adsorbed onto porous adsorbents, such as activated carbon or metal-organic frameworks, to create high-density storage systems. These adsorbent-based storage systems can store a significantly larger amount of nitrogen gas compared to traditional compressed gas cylinders, making them more efficient and cost-effective for transportation and storage. This technology is particularly relevant in applications where large volumes of nitrogen gas are required, such as in the industrial or medical sectors.The physical adsorption of nitrogen gas is also crucial in the field of catalysis. Many catalytic processes involve the interaction of reactants with the surface of a catalyst, and the adsorption of nitrogen gas can provide valuable information about the catalyst's surface properties and accessibility. By studying the physicaladsorption of nitrogen gas on catalyst surfaces, researchers can gain insights into the catalyst's pore structure, surface area, and other characteristics that are essential for optimizing catalytic performance.In the field of material science, the physical adsorption of nitrogen gas is used to characterize the porous structure and surface properties of various materials, such as zeolites, activated carbon, and metal-organic frameworks. The analysis of nitrogen adsorption-desorption isotherms, which describe the relationship between the amount of nitrogen adsorbed and the pressure at a constant temperature, can provide information about the material's surface area, pore size distribution, and other structural features. This information is crucial for the development and optimization of materials with specific applications, such as in catalysis, adsorption, or energy storage.Furthermore, the physical adsorption of nitrogen gas is widely used in the field of environmental science and engineering. Nitrogen-based compounds, such as nitrates or nitrites, can be adsorbed onto various adsorbents, including activated carbon or clay minerals, for the removal of these pollutants from water or soil. This process is particularly important in the treatment of wastewater or the remediation of contaminated sites, where the removal of nitrogen-containing compounds is crucial for environmental protection.In conclusion, the physical adsorption of nitrogen gas is a fundamental phenomenon with a wide range of applications across various scientific and technological fields. From gas separation and purification to gas storage, catalysis, material characterization, and environmental remediation, the understanding and manipulation of nitrogen gas physical adsorption have been instrumental in advancing scientific knowledge and driving technological innovation. As research in this field continues to evolve, new and exciting applications of nitrogen gas physical adsorption are likely to emerge, further expanding its impact on our modern world.。

表面化学官能团改性多孔碳(英文)

表面化学官能团改性多孔碳(英文)

Recent Patents on Chemical Engineering 2008, 1, 27-40271874-4788/08 $100.00+.00© 2008 Bentham Science Publishers Ltd.Surface Chemical Functional Groups Modification of Porous CarbonWenzhong Shen*,1, Zhijie Li 2 and Yihong Liu 11State Key Laboratory of Heavy Oil, China University of Petroleum, Dongying, Shandong, 257061, P. R. China2Department of Applied Physics, University of Electronic Science and Technology of China, Chengdu, Sichuan, 610054, P. R. ChinaReceived: August 29, 2007; Accepted: September 11, 2007; Revised: November 2, 2007Abstract: The surface chemistry and pore structure of porous carbons determine its application. The surface chemistry could be modified by various methods, such as, acid treatment, oxidization, ammonization, plasma, microwave treatment, and so on. In this paper, the modification methods were illustrated and compared, some new methods also reviewed. The surface chemical functional groups were determined by the treatment methods, the amminization could increase its basic property while the oxidization commonly improved its acids. In the end, the commonly characterization methods were also mentioned. Some interesting patents are also discussed in this article.Keywords: Porous carbon, surface chemical groups, modification, characterization. 1. INTRODUCTIONPorous carbons had been widely used as adsorbents, catalyst/catalyst supports, electronic material and energy storage material due to its higher surface area and larger pore volume.The specific surface area, pore structure and surface chemical functional groups of porous carbon determined its applications [1-2]. The pore structure of porous carbon could be controlled by various routes, such as, activation conditions (activation agent, temperature and time), precursor, templates, etc. The surface chemical functional groups mainly derived from activation process, precursor, heat treatment and post chemical treatment.The surface functional groups anchored on/within carbons were found to be responsible for the variety in physicochemical and catalytic properties of the matters considered [3-5]. So, many researchers focused on how to modify as well as to characterize the surface functional groups of carbon materials in order to improve or extend their practical applications [5-7]. Ljubisa R. Radovic reviewed the carbon materials as adsorbents in aqueous solution and pointed out that the control of chemical and physical conditions might be harnessed to produce carbon surfaces suitable for particular adsorption applications [8]. Carlos Moreno-Castilla compared the surface chemistry of the carbon has a great influence on both electrostatic and non-electrostatic interactions, and can be considered the main factor in the adsorption mechanism from dilute aqueous solutions [9].Modification of the surface chemistry of porous carbons might be a viable attractive route toward novel applications of these materials. A modified activated carbon containing*Address correspondence to this author at the State Key Laboratory of Heavy Oil, China University of Petroleum, Dongying, Shandong, 257061, P. R. China; Tel: +86-546-8395341; Fax: +86-546-8395395; E-mail: shenwzh2000@ different functional groups could be used for technological applications such as extracting metallic cations from aqueous and nonaqueous solutions, in catalysis, for treatment of waste and toxic effluents produced by a variety of chemical processes, and so on.The heteroatoms on the surface of activated carbon took significant role on its application. The heteroatoms of porous carbon surface mainly contained oxygen, nitrogen, hydrogen, halogen, etc, which bonded to the edges of the carbon layers and governed the surface chemistry of activated carbon [10]. Among these heteroatoms, the oxygen-containing functional groups (also denoted as surface oxides) were the widely recognized and the most common species formed on the surface of carbons, which significantly influenced their performance in sensors [11], energy storage and conversion systems [12-14], catalytic reactions [15], and adsorptions [16-18]. The surface oxygen-containing functional groups could be introduced by mechanical [19, 20], chemical [21, 22], and electrochemical routes [23]. The employment of oxidizing agents in wet or dry methods was reported to generate three types of oxygen-containing groups: acidic, basic, and neutral [24-27]. Based on the above modifications, a continuous supply of suitable oxidizing agents into the pores of a carbon matrix was believed to be a key factor determining the successful introduction of reliable oxygen-containing functional groups onto the surface of carbon materials.In addition, the nitrogen-containing groups generally provide basic property, which could enhance the interaction between porous carbon and acid molecules, such as, dipole-dipole, H-bonding, covalent bonding, and so on. The nitrogen groups were introduced by ammine treatment, nitric acid treatment and some containing nitrogen molecule reaction.In this review, we focused on the introducing oxygen and nitrogen heteroatoms on traditional porous carbon (activated carbon and activated carbon fiber) by various methods; the improved application property of modified porous carbon28 Recent Patents on Chemical Engineering, 2008, Vol. 1, No. 1 Shen et al. was also illustrated. In the end, the ordinarily character-rization means of oxygen and nitrogen groups were listed.2. METHODS FOR SURFACE MODIFICATIONThe nature and concentration of surface functionalgroups might be modified by suitable thermal or chemicalpost-treatments. Oxidation in the gas or liquid phase couldbe used to increase the concentration of surface oxygengroups; while heating under inert atmosphere might be usedto selectively remove some of these functions. It was shownthat gas phase oxidation of the carbon mainly increased theconcentration of hydroxyl and carbonyl surface groups,while oxidations in the liquid phase increased especially theconcentration of carboxylic acids [2]. Carboxyl, carbonyl,phenol, quinone and lactone groups on carbon surfaces wereshown in Fig. (1) [28].While, the ammonization could introduce the basicgroups, such as, C-H, C=N groups, amino, cyclic amides,nitrile groups, pyrrole-like structure [29]; which were shownin Fig. (2) [30]. In addition, the halogen-containing groupscould produce through porous carbon reacted with halogen atmoderate temperature, this modified porous carbon showedpotential application in electrochemistry or batteries [31].2.1. Acid TreatmentAcid treatment was generally used to oxidize the porouscarbon surface; it enhanced the acidic property, removed themineral elements and improved the hydrophilic of surface.The acid used in this case should be oxidization in nature;the nitric acid and sulfuric acid were the most selected.Liu et al. reported that coconut-based activated carbonwas modified by nitric acid and sodium hydroxide; it showedexcellent adsorption performance for Cr (VI) [32].Modification caused specific surface area to decrease and thetotal number of surface oxygen acidicgroups to increase. Nitric acid oxidization produced positiveacid groups, and subsequently sodium hydroxide treatmentreplaced H+ of surface acid groups by Na+, and the acidity ofactivated carbon decreased. The adsorption capacity of Cr(VI) was increased from 7.61mg/g to 13.88mg/g due to thepresence of more oxygen surface acidic groups and suitablesurface acidity after modification.Shim et al. also modified the pitch-based activatedcarbon fibers with nitric acid and sodium hydroxide [6]. Thespecific surface area of the activated carbon fibers decreasedafter oxidation with 1 M nitric acid, but the total acidityincreased three times compared to the untreated activatedcarbon fibers, resulting in an improved ion-exchangecapacity of the activated carbon fibers. The points of zerocharge of the activated carbon fibers that affect theselectivity for the ionic species changed from pH 6 to pH 4by 1 M nitric acid and to pH 10 by 1 M sodium hydroxidetreatment. The carboxyl acid and quinine groups wereintroduced after nitric acid oxidation. The carboxyl groups ofactivated carbon fibers decreased, while the lactone andketone groups increased after the sodium hydroxidetreatment. The adsorption capacity of copper and nickel ionis mainly influenced by the lactone groups on the carbonsurface, pH and by the total acidic groups.Coal-based activated carbons were modified by chemicaltreatment with nitric acid and thermal treatment undernitrogen flow [33]. The treatment with nitric acid caused theintroduction of a significant number of oxygenated acidicsurface groups onto the carbon surface, while the heattreatment increases the basicity of carbon. The porecharacteristics were not significantly changed after these Fig. (1). Simplified schematic of some acidic surface groups bonded to aromatic rings on AC [28].Fig. (2). The nitrogen functional forms possibly present in carbonaceous materials [30].H HO-Pyrrole Pyridine Pyridinium Pyridone Pyridine-N-oxideHCarboxyl Quinone HydroxylCarbonyl Carboxylic anhyride LactoneSurface Chemical Modification of Porous Carbon Recent Patents on Chemical Engineering, 2008, Vol. 1, No. 1 29modifications. The dispersive interactions are the most important factor in this adsorption process. Activated carbon with low oxygenated acidic surface groups has the best adsorption capacity for benzene and toluene.The coconut-based activated carbon was pretreated with different concentrations of nitric acid (from 0.5 to 67%) and was selected as palladium catalyst support [34], the result showed that the amount of oxygen-containing groups and the total acidity on the activated carbons, the Pd particle size and catalytic activity of Pd/C catalysts are highly dependent upon the nitric acid concentration used in the pretreatment. The pretreatment of activated carbon with a low concentration of nitric acid could increase the structure parameters due to removal of the impurities, would be beneficial to create an appropriate density of total acidity environment, and would further improve the Pd dispersion and the catalytic activity of Pd/C catalysts. Meanwhile, a too-large amount of oxygen-containing groups assembling densely on the activated carbon could influence the Pd dispersion on the activated carbon well.Peach stone shells were pretreated by H3PO4 and pyrolysis at 500o C for 2 h, then, it was prepared by changing the gas atmosphere during thermal treatment (no external gas, flowing of nitrogen, carbon dioxide, steam or air [35]. High uptake of p-nitrophenol appears, affected to low extent with gaseous atmosphere except steam which raises adsorption considerably. Flowing air was the most effective in enhancing the adsorption of methylene blue, which was attributed to the formation of oxygen-functionalities with acidic nature, and to enhancement of wider microporosity. The removal of lead ions was considerably enhanced by running air during thermal treatment (two-fold increase) due to the formation of acidic oxygen-functionalities associated with metal exchange by the negatively charged carbon surface. Li describes the method of eliminating residual carbon from flow able oxide [36].The activated carbon derived from poly(VDC/MA) was treated with HNO3/H2SO4 solutions and heat-treatment in Ar [37]. Acid-treatment increased the adsorption of methyl mercaptan compared with the original activated carbon, and the adsorbed amounts increased with ratio of H2SO4 in HNO3/H2SO4 solutions. Hydrogen bonding between acidic groups formed by acid-treatment and thiol-groups methyl mercaptan played a role in adsorption of methyl mercaptan on activated carbon. Hasenberg et al. shows a process and catalyst blend for selectively producing mercaptans and sulfides from alcohols [38].Surface modification of a coal-based activated carbon was performed using thermal and chemical methods [39]. Nitric acid oxidation of the conventional sample produced samples with weakly acidic functional groups. There was a significant loss in microporosity of the oxidized samples which was caused by humic substances that were formed as a by-product during the oxidation process. However, thermal treatment produced a carbon with some basic character while amination of the thermally treated carbon gave a sample containing some amino (-NH2) groups.The formation of the weakly acidic functional groups on porous carbon surface were thought to be similar to the reaction involving the oxidation of 9,10-dihydrophen-anthrene and diphenylmethane with nitric acid [40], and the mechanism was displayed in Fig. (3). The formation of the dicarboxylic group was thought to occur on the aliphatic side of the molecule especially if the side chains consisted of more than one carbon atom (reaction (a)). The reaction was initiated by the splitting of the C-C at the a-position of the benzylic carbon atom. Oxidation involving a methylene (-CH2-) group would result in the formation of a ketone as shown in reaction (b). Nitrogen could be added to the carbon by a similar reaction as in the nitration of benzene. The mechanism would involve the formation of the highly reactive nitronium ion (NO2-), which would ultimately form the nitrated product as shown in reaction (c).The amination reaction was achieved via a two stage process. The first stage was the nitration stage where the nitric acid was mixed with concentrated sulphuric acid to form the nitronium ions which then reacted via electrophilic substitution of the hydrogen ion of the carbon matrix as shown in reaction (d). The formed nitro-species formed was reduced using a suitable reducing agent and in this case sodium dithionite was employed. This result then showed the effectiveness of the reduction reaction shown in reaction (e). This modification process was another example of the application of a classic organic reaction on activated carbon modification. The reaction was shown in the illustration of the amination of phenanthrene.Calvo et al. reported that the surface chemistry of commercial activated carbon was one of the factors determining the metallic dispersion and the resistance to sintering, being relevant the role of surface oxygen groups [41]. The surface oxygen groups were considered to act as anchoring sites that interacted with metallic precursors and metals increasing the dispersion, with CO-evolving complexes significantly implied in this effect. On the other hand, CO2-evolving complexes, mainly carboxylic groups, seemed to decrease the hydrophobicity of the support improving the accessibility of the metal precursor during the impregnation step. The treatment of activated carbons with nitric acid led to a higher content in oxygen surface groups, whereas the porous structure was only slightly modified. As a result of oxidation, the dispersion of Pd on the surface of activated carbon was improved.Santiagoet al. compared several activated carbons for the catalytic wet air oxidation of phenol solutions [42]. Two commercial activated carbons were modified by HNO3, (NH4)2S2O8, or H2O2 and by demineralisation with HCl. The treatments increased the acidic sites, mostly creating lactones and carboxyls though some phenolic and carbonyl groups were also generated. Characterisation of the used activated carbon evidenced that chemisorbed phenolic polymers formed through oxidative coupling and oxygen radicals played a major role in the catalytic wet air oxidation over activated carbon.Also, citric acid was used to modify a commercially available activated carbon to improve copper ion adsorption from aqueous solutions [25]. It was found that the surface modification by citric acid reduced the specific surface area by 34% and point of zero charge (pH) of the carbon by 0.5 units. But the modification did not change both external diffusion and intraparticle diffusion.30 Recent Patents on Chemical Engineering, 2008, Vol. 1, No. 1 Shen et al.2.2. Ammonia TreatmentIt was well known that nitrogen-containing surfacegroups gave to activated carbons increased ability to adsorb acidic gases [43]. Practically, nitrogen was introduced intostructure of activated carbon according to several proceduresincluding treatment with ammonia or preparation of theadsorbent from nitrogen-containing polymers (Acrylictextile, polyaryamide or Nomex aramid fibers) [44-46].Heating of phenol-formaldehyde-based activated carbon fiber in the atmosphere of dry ammonia at severaltemperatures ranged from 500o C to 800o C resulted in aformation of new nitrogen-containing groups in the structureof the fiber including C-N and C=N groups, cyclic amides,nitrile groups (C N) [47], and pyrrole-like surface structures with N-H groups [48]. Despite the changes in the surface chemistry, an outcome of heating of activatedcarbons in ammonia atmosphere might also be changed inporosity of the treated carbon. As it reported, extensive heat-treatment with gaseous ammonia might cause changes in therelative amounts of macropore, mesopore and micropores ofcommercial activated carbon [42].In any case, since introducing of nitrogen-containingsurface groups made activated carbon more alkaline and soincreased adsorption of acidic agents is expected.The commercial activated carbons were treated by gaseous NH3 ranging from 400o C to 800o C for 2 h [49]. The CH and CN groups appeared after NH3 treatment. It demonstrated enhanced adsorption of phenol from water due to the formation of nitrogen-containing groups during ammonia-treated, which could form hydrogen bond with phenol.A series of activated carbon fibers were produced by treatment with ammonia to yield a basic surface [47]. The adsorption isotherms of an acidic gas (HCl) showed a great improvement in capacity over an untreated acidic fiber. The adsorption was completely reversible and therefore involved the enhanced physical adsorption instead of chemisorption. This demonstrated that activated carbon fibers could be tailored to selectively remove a specific contaminant (acidic gas) based on the chemical modification of their pore surfaces.Commercial activated carbon and activated carbon fiber were modified by high temperature helium or ammonia treatment, or iron impregnation followed by high temperature ammonia treatment [50]. Iron-impregnated and ammonia-treated activated carbons showed significantly higher dissolved organic matter uptakes than the virgin activated carbon. The enhanced dissolved organic matter uptake by iron-impregnated was due to the presence of iron species on the carbon surface. The higher uptake of ammonia treated was attributed to the enlarged carbon pores and basic surface created during ammonia treatment.A commercial raw granular activated carbon was modified by polyaniline to improve arsenate adsorption [51].Fig. (3). The formation of acidic functional groups by nitric acid and amination reaction by thermal treatment [38].5HNO32HNO3HNO3HNO3NH3NO22HNO2+++++H2O24+OHH2OHH(a)(b)(c)(d)(e)224OOHO++Surface Chemical Modification of Porous Carbon Recent Patents on Chemical Engineering, 2008, Vol. 1, No. 1 31It was found that the modification did not change the specific surface area. The content of the aromatic ring structures and nitrogen-containing functional groups on the modified granular activated carbon was increased. The surface positive charge density was dramatically increased in acidic solutions. The presence of humic acid did not have a great impact on the arsenic adsorption dynamics. The modification significantly enhanced the adsorption of humic acid onto the carbon. Meanwhile, the arsenate was reduced to arsenite during the process.Lin et al. provided a method for minute deposition of polyaniline onto microporous activated carbon fabric could enhance the capacitance of the carbon serving as electrodes for electrochemical capacitors [52]. The result demonstrated that a capacitance enhancement of 50% in comparison with bare carbon could be achieved with minute polyaniline deposition (5wt%) using the deposition method, while only 22% was reached using the conventional method.2.3. Heat TreatmentThe nature and concentration of surface functional groups might be modified by suitable thermal or chemical post-treatments. Heating oxidation in the gas or liquid phase could be used to increase the concentration of surface oxygen groups, while heating under inert atmosphere might be used to selectively remove some of these functions. Thermal treatments had been used to produce activated carbons with basic character and such carbons were effective in the treatment of some organic hydrocarbons [53].Heat treatment of carbon in an inert atmosphere or under inert atmospheres (hydrogen, nitrogen or argon) flow could increase carbon hydrophobicity by removing hydrophilic surface functionalities, particularly various acidic groups [54-57]. It had been shown that H2 was more effective than inert atmospheres because it could also effectively stabilize the carbon surface by deactivation of active sites (i.e., forming stable C-H bonds and/or gasification of unstable and reactive carbon atoms) found at the edges of the crystallites. H2 treatment at 900o C could produce highly stably and basic carbons [52, 55], and the presence of a platinum catalyst could considerably lower the treatment temperature [56]. H2-treated carbons were expected to demonstrate much lower reactivity toward oxygen or chemical agents compared to carbons that were heat-treated in an inert atmosphere. The hydrophobic porous carbon effectively removed the non-polar organic molecules from aqueous solution. However, in order to prepare hydrophobic porous carbon, it needed high temperature and inert/reductive atmospheres to remove the heteroatoms on the surface of porous carbon.The wood, coal-based activated carbons and a commer-cial activated carbon fiber with different physicochemical characteristics were subjected to heat treatment at 900o C under vacuum or hydrogen flow [58]. Oxygen sorption experiments showed lower amounts of oxygen uptake by the H2-treated than by the vacuum-treated carbons, indicating that H2 treatment effectively stabilized the surfaces of various carbons. At low pressures, from 0.001 mmHg to 5 mmHg, adsorption of oxygen was governed by irreversible chemisorption, which was well described by the Langmuir equation. At higher pressures oxygen uptake occurred as a result of physisorption, which was in agreement with Henry’s law. Kinetic studies showed that oxygen chemisorp-tion was affected by both carbon surface chemistry and porosity. The results indicated that oxygen chemisorption initially started in the mesopore region from the high energetic sites without any mass transfer limitation; thus a constant oxygen uptake rate was observed. Once the majo-rity of these sites were utilized, chemisorption proceeded toward the less energetic sites in mesopores as well as all the sites located in micropores. As a result, an exponential decrease in the oxygen uptake rate was observed.Different precursors resulted in various elemental compositions and imposed diverse influence upon surface functionalities after heat treatment. The surface of heat-treated activated carbon fibers became more graphitic and hydrophobic. Polyacrylonitrile- and rayon-based activated carbon fibers subjected to heat treatment [59]. The presence of nitride-like species, aromatic nitrogen-imines, or chemi-sorbed nitrogen oxides was found to be of great advantage to adsorption of water vapor or benzene, but the pyridine-N was not. Unstable complexes on the surface would hinder the fibers from adsorption of carbon tetrachloride. The rise in total ash content or hydrogen composition was of benefit to the access of water vapor.2.4. Microwave TreatmentThe main advantage of using microwave heating was that the treatment time could be considerably reduced, which in many cases represented a reduction in the energy con-sumption. It was reported that microwave energy was derived from electrical energy with a conversion efficiency of approximately 50% for 2450 MHz and 85% for 915 MHz [60].Thermal treatment of polyacrylnitrile activated carbon fibers had been carried out using a microwave device [61]. Microwave treatment affected the porosity of the activated carbon fibers, causing a reduction in micropore volume and micropore size. Moreover, the microwave treatment was a very effective method for modifying the surface chemistry of the activated carbon fibers with the production of pyrone groups. As a result very basic carbons, with points of zero charge approximately equal to 11, were obtained.Microwave heating offered apparent advantages for activated carbon regeneration, including rapid and precise temperature control, small space requirements and greater efficiency in intermittent use [62]. Quan et al. investigated the adsorption property of acid orange 7 by microwave regeneration coconut-based activated carbons[63]. It was found that after several adsorption-microwave regeneration cycles, the adsorption rates and capacities of granular activated carbons could maintain relatively high levels, even higher than those of virgin Granular activated carbons. The improvement of granular activated carbons adsorption properties resulted from the modification of pore size distribution and surface chemistry by microwave irradiation.2.5. Ozone TreatmentOzone as a strong oxidization agent was widely applied in organic degradation; it could also oxidize the carbon material surface to introduce oxygen-containing groups. The32 Recent Patents on Chemical Engineering, 2008, Vol. 1, No. 1 Shen et al.ozone dose and oxidization time affected the resultant oxygen-containing groups and the oxygen concentration on the carbon surface. The result of bituminous origin-based activated carbon oxidization with ozone showed that the higher the ozone dose, the higher was the oxidation of the carbon and the greater was the number of acid groups present on the carbon surface, especially carboxylic groups, whereas the pH of the point of zero charge decreased [64]. The surface area, micropore volume, and methylene blue adsorption all reduced with higher doses. These results were explained by the ozone attack on the carbon and the fixation of oxygen groups on its surface. Jackson introduces a method for supercritical ozone treatment of a substrate [65].The impact of ozonation on textural and chemical surface characteristics of two coal-based activated carbons and their ability to adsorb phenol, p-nitrophenol, and p-chlorophenol from aqueous solutions had been investigated by Alvarez et al. [66]. The porous structure of the ozone-treated carbons remained practically unchanged with regard to the virgin activated carbon. At 25o C primarily carboxylic acids were formed while a more homogeneous distribution of carboxylic, lactonic, hydroxyl, and carbonyl groups was obtained at 100o C.2.6. Plasma TreatmentThe plasma treatment was regarded as a promising technique to modify the surface chemical property of porous carbon since it produced chemically active species affecting the adsorbability. During the plasma treatment, the slower chemical reaction by chemically active species took place only on the surface of activated carbon without changing its bulk properties at low pressure by long time treatments. It was possible to create any ambiance for oxidative, reductive, or inactive reaction by changing the plasma gas [67]. Plasma could introduce basic and acid functional groups that were determined by the gaseous resource. The semi-quantitative analysis of the surface acidic functional groups showed that a difference in treatment conditions affected the quality and quantity of the functional groups [68].Some experimental efforts had been reported on activated carbon treatment with oxygen-included plasmas. The negative charge of activated carbon was brought after the plasma treatment was due to dissociation of newly formed acidic groups. The hydrophilicity of plasma-treated carbons did not change significantly. The oxygen plasma appeared not to reach the smallest micropores of the carbon, indicating that the reaction took place only near the external surfaces of the particles [69, 70]. The surface area of activated carbon that was treated by oxygen non-thermal plasma was decreased, and the concentrations of acidic functional groupsat the surface were increased and the saturated adsorption amount of copper and zinc ion was considerably increased [71-74]. Oxygen species produced during the discharge react on the activated carbon surface resulting in the creation of weakly acidic functional groups that played an important role in adsorbing metal cations. Improvement in the adsorbability was attributed to the change in the surface chemical structure of the commercial activated carbon rather than the modification of the surface physical structure [75]. For example, the CF4 plasma treatment could effectively improve the hydrophobic property, polarization and power density of the activated carbon fibers [76]. The activation of the carbon-surface by the nitrogen radio frequency plasma yielded a significant increase in adhesion for Cu-coatings [77]. The submicron vapor grown carbon fibers preserved their general smoothness upon plasma oxidation and the structural changes brought about by this treatment essentially took place only at the atomic scale [78]. The vapor grown carbon fibers were modified using NH3, O2, CO2, H2O and HCOOH plasma gases to increase the wettability and the results show that the oxidation strength was O2>CO2>H2O>HCOOH [79]. The polyacrylonitrile fibers were treated with the nitrogen glow discharge plasma and the hydrophilic groups (N-H, C=N) were introduced on the fiber surfaces [80]. The air and nitrogen glow discharge were usedto modify the activated carbon fibers, their surface became rough and several types of polar oxygen groups were introduced into the carbon fiber surface [81].The invention by Miller et al. induces the steps of evaporation for regeneration of commercial activated carbon[82].Viscose-based activated carbon fibers were treated by a dielectric-barrier discharge plasma and nitrogen as deed gas at different conditions [83]. It showed that the nitrogen plasma modification could remarkably change the distribution of the oxygen functional groups on the activated carbon fibers surface and there were more nitrogen atoms incorporated into the aromatic ring.Different plasma treatment and the changes of related chemical functional groups were listed in Table 1.In addition, space charge density could be improved by nitrogen plasma surface treatment of carbon materials [84].Recently, atmospheric pressure plasma could treat various materials even those which were low temperatureTable 1. The Related Chemical Groups Change at Different Plasma Treatment ConditionsPlasma gaseous Increased chemical groups Decreased chemical groups O2– C-OOH, C=O – C-OH, C-O-C [72]N2– C-OH, C-O-C–, O=C-O, pyridine and quaternary nitrogen – C=O (aromatic ring) [79]NH3 N-H[70]CO2– C-OOH, C=O [76]H2O – C-OOH, C=O [76]。

二氧化钛表面超强酸化光氧复合降解罗丹明B

二氧化钛表面超强酸化光氧复合降解罗丹明B

第40卷第2期2021年3月Vol.40No.2Mar.2021大连工业大学学报JournalofDalianPolytechnicUniversityDOI:10.19670/ki.dlgydxxb.2021.0210二氧化钛表面超强酸化光氧复合降解罗丹明B温宇,杨大伟(大连工业大学轻工与化学工程学院,辽宁大连116034)摘要:采用共结晶方法制备了锌锆共掺杂的介孔二氧化钛,前驱体用硫酸处理使其具有超强酸性。

将制备的介孔二氧化钛用于降解废水模拟物罗丹明B,测试其光催化与氧催化降解能力。

通过紫外-可见分光光度计、X射线衍射、电镜扫描等对催化剂进行表征,实验结果表明,在强酸修饰二氧化钛前驱体的影响下,掺杂锌锆的介孔二氧化钛具有光催化与氧催化活性。

锌锆共掺杂介孔二氧化钛的光催化与氧催化效率分别达到了72%与25%o硫酸处理后在TiO2与掺杂原子表明形成酸性中心,在无光条件下氧化降解废水效率为30%,提高了降解效率。

关键词:二氧化钛;光催化;酸催化;罗丹明B中图分类号:X703.5文献标志码:A文章编号:1674-1404(2021)02-0136-04Composite degradation of rhodamine B using TiO2withphotocatalytic oxygen and super acidWEN Yu,YANG Dawei(SchoolofLightndustryandChemicalEngineering,DalianPolytechnicUniversity,Dalian116034,China) Abstract:The mesoporous titania doped with zinc oxide,zirconium dioxide,zinc and zirconium were prepared by the co-crystallization method and the precursor of mesoporous titania was pretreated with sulfuric acid to endowed it super acidic.The mesoporous titania was used for degradation of rhodamine B in simulated wastewater and its photocatalytic activity and oxygen catalytic ability was analyzed by UV-visible spectrophotometer,X ray diffraction,scanning electron microscopy.The results showed that the T1O2doped metal oxides and super acid exhibited excellent photocatalytic and oxygen catalytic ability.The degradation rate of rhodamine B photocatalyzed and oxygen catalyzed by the prepared catalysts were72%and25%,respectively.After treatment with sulfuric acid,the acidic centers were formed between the doped atoms and the surface of titanium dioxide,which improved the oxygen degrading efficiency of wastewater to30%.Keywords:TiO2;photocatalytic;acidic catalysis;rhodamine B0引言工业生产中生成的有机废水对环境造成严重污染,国家对废水排放标准执行越来越严格,如何降低或消除有机废水中大分子有机物成为研究的重点。

活性炭纤维吸附含溴甲烷气体的性能_李小波

活性炭纤维吸附含溴甲烷气体的性能_李小波

第7卷第8期环境工程学报Vol .7,No .82013年8月Chinese Journal of Environmental EngineeringAug .2013活性炭纤维吸附含溴甲烷气体的性能李小波1关建建1黄庆林2张瑞峰2楼旭日2马兰3周矛峰4王同华1*(1.大连理工大学工业生态与环境工程教育部重点实验室,化工学院炭素材料研究室,大连116024;2.中国天津出入境检验检疫局,天津300457;3.中国人民解放军防化研究院,北京100191;4.江苏同康活性炭纤维特种面料有限责任公司,南通226003)摘要采用动态吸附法在25ħ下,测定了3种活性炭纤维(ACF-1、ACF-2和ACF-3)对含溴甲烷气体的吸附性能和回收效果,并对活性炭纤维的孔结构进行表征。

探讨了孔结构、溴甲烷浓度、气体流量、循环使用次数等因素对活性炭纤维吸附溴甲烷性能的影响。

结果表明,活性炭纤维比表面积大小及0.4 0.8nm 左右的微孔数量决定了其对溴甲烷吸附性能的优劣;气体中溴甲烷的浓度的提高使活性炭纤维对溴甲烷的穿透和饱和吸附量增加,而气体流量的增加则使活性炭纤维对溴甲烷的穿透和饱和吸附量降低,但两者均使穿透和饱和吸附时间缩短;活性炭纤维多次循环使用后,对溴甲烷的吸附容量明显地降低,循环12次后达到稳定吸附,其稳定吸附值为133.5mg /g 。

关键词溴甲烷活性炭纤维吸附废气中图分类号X701.7文献标识码A文章编号1673-9108(2013)08-3131-06Adsorption performance of CH 3Br-containing gas on activated carbon fiberLi Xiaobo 1Guan Jianjian 1Huang Qinglin 2Zhang Ruifeng 2Lou Xuri 2Ma Lan 3Zhou Maofeng 4Wang Tonghua 1(1.Key Laboratory of Industrial Ecology and Environmental Engineering ,Ministry of Education ,Carbon Research Laboratory ,School of Chemical Engineering ,Dalian University of Technology ,Dalian 116024,China ;2.Tianjin Enter-Exit Inspection and Quarantine Bureau ,Tianjin 300457,China ;3.Institute of Chemical Defense of thePeople ’s Liberation Army ,Beijing 100191,China ;4.Jiangsu Tongkang Activated Carbon Fibers Co.Ltd.,Nantong 226003,China )Abstract The adsorption and recovery performances of CH 3Br from the waste gas containing CH 3Br vapor on the activated carbon fiber were studied by dynamic adsorption method.The effects of pore structure of ACF ,CH 3Br concentration in waste gas ,gas flow and adsorption cycle times of ACF on the breakthrough and saturation adsorption quantity of CH 3Br were investigated.The results show that the adsorption performances of CH 3Br on ACF depend on the specific surface area and the amount of micropore with the size of 0.4 0.8nm.As the in-crease of CH 3Br concentration in waste gas ,the breakthrough and saturated adsorption quantities of CH 3Br on ACF were enhanced .And the rise of gas flow resulted in the opposite results.But both shorten the breakthrough and saturated adsorption time of CH 3Br on ACF.With the increase of cycle times ,the adsorption capacity of CH 3Br on ACF reduces obviously.The adsorption capacity of CH 3Br reaches the stable adsorption value of 133.5mg /g when ACF are recycled up to 12times.Key words CH 3Br ;activated carbon fiber ;adsorption ;waste gas 收稿日期:2012-04-17;修订日期:2012-06-05作者简介:李小波(1985 ),男,硕士研究生,主要研究方向:活性炭纤维和炭纤维的制备及性能的研究。

吸附热力学的英文

吸附热力学的英文

吸附热力学的英文English:Adsorption thermodynamics refers to the study of the heat effects involved in the process of adsorption, which is the accumulation of gas, liquid, or dissolved substances on the surface of a solid or a liquid. It encompasses the analysis of the energy changes, such as the heat of adsorption, enthalpy, and entropy, that occur during the adsorption process. The investigation of adsorption thermodynamics is crucial in understanding the physical and chemical properties of adsorbents and adsorbates, as well as in the design and optimization of adsorption processes in various industries. By studying the thermodynamics of adsorption, researchers and engineers can gain insights into the efficiency, selectivity, and performance of different adsorbents, ultimately leading to the development of more effective adsorption systems for environmental remediation, gas purification, and separation processes.中文翻译:吸附热力学指的是研究吸附过程中涉及的热效应,吸附是指气体、液体或溶解物质在固体或液体表面的积聚。

玉米秸秆和玉米芯生物炭对水溶液中无机氮的吸附性能

玉米秸秆和玉米芯生物炭对水溶液中无机氮的吸附性能

玉米秸秆和玉米芯生物炭对水溶液中无机氮的吸附性能武丽君;王朝旭;张峰;崔建国【摘要】为探明玉米秸秆和玉米芯生物炭对水溶液中无机氮的吸附性能,研究了其对NH4+-N、NO3--N和NO2--N的吸附动力学过程;并用等温吸附模型对NH4+-N和NO3--N的吸附过程进行拟合,探讨制得生物炭对无机氮的吸附机理.结果表明,400℃和600℃制得玉米秸秆和玉米芯生物炭均呈碱性,表现为400℃<600℃;同种原材料,与400℃制得生物炭相比,600℃制得生物炭碱性含氧官能团数量较多,而酸性含氧官能团数量较少.400℃制得生物炭对NH4+-N的吸附能力较强(玉米秸秆和玉米芯生物炭的平衡吸附量分别为4.22和4.09mg/g);而600℃制得生物炭对NO3--N和NO2--N的吸附能力较强(玉米秸秆和玉米芯生物炭对NO3--N的平衡吸附量分别为0.73和0.63mg/g;对NO2--N的平衡吸附量分别为0.55和0.35mg/g).与 NO3--N 和 NO2--N 相比,玉米秸秆和玉米芯生物炭对 NH4+-N 的吸附能力更强,4种生物炭对NH4+-N 的平衡吸附量是 NO3--N/NO2--N 的4.29~20.2倍.等温吸附模型拟合研究表明,玉米秸秆和玉米芯生物炭对水溶液中 NH4+-N 和NO3--N的吸附过程均可用Freundlich模型描述,其在生物炭表面的吸附是多分子层吸附.%In order to explore the adsorption characters of inorganic nitrogen in aqueous solution by maize straw- and corn cob-derived biochars, the adsorption kinetics of NH4+-N, NO3--N and NO2--N were studied. The adsorption processes of NH4+-N andNO3--N were fitted by Langmuir and Freundlich isothermal adsorption models, and the adsorption mechanisms were also elucidated. The results showed that the maize straw- and corn cob-derived biochars produced at 400℃ and 600℃ were both alkaline (400℃<600℃).As for the same rawmaterial, the biochar produced at 600℃ showed relatively higher alkaline oxygen-containing functional group content and lower acidic oxygen-containing functional group content compared with the biochar produced at 400℃. The biochars produced at 400℃ had a stronger adsorption capacity to NH4+-N (the equilibrium adsorption amounts of maize straw- and corn cob-derived biochars were 4.22 and 4.09mg/g, respectively). However, the biochars produced at 600℃ had a stro nger adsorption capacity to NO3--N and NO2--N (for NO3--N: the equilibrium adsorption amounts of maize straw- and corn cob-derived biochars were 0.73 and 0.63mg/g, respectively; for NO2--N: 0.55and 0.35mg/g, respectively). Compared to NO3--N and NO2--N, all the four kinds of biochar showed stronger adsorption capacity to NH4+-N, and the equilibrium adsorption amounts of NH4+-N were 4.29~20.2 times more than NO3--N/NO2--N. The isothermal adsorption model study showed that the adsorption of NH4+-N and NO3--N in aqueous solution by maize straw- and corn cob-derived biochars could be described by Freundlich model, and the multi-layer adsorption was the major adsorption mechanism.【期刊名称】《中国环境科学》【年(卷),期】2016(000)001【总页数】8页(P74-81)【关键词】生物炭;无机氮;吸附性能;含氧官能团【作者】武丽君;王朝旭;张峰;崔建国【作者单位】太原理工大学环境科学与工程学院,山西太原 030024;太原理工大学环境科学与工程学院,山西太原030024; 山西省市政工程研究生教育创新中心,山西太原 030024;太原理工大学环境科学与工程学院,山西太原 030024; 山西省市政工程研究生教育创新中心,山西太原 030024;太原理工大学环境科学与工程学院,山西太原 030024; 山西省市政工程研究生教育创新中心,山西太原030024【正文语种】中文【中图分类】X53∗责任作者, 讲师,*****************农田土壤大量施用氮肥造成了一系列环境问题,氮素淋失不但导致其利用率降低,而且使地下水污染,地表水体富营养化[1-2].因此,寻求减少土壤氮素流失的方法,治理氮污染问题迫在眉睫.近年来,生物炭因其良好的环境效应已成为农业和环境科学领域的研究热点.生物炭是以废弃生物质为原料,在限氧或无氧、高温条件下形成的富碳物质.以玉米秸秆和玉米芯为原料制备生物炭,不但可以变废为宝,而且有利于环境保护[3].玉米秸秆和玉米芯生物炭的农田施用有望缓解土壤氮素流失,提高土壤营养元素水平和生产能力.制备生物炭的原材料、工艺不同,生物炭的理化特性也不尽相同.张千丰等[4]通过3种作物残体(玉米芯、大豆秸秆和水稻颖壳)制备生物炭的研究发现,随热解温度的升高,生物炭的pH值随之升高.李飞跃等[5]在利用稻壳生物炭(热解温度为350和500℃)对水中NH4+-N吸附的研究表明,不同温度制得生物炭都呈碱性,且高温制得生物炭的碱性更强(pH值达9.49).另外,不同热解温度对生物炭表面的含氧官能团含量影响较大.赵牧秋等[6]采用椰糠、木薯秸秆、桉树枝和猪粪4种原材料,分别在300、400、500和600℃条件下制备生物炭,研究表明不同温度制得生物炭的碱性含氧官能团含量随热解温度升高呈增加趋势.郝蓉等[7]在不同热解温度(200~800℃)对水稻秸秆生物炭表面含氧官能团的影响研究中发现,酸性和碱性含氧官能团含量均随热解温度的升高先增加后减少,高温和低温均不利于生物炭含氧官能团的形成.这些差异可能与制炭材料和制炭温度的不同有关.然而,目前为止,生物炭pH 值和酸碱性含氧官能团含量的差异对无机氮吸附性能影响的研究不多[8-9],相关机理解释亦缺乏.因此,本研究选取来源广泛的玉米秸秆和玉米芯作为制备生物炭的原材料,探讨不同制炭温度所得生物炭的特性差异,及其对NH4+-N、NO3--N和NO2--N的吸附动力学特征;并用Langmuir和Freundlich等温吸附模型进行拟合,以阐明玉米秸秆和玉米芯生物炭对NH4+-N和NO3--N的吸附机理.以期为为玉米秸秆和玉米芯生物炭的农田施用提供理论基础.1.1 生物炭的制备及基本特性采用农业废弃生物质玉米秸秆和玉米芯作为原材料制备生物炭.玉米秸秆和玉米芯取自山西省太原市小店区农田,将杂质去除,80℃烘干, 过2mm筛备用.将生物质材料放入管式电阻炉(SKG10123K,天津中环电炉)中,用橡胶塞塞紧两端.升温前预先通入高纯氮气20min(流速150mL/ min),以形成无氧环境;然后以20℃/min的升温速率升温至400℃或600℃,恒温4h;待温度降至室温后取出,研磨,过0.15mm 筛,制成粉末状生物炭备用.400℃和600℃制得玉米秸秆和玉米芯生物炭,分别记为MS400、MS600、CC400和CC600(MS代表玉米秸秆,CC代表玉米芯,400和600代表制炭温度).生物炭表面酸(碱)性含氧官能团数量的测定采用Boehm滴定法[10].称取1.0g样品,加入50mL 0.05mol/L NaOH(HCl)溶液,密闭振荡反应24h;然后取上清液10mL,用0.05mol/L HCl(NaOH)溶液滴定,确定其消耗量,进而计算出生物炭表面酸(碱)性含氧官能团的数量.生物炭表面的电荷分布通过测试等电点(pHpzc)间接表征[11].生物炭的比表面积、总孔容和平均孔径采用N2吸附BET法测定(3H-2000PS2型,贝士德仪器).生物炭的pH值采用pH计测定(炭水比1:10).1.2 吸附动力学研究为探明不同原材料和不同制炭温度所得生物炭对无机氮的吸附性能,分别开展了生物炭对水溶液中铵态氮、硝态氮和亚硝态氮的吸附动力学实验.称取1.0g生物炭于250mL具塞锥形瓶中,加入100mL NH4Cl、NaNO3或NaNO2溶液(100mg/L),在恒温[(25±0.5)℃]条件下振荡(180r/min);分别于0、1、5、20、40、60、90、150和240min采集3mL混匀悬浮液,并在浓度计算中考虑体积变化;过滤后(0.45µm滤膜),采用比色法测定其中NH4+-N、NO3--N和NO2--N的含量[12].式中:qt为t时刻生物炭的吸附量,mg/g;v为混合液体积,L;c0和ct分别为初始和t 时刻混合液中吸附质的浓度,mg/L;m为生物炭投加量,g.1.3 吸附等温线测定采用批量吸附实验测定所制备生物炭对铵态氮和硝态氮的吸附等温线.吸附实验在水平振荡条件下进行.首先向7个50mL锥形瓶中均加入0.25g生物炭;然后依次分别加入25mL浓度为100、150、200、250、300、350和400mg/L的NH4Cl 或NaNO3溶液,恒温[(25±0.5)℃]振荡(180r/min)4.0h后;在悬浮液混匀状态下取样10mL,经0.45µm滤膜过滤后,采用比色法测定其中NH4+-N和NO3--N的含量[12].用Langmuir和Freundlich等温吸附方程对实验数据进行拟合,Langmuir和Freundlich方程常用来描述离子在吸附质上的吸附作用,其吸附方程分别为:式中:ce为吸附平衡时混合液中吸附质的浓度, mg/L;qe为吸附平衡时生物炭的吸附量,mg/g; qmax为生物炭的最大吸附量,mg/g;b为表征吸附剂与吸附质间亲和力的参数,L/mg,b值越大,吸附亲和力越大.式中:ce为吸附平衡时混合液中吸附质的浓度, mg/L;qe为吸附平衡时生物炭的吸附量,mg/g;Kf为Freundlich吸附常数,mg1-1/n·L1/n/g;1/n为Freundlich指数.1.4 数据分析所有实验3次重复,利用Excel 2010对实验数据进行统计分析,并计算其标准偏差;利用Origin 8.0制图.2.1 不同温度条件下玉米秸秆和玉米芯生物炭的基本特性不同温度条件下玉米秸秆和玉米芯生物炭均呈碱性(pH 9.47~10.32);对同种材料而言, 600℃制得生物炭的pH值大于400℃制得生物炭.等电点(pHpzc)也有相同趋势,且pHpzc>pH.同种材料制得生物炭,低温利于酸性含氧官能团的形成,400℃制得玉米秸秆生物炭(MS400)相比600℃制得玉米秸秆生物炭(MS600)增加了0.25mmol/g;400℃制得玉米芯生物炭(CC400)相比600℃制得玉米芯生物炭(CC600)增加了0.13mmol/g.然而,高温则利于碱性含氧官能团的形成,MS600相比MS400增加了0.13mmol/g, CC600相比CC400增加了0.10mmol/g.不同温度制备生物炭的比表面积、总孔容和平均孔径存在差异,其中CC400的比表面积最大(0.65m2/g), 400℃制得生物炭的总孔容大于600℃制得生物炭(表1).同种原料制备的生物炭,热解温度越高,其pH值越高.这主要是由于生物炭中C、O和H等元素在高温时损失较多,而其中的Ca、Mg、K、Na和Si等无机元素经烧结、融合后形成无机矿物,使得生物炭的灰分含量相应增加[14-15],这些灰分物质的形成是生物炭pH值增加的主要原因.一般来说,随着热解温度的升高,酸性含氧官能团含量逐渐降低,而碱性含氧官能团含量则升高.Singh等[16]发现热解温度从400℃升高到550℃时,生物炭酸性含氧官能团含量明显降低(从5.71降至1.58mmol/g).Chun等[17]在以小麦秸秆制备的生物炭的研究中也发现上述相同结论.生物质热解过程中形成的一些酸性物质会部分残留在生物炭中,但随着热解温度的升高,这些物质会逐渐挥发,因而高温制备的生物炭中酸性物质的含量较少,酸性含氧官能团含量较低,而碱性含氧官能团含量则较高[18].研究表明,随着热解温度的升高,材料的裂解程度增加[19],生物炭孔隙结构逐渐发育,比表面积逐渐增大;同时,当热解温度过高时,挥发分气泡演变可导致炭材料结构变化,并使微孔数量减少及大孔数量增加而导致生物炭比表面积减小[20].2.2 不同温度条件下玉米秸秆和玉米芯生物炭对无机氮的吸附动力学2.2.1 生物炭对铵态氮的吸附动力学不同温度条件下玉米秸秆和玉米芯生物炭对水溶液中NH4+-N的吸附,在前30min吸附量急剧增加,之后呈现缓慢增加趋势,在约150min达到吸附平衡.同种原材料,低温(400℃)制得生物炭显著利于NH4+-N的吸附.MS400的平衡吸附量(4.22mg/g) 是MS600的1.31倍,而CC400的平衡吸附量(4.09mg/g)是CC600的1.50倍.另一方面,同一温度不同原材料制得生物炭的NH4+-N吸附性能没有显著差异.MS400和CC400的平衡吸附量分别为4.22mg/g和4.09mg/g,而MS600和CC600的平衡吸附量分别为3.21mg/g和2.72mg/g.综上,不同热解温度所得玉米秸秆和玉米芯生物炭对水溶液中NH4+-N 的吸附性能研究表明,MS400 对NH4+-N的吸附性能最好(图1).研究表明,随热解终温的增加,以橡木为原料制备的生物炭对NH4+-N的吸附量(热解终温为300、400、500和600℃时,吸附量分别为3.12、2.33、1.38和0.15mg/g)随之降低[21].另外,李扬等[22]在芦苇生物炭对底泥氮素释放影响的研究中发现,随着热解温度的升高,生物炭对NH4+-N的吸附能力逐渐减弱(从0.79mg/g降为0.31mg/g).张继义等[23]针对小麦秸秆生物炭对水中NH4+-N吸附性能的研究表明,300℃条件下制得生物炭对溶液中NH4+-N的去除率最大(达到71%),在400、500和600℃条件下,随着炭化温度的升高,所得生物炭对NH4+-N 的去除率依次降低.究其原因,主要由于随着热解温度的升高,生物炭的酸性含氧官能团数量减少,对NH4+-N的吸附能力减弱.本研究表明,同种原材料,低温制得生物炭的NH4+-N平衡吸附量较高与其酸性含氧官能团含量较高有关(表1),生物炭表面的酸性含氧官能团可通过阳离子交换作用吸附固定NH4+-N[24].2.2.2 生物炭对硝态氮和亚硝态氮的吸附动力学不同温度条件下玉米秸秆和玉米芯生物炭对NO3--N的吸附作用在前50min比较明显,吸附速率较快,在90min基本达到吸附平衡.高温制得生物炭对NO3--N的吸附能力较强:MS600对NO3--N的平衡吸附量(0.73mg/g)是MS400的1.43倍,CC600对NO3--N的平衡吸附量(0.63mg/ g)是CC400的1.58倍(图2).生物炭对NO2--N的吸附在前90min急剧增加,之后趋于平缓,在150min达到吸附平衡.与NO3--N类似,高温制得生物炭对NO2--N的吸附能力亦较强:MS600对NO2--N的平衡吸附量(0.55mg/g)是MS400的1.71倍,CC600对NO2--N的平衡吸附量(0.35mg/g)是CC400的1.74倍(图3).4种生物炭对NO2--N的平衡吸附量均比NO3--N小, MS600、MS400、CC600和CC400对NO2--N的平衡吸附量分别比对NO3--N的平衡吸附量减少了0.18、0.19、0.28和0.20mg/g.研究表明,生物炭对NO3--N的吸附性能与其表面碱性含氧官能团数量密切相关.Kameyama等[25]在研究甘蔗渣生物炭对土壤NO3--N淋溶的影响中发现,800℃制得生物炭对NO3--N的吸附能力最好(平衡吸附量0.62mg/g),同时此温度下生物炭形成大量的碱性含氧官能团.王章鸿等[21]研究发现,当热解终温由300℃升至600℃时,橡木生物炭的碱性含氧官能团数量相应增多;同时,随热解终温的升高,生物炭对NO3--N的吸附量呈指数增加(吸附量由0.29增至2.8mg/g).制炭温度越高,生物炭酸性含氧官能团数量越少,而碱性含氧官能团数量则越多,比表面积、表面金属氧化物也随之增多,因此高温制得生物炭对NO3--N和NO2--N的吸附性能优于低温制得生物炭[25].本研究也表明,同种原材料,高温制得生物炭的NO3--N/NO2--N平衡吸附量较高与其碱性含氧官能团含量较高有关(表1).不同温度条件下玉米秸秆和玉米芯生物炭对水溶液中无机氮的吸附实验结果表明,同一生物炭对NH4+-N的平衡吸附量高于NO3--N和NO2--N.MS600、MS400、CC600和CC400 4种生物炭对NH4+-N的平衡吸附量分别是对NO3--N平衡吸附量的4.38、8.24、4.29和10.2 倍,是对NO2--N平衡吸附量的5.81、13.0、7.69 和20.2倍.pHpzc为生物炭表面电荷为零时溶液对应的pH值,而本研究中4种生物炭的pH值均小于其pHpzc值(表1),因此水溶液中生物炭的表面均带正电荷,并与溶液中的NH4+进行交换吸附[26].因此,本研究中4种生物炭对NH4+-N的平衡吸附量均远大于NO3--N和NO2--N.2.3 不同温度条件下玉米秸秆和玉米芯生物炭对铵态氮和硝态氮的吸附等温线2.3.1 不同温度条件下玉米秸秆和玉米芯生物炭对铵态氮的吸附等温线不同温度条件下所得玉米秸秆和玉米芯生物炭对NH4+-N的吸附等温线用Langmuir和Freundlich方程进行拟合(图4、图5).结果表明,随着NH4+-N初始浓度的增加,生物炭对NH4+-N的平衡吸附量也逐渐增大.Langmuir模型中最大吸附量qmax的拟合结果表明,生物炭MS400对NH4+-N的最大吸附量最高(12.2mg/g).Langmuir模型中b为表征吸附剂与吸附质间亲和力的参数,且b值越大,吸附亲和力越大[27].本研究中b值的拟合结果为:MS400>MS600,CC400>CC600.因此,Langmuir模型拟合分析表明,低温制得生物炭(MS400和CC400)对NH4+-N的吸附能力更强(表2).Freundlich模型中吸附常数Kf反映吸附剂吸附能力的强弱,Freundlich指数1/n反映吸附剂吸附位点能量分布的特征.Kf值越大,表明吸附能力越强;1/n值越小,表明吸附强度越大,尤其当0.1<1/n<1时,表明其易于吸附[28-30].拟合结果表明,400℃制得生物炭的Kf值(MS和CC分别为0.66和0.70)大于600℃制得生物炭(MS和CC分别为0.36和0.33);400℃制得生物炭的1/n值(MS 和CC分别为0.45和0.43)小于600℃制得生物炭(MS和CC分别为0.52和0.49).因此,Freundlich模型拟合分析也表明,与高温(600℃)制得生物炭相比,低温(400℃)制得生物炭更有利于NH4+-N的吸附(表2).Langmuir模型假定吸附剂表面由大量吸附活性中心组成,当表面吸附活性中心全部被占满时,吸附量达到饱和值,吸附质在吸附剂表面呈单分子层分布.而Freundlich 模型描述的是多分子层吸附,在吸附质浓度较高时吸附量会持续增加[31].Langmuir 与Freundlich方程都能描述生物炭对NH4+-N的等温吸附过程,两种模型的拟合相关系数(R2)均大于0.94,但Freundlich模型对数据的拟合程度略高,其相关系数(R2)大于0.98.因此,不同温度所得玉米秸秆和玉米芯生物炭对NH4+-N的吸附更符合Freundlich模型,NH4+-N在生物炭表面的吸附是多分子层吸附过程.2.3.2 不同温度条件下玉米秸秆和玉米芯生物炭对硝态氮的吸附等温线不同温度条件下玉米秸秆和玉米芯生物炭对NO3--N的Langmuir 和Freundlich等温吸附拟合曲线如图6、图7所示.Langmuir模型中b值越大,表明吸附亲和力越大[27].600℃制得生物炭的b值(MS和CC分别为2.18和3.72)明显大于400℃制得生物炭(MS和CC分别为1.68和3.40).另一方面,Freundlich模型中Kf值越大,1/n值越小,表明吸附能力越强[28-30].对Kf值而言,MS600>MS400,CC600> CC400;对1/n值而言,MS600<MS400,CC600< CC400.因此,Langmuir和Freundlich模型拟合分析均表明,高温制得生物炭(MS600和CC600)对NO3--N 的吸附能力较强(表3).Langmuir与Freundlich方程都能描述生物炭对NO3--N的等温吸附过程,不同生物炭Langmuir模型的拟合相关系数(R2)均低于Freundlich模型(R2大于0.97).因此,不同温度所得玉米秸秆和玉米芯生物炭对NO3--N的吸附更符合Freundlich 模型,NO3--N在生物炭表面的吸附也是多分子层吸附过程.同种生物炭对NH4+-N 和NO3--N的Freundlich等温吸附模型拟合参数Kf和1/n值的大小亦表明,不同温度所得玉米秸秆和玉米芯生物炭对NH4+-N的吸附能力优于NO3--N.3.1 同种原材料(玉米秸秆或玉米芯),与400℃制得生物炭相比,600℃制得生物炭的pH值较高,碱性含氧官能团数量较多,而酸性含氧官能团数量较少.3.2 生物玉米秸秆和玉米芯生物炭对NH4+-N的吸附效果表现为400℃>600℃;对NO3--N和NO2--N的吸附效果表现为600℃>400℃.3.3 4种生物炭对NH4+-N的平衡吸附量均显著大于NO3--N和NO2--N.3.4 4种生物炭对水溶液中NH4+-N和NO3--N的吸附过程可以用Freundlich 模型描述,其在生物炭表面的吸附是多分子层吸附.【相关文献】[1] 高德才,张蕾,刘强,等.旱地土壤施用生物炭减少土壤氮损失及提高氮素利用率 [J].农业工程学报, 2014,30(6):54-61.[2] 刘汝亮.宁夏引黄灌区稻田氮素淋失特征与过程控制研究 [D].北京:中国农业科学院, 2013.[3] 曹国良,张小曳,郑方成,等.中国大陆秸秆露天焚烧的量的估算[J].资源科学, 2006,28(1):9-13.[4] 张千丰,孟军,刘居东,等.热解温度和时间对三种作物残体生物炭pH值及碳氮含量的影响 [J].生态学杂志, 2013,32(9): 2347-2352.[5] 李飞跃,谢越,石磊,等.稻壳生物质炭对水中氨氮的吸附[J].环境工程学报, 2015,9(3):1221-1226.[6] 赵牧秋,金凡莉,孙照炜,等.制炭条件对生物炭碱性基团含量及酸性土壤改良效果的影响 [J].水土保持学报, 2014,28(4): 299-309.[7] 郝蓉,彭少麟,宋艳暾,等.不同温度对黑碳表面官能团的影响[J].生态环境学报, 2010,19(3):528-531.[8] 邢英,李心清,周志红,等.生物炭对水体中铵氮的吸附特征及其动力学研究 [J].地球与环境, 2011,39(4):511-516.[9] Ding Y, Liu Y X, Wu W X, et al.Evaluation of biochar effects on nitrogen retention and leaching in multi-layered soil columns [J].Water, Air, and Soil Pollution, 2010,213(1-4):47-55.[10] Zhang G X, Zhang Q, Sun K, et al.Sorption of simazine to cornstraw biochars prepared at different pyrolytic temperatures [J].Environmentrics Pollution, 2011,159(10):2594-2601.[11] Kikuchi Y, Qian Q R, Machida M, et al.Effect of ZnO loading to activated carbon on Pb(II) adsorption from aqueous solution [J].Carbon, 2006,44(2):195-202.[12] 国家环保总局《水和废水检测分析方法》编委会.水和废水分析监测方法 [M].4版.北京:中国环境科学出版社, 2002,211-282.[13] 孙金香,王海增.废弃Mg(OH)2/AC焙烧产物对染料吸附性能研究 [J].中国环境科学,2014,34(2):390-395.[14] Shaaban A, Se S M, Dimin M F, et al.Influence of heating temperature and holdingtime on biochars derived from rubber wood sawdust via slow pyrolysis [J].Journal of Analytical and Applied Pyrolysis, 2014,107:31-39.[15] Ahmad M, Lee S S, Dou X M, et al.Effects of pyrolysis temperature on soybean stover and peanut shell-derived biochar properties and TCE adsorption in water [J].Bioresource Technology, 2012,118:536-544.[16] Singh B, Singh B P, Cowie A L.Characterisation and evaluation of biochars for their application as a soil amendment [J].Australian Journal Soil Research, 2010,48(6/7):516-525.[17] Chun Y, Sheng G Y, Chiou C T, et positions and sorptive properties of crop residue-derived chars [J].Environmental Science Technology, 2004,38(17):4649-4655. [18] 刘玉学,刘微,吴伟祥,等.土壤生物质炭环境行为与环境效应[J].应用生态学报, 2009,20(4):977-982.[19] Ding W C, Dong X L, Ime I M, et al.Pyrolytic temperatures impact lead sorption mechanisms by bagasse biochars [J].Chemosphere, 2014,105:68-74.[20] Ozlem O.Influence of pyrolysis temperature and heating rate on the production of bio-oil and char from safflower seed by pyrolysis, using a well-swept fixed-bed reactor [J].Fuel Processing Technology, 2007,88(5):523-531.[21] 王章鸿,郭海艳,沈飞,等.热解条件对生物炭性质和氮、磷吸附性能的影响 [J].环境科学学报, 2015,35(9):2805-2012.[22] 李扬.生物炭覆盖对底泥氮、磷释放的影响及其吸附性能研究 [D].青岛:中国海洋大学, 2013.[23] 张继义,韩雪,武英香,等.炭化小麦秸秆对水中氨氮吸附性能的研究 [J].安全与环境学报, 2012,12(1):32-36.[24] Wang Z H, Guo H Y, Shen F, et al.Biochar produced from oak sawdust by Lanthanum (La)-involved pyrolysis for adsorption of ammonium (NH4+), nitrate (NO3−), and phosphate (PO43−) [J].[25] Kameyama K, Miyamoto T, Shiono T, et al.Influence of sugarcane bagasse-derived biochar application on nitrate leaching in calcaric dark red soil [J].Journal Environmental Quality, 2012, 41(4):1131-1137.[26] Qiu Y P, Cheng H Y, Xu C, et al.Surface characteristics of crop-residue-derived black carbon and lead (II) adsorption [J].Water Research, 2008,42(3):567-574.[27] Raji C, Anirudhan T S.Batch Cr (VI) removal by polyacrylamide-grafted sawdust: kinetics and thermodynamics [J].Water Research, 1998,32(12):3772-3780.[28] Malandrino M, Abollino O, Giacomino A, et al.Adsorption of heavy metals on vermiculite: influence of pH and organic ligands [J].Journal of Colloid and Interface Science, 2006,299(2):537-546.[29] 高淑玲,杨翠玲,罗鑫圣,等.坡缕石黏土污泥对水相中亚甲基蓝吸附研究 [J].中国环境科学, 2014,34(1):78-84.[30] 郎印海,刘伟,王慧.生物炭对水中五氯酚的吸附性能研究[J].中国环境科学, 2014,34(8):2017-2023.[31] Surchi K M S.Agricultural wastes as low cost adsorbents for Pb removal: Kinetics, equilibrium and thermodynamics [J].International Journal of Chemistry, 2011,3(3):102-113.。

变压吸附实验报告【精品】

变压吸附实验报告【精品】

我不应把我的作品全归功于自己的智慧,还应归功于我以外向我提供素材的成千成万的事情和人物!——采于网,整于己,用于民2021年5月12日变压吸附实验报告篇一:分子筛变压吸附研究报告院级本科生科技创新项目研究报告项目名称变压制富氧分子筛延长寿命的研究立项时间XX年10月计划完成时间XX年12月项目负责人储万熠学院与班级冶金与生态工程学院冶金1302班北京科技大学教务摘要变压吸附制氧关键的因素是制氧吸附剂和制氧工艺。

制氧吸附剂的性能优劣和使用寿命直接影响产品气的氧浓度和收率,氮吸附容量是评价制氧吸附剂性能优劣的一项重要指标。

本课题首先对分子筛进行XRF分析、XRD表征和TEM表征探究分子筛的物理及化学性质,确定对分子筛造成影响的条件。

ANSYS FLUENT中的多孔介质模型可以模拟多孔介质内的流体流动、“三传一反”。

PSA空分吸附床由固体吸附剂颗粒填充而成,气-固两相区可作为多孔介质,因此可基于多孔介质模型对变压吸附空分吸附床进行模拟,从而得到床层内气体的流动状态和组分浓度分布情况。

为研究提高分子筛寿命的研究提供可靠有效的实验数据。

Research of Prolong the Life ofPressure-Swinging-Oxygen-Making Molecular SieveAbstractThe keyfactorof thepressure swinging oxygen making is oxygen adsorbentandoxygenprocess. The quality and service life of oxygen adsorbentdirect impact on the oxygenconcentrationandyield of productgas, nitrogen adsorptioncapacity ofthe oxygensorbentperformanceevaluation ofthe meritsofan important indicator.This paperfirstdo XRFanalysis, XRDand ofmolecular TEMcharacterization sieveinquiryto ofphysicalandchemicalproperties theimpact onmolecular determinesievesconditions.The porous medium model in ANSYS FLUENT can simulate fluid flow in porous media. PSA air separation adsorbent bed is filled by a solid sorbent particles, gas - solid two phase region as a porous medium, thus can simulate the pressure swing adsorption air separation adsorbent bed based on the porous medium model, resulting in the flow state within the bed of gas and component concentration distribution for providing valid and reliable experimental dataof improving molecular sieve’s life.目录1引言 (1)1.1课题研究背景 (1)1.2课题研究目的及意义 (1)2原矿矿物学分析 (2)2.1分子筛XRF分析 (2)2.2 分子筛XRD表征 (3)2.3 分子筛TEM表征 (5)2.4 分子筛孔隙率实验 (6)2.4.1 失活实验 (6)2.4.2 活化实验 (6)2.4.3 差热曲线 (7)3 ANSYS FLUENT模拟 (8)3.1 模型建立 (8)3.2 模拟结果 (11) (11)3.2.2 速度云图.........................................................................113.2.3 温度云图.........................................................................124 FLUENT模拟结论 (12)参考文献 (12)1 引言1.1 课题研究背景变压吸附制氧关键的因素是制氧吸附剂和制氧工艺。

The Principles of Adsorption

The Principles of Adsorption

The Principles of AdsorptionAdsorption is a critical process in many industries, from water purification to pharmaceuticals and beyond. In essence, it involves the attraction of molecules or particles to a surface or interface. Understanding the principles of adsorption is essential to optimizing these processes and achieving desired results.First, it is essential to understand the various types of adsorption. There are two main types: physical adsorption and chemical adsorption. Physical adsorption involves the attraction of molecules to a surface through van der Waals forces, while chemical adsorption involves a more significant interaction, with the formation of chemical bonds between the surface and adsorbing species.The strength of adsorption is determined by several factors, including temperature, pressure, and the nature of the adsorbent and adsorbate. The higher the temperature and pressure, the more significant the adsorption, but at some point, saturation can occur, and further adsorption becomes impossible. The nature of the adsorbent and adsorbate is also crucial. For example, an adsorbent with a high specific surface area will have a more significant capacity for adsorption, while a polar adsorbate will be more attracted to a polar surface.In addition to these factors, the kinetics of adsorption must also be considered. The rate of adsorption depends on the concentration of the adsorbate at the interface, the surface area of the adsorbent, and the mass transfer rate of the adsorbate to the interface.The principles of adsorption are applied in various ways in different industries. In water purification, activated carbon is used as an adsorbent to remove impurities such as chlorine and pesticides from drinking water. In the pharmaceutical industry, adsorption is used in the purification of drugs and the removal of impurities or contaminants. In the oil and gas industry, adsorption is utilized in processes such as natural gas purification and carbon dioxide capture.One area of particular interest in adsorption research is the development of new materials with improved adsorption properties. For example, graphene and other two-dimensional materials have been shown to have excellent adsorption capacity due to their high surface area. Metal-organic frameworks (MOFs) are also promising materials, with a high degree of tunability and the ability to target specific species for adsorption.In conclusion, understanding the principles of adsorption is essential for optimizing processes and achieving desired results in various industries. Factors such as temperature, pressure, the nature of the adsorbent and adsorbate, and the kinetics of adsorption all contribute to the strength and capacity of adsorption. Continued research and development of new materials with improved adsorption properties will further enhance the applications and effectiveness of this critical process.。

可调氧浓度的制氧方法

可调氧浓度的制氧方法

可调氧浓度的制氧方法There are various methods for adjustable oxygen concentration, such as pressure swing adsorption (PSA), vacuum swing adsorption (VSA), and membrane separation. Among the first two methods, PSA is the most commonly used one. It functions based on the adsorption of gas molecules on the surface of solid materials such as zeolite. The difference in adsorption capacity between nitrogen and oxygen enables the separation of the two gases, resulting in oxygen with a higher concentration.可调氧浓度的制氧方法有许多种,例如压力摆动吸附(PSA)、真空摆动吸附(VSA)和膜分离。

在前两种方法中,PSA是最常用的。

它是基于气体分子在沸石等固体材料表面的吸附作用来实现的。

氮气和氧气吸附能力的差异使得这两种气体得以分离,从而产生浓度较高的氧气。

In recent years, membrane separation technology has gained attention for its ability to produce high-purity oxygen. It involves the use of semi-permeable membranes to separate the components of air based on their differing ability to pass through the membrane. This method has the advantage of being energy-efficient and easy tooperate, making it a promising option for adjustable oxygen concentration.近年来,膜分离技术因其生产高纯度氧气的能力而受到关注。

PPB级高纯氮生产的工艺设计及其技术特点分析

PPB级高纯氮生产的工艺设计及其技术特点分析
装置能耗和增加装置可靠性。
1 工艺设计及流程
1. 1 吸附装置
如图 1 所示为适用于 PPB 级高纯氮生产的吸附装置 100,
包括吸附桶 101、 连通于吸附桶 101 底部的气体入口 102 以及
连通于吸附桶 101 顶部的气体出口 103。 气体入口 102 与气体
出口 103 之间设有用于吸附脱除 H2 O 的第一吸附层 104、 用于
中的 H2 O 杂质、 CO 杂质、 CO2 杂质, 而无需安装后纯化器进
行再次纯化。
通过阀门切换系统 300 的设置可实现吸附和解吸之间相互
切换, 吸附装置 100 用于吸附空气中的 H2 O、 CO 及 CO2 , 而解
吸装置 200 用于解除活性氧化铝、 锰铜催化剂、 分子筛的吸附
作用, 保持性氧化铝、 锰铜催化剂、 分子筛这些吸附料的吸附
纯气体的需求越来越多, 高纯氮气在电子、 多晶硅等行业的应
用越来越广泛 [1-3] 。 经过 30 多年的发展, 我国的高纯氮气生产
技术日趋成熟, 正朝着工艺形式多样化的方向发展。 从最初传
统的单塔精馏制氮工艺到目前冷凝较多的双塔精馏制氮工艺,
蒸发器制氮工艺有了巨大的飞跃 [4] 。 制取氮气的基本方法是将
关键词: 高纯氮; 冷冻制氮; 吸附; 纯化; 工艺设计
中图分类号: TQ171
文献标志码: B
文章编号: 1001-9677(2021)010-0137-03
Process Design and Technical Characteristics Analysis of PPB
Grade High -purity Nitrogen Production
均连接有气体放空口。 运作时可通过设置阀门的数量和位置控
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Received September 22, 1975, accepted March 13, 1976 Saran carbon adsorbs more N2 than Oz at 25°C due to stronger interaction of the larger nitrogen molecule with adsorbent pore walls. Exchange of H ions on carboxylic acid groups located on the surface of oxidized Saran carbons and Carbolac-1 by calcium ions increases the extent of chemisorption of 02 and physisorption of N~, if the carbons are outgassed to at least 180°C. The higher uptake of Nz has been attributed to interaction of the nitrogen quadrupole moment with the electrostatic field gradient. It is suggested that the chemisorption of oxygen on the Ca-exchanged carbons is due to carbanion formation upon decarboxylation of the calcium salt of surface carboxylic acid groups. The addition of large amounts of chlorine to Saran carbon has a negligible effect on the ratio of N2 to O3 which is adsorbed. I. INTRODUCTION
III. RESULTS AND DISCUSSION
' S(900°C) S(CO2-19.6) S(COs-38.3) S (CO2-60.4) S (air-48.6) S (air-63.8) Carbolac-1 Graphon
about 9: 1) in an argon atmosphere. The heating cycle was: a heating rate of 100°C/hr to 350°C, hold at 350°C for 2 hr, a heating rate of 200°C/hr to 900°C, and hold at 900°C for 4 hr. Saran carbon was activated to various levels of burn-off in air at 450°C and in CO2 at 800°C. The experimental details of pyrolysis and activation have been described elsewhere (6).
Adsorption of Oxygen and Nitrogen on Surface-Modified Carbons
P. EHRBURGER, 1 0 . P. MAHAJAN, AND P. L. WALKER, JR.
Department of Material Sciences, The Pennsylvania State University, University Park, Pennsylvania 16802
1 Permanent address: Centre De Recherches Sur La Physico Chimie Des Surfaces Solides, 68200 Mulhouse, France.
on nonionic solids, but in the case of ionic solids the heat of adsorption of N2 is higher. He has suggested that this may be due to the larger quadrupole moment of N2 compared to that of 02. Huang and Emmett (5) observed that the adsorption of molecules having high quadrupole moments is increased on cationexchanged silica-alumina. Carbons possess high surface reactivity and it is possible to change their surface polarity by fixing dipole groups like C-C1 or by cation exchange of surface carboxylic protons. It would be desirable to investigate if adsorption of N2 on high surface area adsorbent carbons can be enhanced by interaction of the nitrogen quadrupole moment with the deliberately introduced surface dipoles or surface electrostatic field potential. The present paper is an attempt in this direction.
Adsorption isotherms of N2 and 02 on unactivated Saran carbon and Carbolac-1 are shown in Fig. 1. The isotherms are linear and reversible over the entire pressure range studied. Volumes of N2 and 02 adsorbed on various samples at 600 Torr are given in Table I. Experimental uncertainty in amounts adsorbed was 4-0.1 cm3/g. Saran samples (S)
Physical adsorption on carbon surfaces has been used extensively for purification and separation of various gases (1, 2). Since there is an increasing demand for oxygen in different technological processes, attempts have recently been made to separate oxygen from air by selective adsorption on carbons having high specific surface areas. Nandi and Walker (3) have shown that certain microporous carbons exhibit molecular sieving properties towards 02 and N2, resulting in selective oxygen adsorption from air. These workers also observed that carbons having vinylidene chloride as their main organic precursor had a greater uptake of N2 than 02 at room temperature. Since the kinetic diameter of N2 is larger than that of 02 (3.64 and 3.46A, respectively), these results cannot be explained in terms of molecular sieving but rather by specificity in physical adsorption. Specific interactions due to electrostatic forces between various adsorbates and solid surfaces have been reported in the literature (2). Drain (4) has shown that both 02 and N2 have similar heats of adsorption
II. EXPERIMENTAL
A. Materials
Saran carbon and Carbolac-1, a highly oxidized channel black manufactured by Cabot Corporation, were used as adsorbents. Saran carbon was prepared by the pyrolysis of Saran (a copolymer of PVD C and PVC in a ratio of
samples was determined gravimetrically as calcium oxide by burning the sample at 950°C.
C. Adsorption Isotherms
Adsorption of 02 and N2 was measured at 25°C in a conventional volumetric apparatus. Before making an adsorption run, the sample was normally outgassed overnight at 120°C. Thirty minutes was allowed for each adsorption point, with equilibrium reached within this time period. All adsorption volumes given in the paper are reported at STP conditions.
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