泰山会文档
泰山会
最近，联想集团陷入舆论风波，先是在5月4日被宣布将从“恒生指数50只成分股”中剔除，紧接着又受到2年前5G编码标准投票不支持华为的“卖国”指责。
创始人柳传志5月16日发声，“行动起来，誓死打赢联想荣誉保卫战”。
不得不说，柳传志的能量巨大，俨然一个“带头大哥”。
在他发声后，包括马云、李彦宏、刘强东和雷军等百位企业家力挺支持，甚至连微博上沉寂两个多月的贾跃亭也跳出来声援支持。
在这些商界大佬的背后，有一个共同的圈子——泰山会。
企业家的“小圈子”不小在商业领域里，企业家圈子普遍存在。
无论是校友会、商会，还是俱乐部、会所，基于圈子这一平台，圈子成员或公开或私下联系、走动，即使有的不是以商业利益为出发点，但在交流感情的过程中，也能更全面了解各方动态，寻找商机、投资与合作，抱团取暖，在有需要的时候获得帮助，实现自身利益最大化。
看过《窃听风云2》的朋友，一定会对里面提到的地主会有深刻的印象，这是一群喜欢打牌的香港富豪组成的，他们几乎控制了半个香港的股市，可以任意操纵股票。
其实这个地主会是有雏形的，就是现实中的大D会。
最早的时候，李嘉诚、李兆基、郑裕彤、还有何鸿燊，几个华人世界顶级富豪，是香港澳门固定的牌友，经常在一起打一种广东的纸牌，名为锄大地。
不过后来年纪大了，加上事业各自发展，都是雄霸一方的诸侯。
在内地，也有不少。
比如江南会，以马云为首，还有冯根生、郭广昌、沈国军、卢伟鼎等人。
还有柳传志的泰山会，当年史玉柱出事后，就是泰山会的柳传志、段永基等人帮他东山再起的。
除了华夏同学会、泰山会、江南会，还有正和岛、阿拉善SEE生态协会、长安俱乐部、金鼎俱乐部、亚布力论坛、中国金融博物馆书院、欧美博士团、接力中国、地方商帮等也汇聚了一批中国优秀的商业精英。
当然，商界中也有可以远离各个圈子的大佬，比如宗庆后，从不加入任何企业家的圈子，亦不与任何一个企业家交往甚密。
他认为，“大家还是‘君子之交淡如水’比较好。
”企业家圈子就是生产力有人的地方就有江湖，有江湖的地方就有圈。
泰山论坛项目 文档
泰山世界文化论坛可行性方案目录第一章总论 (2)第一节企业概况 (2)第二节项目概况 (2)第二章项目提出的背景及建设的必要性 (9)第一节山东省及泰安市概况 (9)第二节项目提出的背景 (14)第三节项目提出的必要性 (23)第三章项目建设规模及内容（附图1） (32)第四章用地情况分析 (32)第一节项目选址区域（附图2） .............. 错误！未定义书签。
第二节项目用地情况 ................................. 错误！未定义书签。
第三节地上附属物补偿情况 ..................... 错误！未定义书签。
第五章组织机构与人力资源配置 (32)第一节组织机构 (32)第二节劳动定员 (33)第三节员工来源 (34)第六章建设实施及工程进度安排 (34)第七章投资估算及资金筹措 (35)第八章社会效益分析 (36)第一章总论第一节企业概况1、企业名称：山东泰山影视传媒有限公司2、注册资本：500万元3、法定代表人：王丰4、公司地址：泰安市东岳大街西段泰安市工商局三楼5、单位概况山东泰山影视传媒有限公司成立于2010年10月，公司主要从事文化艺术交流与策划、企业形象策划推广、电影电视片拍摄制作、设计制作发布国内各类广告，公司现有员工50人，设有策划部、产品研发部、摄制部、制片部、营销部、动漫部等部室。
第二节项目概况一、项目背景改革开放30年来，中国文化市场以‚一手抓繁荣，一手抓管理‛的方针为指引，基本形成了由娱乐市场、演出市场、音像市场、电影市场、网络文化市场、艺术品市场等组成的统一、开放、竞争、有序的文化市场体系。
目前，文化产业成为我国经济新增长点的态势愈加明显，其在转变经济发展方式、调整国民经济结构中发挥的作用在更大范围内获得了认可。
2009年9月26日，新中国首部《文化产业振兴规划》出台，它是指导我国文化产业发展的纲领性文件。
它的发布，表明文化产业作为国民经济新的重要增长点，已经上升到国家战略层面，标志着文化产业发展进入了一个新的阶段。
泰山会：神秘低调的富豪俱乐部Microsoft Word 97 - 2003 文档
泰山会：神秘低调的富豪俱乐部泰山会（曾用名：泰山产业研究院），成立于1993年，由于成立大会在山东召开，遂取名“泰山”，是由中国民营科技实业家协会主管的非独立法人机构。
它由中国知名且有相当影响力企业的CEO（或董事长）组成，每年只发展1家会员单位。
会员单位包括联想控股、四通集团、泛海集团、远大集团、复星集团、巨人集团等15家，联想控股总裁柳传志亲任会长，段永基任理事长，顾问吴敬琏、胡德平。
泰山会是中国最知名、最神秘的大型商会之一。
2005年，泰山产业研究院核心人物华怡芳去世，研究院遂改名为泰山会。
之后，其组织形式更加私人化，不再设分会，也取消了内刊。
柳传志在一次采访中曾提到：（泰山会）以联谊为主，缺席要交请假费，第一次一万，第二次二十万，“连续请假的以马云居多”，至于活动内容，他透露，“泰山会不谈任何企业经营和行业情况，只谈国家大形势。
”泰山会阵容“对于民营企业家而言，泰山会绝对是一个超豪华阵容。
”泰山会成员：会长柳传志，理事长段永基，会员：万通集团冯仑、泛海集团卢志强、阿里巴巴马云、复星集团郭广昌、远大空调张跃、信远控股林荣强、巨人集团史玉柱、百度李彦宏、段永平、中关村科海集团陈庆振、江西科端集团郑跃文、河南思达集团汪思远、横店集团徐文荣、和光集团吴力、华谊兄弟王中军。
顾问：吴敬琏、胡德平。
个个名列内地百大富豪，所拥有的事业总资产，比台湾地方政府总预算还多好十几倍，掌握的财富超过百兆新台币(1新台币约合0.2元人民币)，事业版图横跨高科技、地产、金融、娱乐各产业，对中国、甚至全世界经济，有呼风唤雨的影响力。
泰山会挂靠于中国民营科技实业家协会(以下简称中民协)，中民协现任副秘书长朱希铎曾任四通集团副总裁，他告诉《中国周刊》记者，“‘泰山’成立十多年，会员几乎没有变过。
”泰山会成立于1993年，由于成立大会在山东召开，遂取名“泰山”。
此外，会员们也认为，“五岳至尊”的泰山寓意一种高度，以泰山取名，也代表中国民营企业家的高度。
泰山国际登山节与中国泰安投资合作洽谈会(10页)
第二十二届泰山国际登山节暨2008中国泰安投资合作洽谈会总体方案（2008年7月29日市政府常务会议、2008年7月30日市委常委会议研究通过）为做好第二十二届泰山国际登山节暨2008中国泰安投资合作洽谈会的各项筹备及组织工作，特制订本方案。
一、指导思想按照构建大泰山旅游圈、创建国际旅游名城、建设旅游经济强市以及建设富裕文明和谐泰安的总体目标要求，以文化建设为切入点，继续解放思想，推进科学发展，努力拓展外向型经济发展空间，积极构筑奥运主题体育大舞台，不断开发国际旅游新品牌，促进全市经济社会又好又快、更好更快发展。
二、名称、时间和地点（一）名称：第二十二届泰山国际登山节暨2008中国泰安投资合作洽谈会。
（二）时间：2008年9月6日至12日。
（三）地点：泰安市。
三、举办单位（一）主办单位：国家旅游局、中华全国体育总会、中国登山协会、中国国际贸易促进委员会、中华全国工商业联合会、中国人民对外友好协会、中央电视台、中国国际广播电台、山东省旅游局、山东省体育局、山东电视台、泰安市人民政府。
（二）承办单位：泰安市人民政府。
四、活动内容本届泰山国际登山节共安排文化、经贸、体育和旅游4大类、7项主题活动。
1、第二十二届泰山国际登山节（泰山·富士山中日友好节）开幕式暨吕远作品演唱会。
（1）时间：9月6日。
（2）地点：天地广场。
（3）活动安排：一是举行开幕仪式；二是举办吕远作品演唱会，由中日两国著名音乐家同台演唱吕远先生系列音乐作品，国内知名歌唱演员及日本演员参加演出。
邀请日本国会议员团和日本友好人士、游客出席开幕仪式和吕远作品演唱会，积极拓展日本客源市场。
（4）承办单位：中央电视台，山东电视台，日本静冈县政府、山梨县政府和富士山协会，北京亚细亚体育文化交流中心，市委宣传部、市旅游局、泰山管委、市公安局、市广播电视局、市卫生局、市建设局、市体育局、市安全监管局、市气象局、市教育局、市招商办、市外经贸局、市台办、市文化局、市接待处、市外办、泰安供电公司等，市旅游局牵头。
泰山导游词范文.doc
泰山导游词范文泰山是中华民族的象征，是灿烂东方文化的缩影，有“五岳之首”、“五岳之长”、“天下第一山”之称。
接下来，我将带领大家在泰山的导游词里一起欣赏泰山的壮丽。
篇一：泰山导游词各位游客，大家早上好，我姓杨，你们叫我杨导就可以了。
本次旅游我们要去登泰山，全程由我来带领大家参观游览，如果大家有什么疑问，大家可以来问我，我尽量帮大家解决。
同时，请爱护景区环境卫生，每个景点我都给大家留够了参观拍照的时间，请大家自觉遵守时间，以免影响后面的一些参观行程。
在到达泰山景区之前，我先给大家对泰山做一个介绍。
泰山位于山东省泰安市，是我国的“五岳之首”，是中华民族的一个伟大的象征，是东方文化世界的缩影，是“天人合一”的寄托之地。
在一九八七年被列入了世界自然文化双重遗产的目录。
泰山自古以来就被看做是国家稳定，民族团结的一个象征。
历朝历代，无论谁当上了黄帝，第一件事就是朝拜泰山。
先后有十二位黄帝来到了泰山封禅。
泰山因此也就成为了我国唯一一座受过黄帝封禅的名山，无论是谁，都对泰山是仰慕备至，孔子和杜甫先后都登过泰山，还留下了一些千古绝句。
现在，我们已经到了泰山脚下，大家向山顶上看，那个红色的建筑就是南天门，位于泰山十八盘的尽头，又名三天门，海拔一千四百六十米，故称天门关。
等一会，无论是坐缆车的还是徒步登山的，我们都将在那里会合。
泰山主要的景点有：百丈崖、望人松、云桥飞瀑、十八盘等。
其中十八盘是登山路中最险要的一段，你能想象吗?它有石阶一千六百余阶，你们顺着我手指的方向看，它像不像一条在崇山峻岭之间的一条灰色的长龙!好了，话不多说，我们一起向上爬，看看谁最先到达山顶，体验“会当凌绝顶，一览众山小。
”的感觉。
现在，我们已经到达了泰山之顶，玉皇顶。
玉皇顶旧称太平顶，又叫做天烛峰，海拔为一千五百四十五米，在我们身旁这座红颜色的庙宇，我们叫它玉皇庙，故称太清宫。
庙内主要建筑有玉皇殿、迎旭亭等，始建年代已不详。
在玉皇顶上看日出，可是绝佳之地。
泰山会
圈子以及后代
今年初，10多个80后的富豪组织了“80后企业家俱乐部”，经常聚集在一起，谈宝马、谈爱好、谈困惑、谈管理。这些孩子，他们在办公室里面需要面对着很多年长的同事，只能谈工作；而与他们同龄的人还在为找一份工作和挣多少钱奔忙。所以，他们只能自己找“圈”。
三年后，巨人公司无法还本，更不要说付息。造成无数家庭妻离子散，家破人亡。数千被诈骗了血汗钱的老百姓到北京找《中国人民保险公司》要求赔偿，《中国人民保险公司》才知道史玉柱竟然胆大包天地伪造《中国人民保险公司》的保函，赤裸裸地欺骗出钱的老百姓。
《中国人民保险公司》把这个情况立即举报到了公安部，国务院。别的不用说，仅仅伪造《中国人民保险公司》的保函一项金融诈骗罪行，史玉柱就得被以法枪决。
，硕士，中关村科技发展(控股)股份有限公司总裁
1970年毕业于清华大学后在北京市176中学任教。
1979年重返校园，获北京航空学院硕士学位。
1982年在中国航空材料研究中心任研究室副主任。
1985年，正式加入四通公司，历任副总经理兼OA部部长、副总裁等职。
1991年至1999年9月，担任四通集团总裁。
下面补充：
直在想，近十年来，中国互联网比较成功，30、40岁的CEO们，跟老一辈的企业家，任正非，柳传志、段永基相比怎么样。
昨夜看完李玉琢写的《我与商业领袖的合作与冲突》，李先后曾经是段永基、任正非的副总裁，左膀右臂之一，写了不少段永基、任正非为人处事的态度和方法。
任正非曾将叛逃到UT斯达康的“沪科”公司几个人送进了监狱，将叛逃的李一男打到投降被收购。
泰山会
马太效应套在当下风头正劲的乐视身上一点都不为过。
仅最近几天，就有两大新闻加诸乐视身上，前者是乐视收购亚马逊中国的消息，后者是乐视超级汽车创纪录的完成10.8亿美元首轮融资，只是前者消息被双方均否认了，后者消息却是由乐视创始人兼董事长、乐视控股CEO贾跃亭登台亲自说出。
《证券日报》记者得到一份首轮投资者名单，包括国家电网旗下英大资本、深圳市政府投资平台深创投、联想控股、民生信托、新华联以及宏兆基金等知名机构都参与到了乐视超级汽车的首轮融资中，仅名单中的这六家机构目前资产管理总额已达数千亿元。
有接近乐视超级汽车的人士向记者透露，包括齐鲁证券在内的多家机构曾有意投资乐视汽车，经过数月遴选，乐视汽车首轮投资者名单才最终确定。
尤为引人注目的是，六家投资机构实际掌控人有3人都是“泰山会”的成员，而宏兆集团董事长姚其湧以及银泰集团董事长沈国军，尽管不是“泰山会”的成员，同样与上述几位大佬非常熟悉。
与其他互联网车企引资来者不拒不同，乐视汽车选择投资人更看重其背后所拥有的“资源”。
比如英大资本背后是国家电网，能为乐视汽车提供建设充电桩等便利条件；新华联在地产方面的优势，则可为乐视汽车落地销售等提供便利。
上述不愿具名的人士表示，乐视超级汽车首轮融资的最重要逻辑——站在生态角度，不止引入资本，还要引入全方位产业资源，通过生态模式“破界化反”，实现全新价值创造。
汽车业最大一笔首轮融资9月19日，在“919乐迷狂欢夜”晚会上，向来重视体验营销的贾跃亭又有了惊人之举，他向“国民英雄”郎平赠送了一台价值超过百万的、由战略合作伙伴Faraday Future（FF）打造的首款互联电动智能超豪华跨界车。
随后，他正式对外宣布，乐视汽车已完成首轮10.8亿美元融资，这一数字也刷新了全球汽车产业的首轮融资纪录。
对于一直以来处于风口浪尖的乐视超级汽车来说，首轮巨额融资的落地，无疑意义重大。
一方面，乐视汽车有力回击了部分舆论对其“PPT造车”的评价；另一方面，10.8亿美元彻底打消了外界对乐视造车资金链的质疑。
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Full paper /Me´moire Characterization and reactivity of WO 3e V 2O 5supported on sulfatedtitanium pillared clay catalysts for the SCR-NO reactionLilia Khalfallah Boudali a ,*,Abdelhamid Ghorbel a ,Paul Grange baLaboratoire de chimie des mate ´riaux et catalyse,de ´partement de chimie,faculte ´des sciences de Tunis,campus universitaire,1060Tunis,TunisiabUnite ´de catalyse et chimie des mate ´riaux divise ´s,Universite ´Catholique de Louvain,place croix du sud 2/17,1348Louvain-La-Neuve,BelgiumReceived 2May 2008;accepted after revision 17November 2008Available online 31December 2008AbstractVanadia and tungsten oxides supported on sulfated Titanium pillared clay were prepared and characterized by N 2physisorption,XRD,XPS,NH 3-TPD and H 2-TPR measurements.The effect of vanadium and tungsten oxides on the catalytic activity of sulfated Ti-pillared clay (STi-PILC)for NO reduction by ammonia was examined.Based on the temperature-programmed reduction,it wasfound that the sulfate stability depends on the loaded metal oxides and the reduction properties of SO 42Àor V 2O 5in the sample were changed in the presence of WO 3.The difference in reduction properties of sulfate strongly suggests some interaction of sulfate with tungsten and vanadia species on the surface of STi-PILC support.Vanadia enhanced the NO removal activity of STi-PILC,while no significant effect of tungsten was observed for WO 3e V 2O 5/STi-PILC catalyst.When both tungsten and sulfate exist simultaneously on the surface of vanadia supported STi-PILC,the sulfate species seems to play a more important role for NO removal activity than tungsten.To cite this article:L.Khalfallah Boudali et al.,C.R.Chimie 12(2009).Ó2008Acade ´mie des sciences.Published by Elsevier Masson SAS.All rights reserved.Re´sume ´Des catalyseurs a`base d’oxydes de vanadium et de tungsten supporte ´s sur des montmorillonites a `piliers de titane sulfate ´ont e ´te ´synthe´tise ´s et caracte ´rise ´s au moyen de techniques d’adsorption de ´sorption de N 2,XRD,XPS,NH 3-TPD et H 2-TPR.L’effet du vanadium et du tungsten sur l’activite´catalytique de la montmorillonite a `piliers de titane sulfate ´dans la re ´duction catalytique se´lective (SCR)de NO par l’ammoniac a e ´te ´e ´tudie ´.Il a e ´te ´montre ´par une e ´tude de re ´duction en tempe ´rature programme ´e par l’hydroge`ne que le vanadium influence la stabilite ´des sulfates et qu’en pre ´sence de WO 3les proprie ´te ´s redox de SO 42Àou de V 2O 5ont change´.La diffe ´rence dans les proprie ´te ´s redox des sulfates et du vanadium apre `s l’ajout du tungsten sugge `re une forte interaction entre les groupements sulfates,le vanadium et le tungsten a`la surface du catalyseur.Le vanadium accroıˆt l’activite ´catalytique de la montmorillonite a`piliers de titane sulfate ´a `toute tempe ´rature de re ´action.En revanche l’effet promoteur du tungsten n’a pas e´te ´observe ´dans le catalyseur au vanadium supporte ´sur la montmorillonite a `piliers de titane sulfate ´.Il semble que *Corresponding author.E-mail address:lilia.khalboudali@fst.rnu.tn (L.Khalfallah Boudali).1631-0748/$-see front matter Ó2008Acade´mie des sciences.Published by Elsevier Masson SAS.All rights reserved.doi:10.1016/j.crci.2008.11.005Available online at C.R.Chimie 12(2009)779e786/direct/CRAS2C/lorsque le tungsten et les sulfates coexistent a`la surface du catalyseur,les sulfates jouent un roˆle de´terminant dans l’activite´catalytique par comparaison au tungsten.Pour citer cet article:L.Khalfallah Boudali et al.,C.R.Chimie12(2009).Ó2008Acade´mie des sciences.Published by Elsevier Masson SAS.All rights reserved.Keywords:WO3;V2O5;Sulfated Ti-pillared clay;Acid and red-ox sites;SCR-NO1.IntroductionNitric oxide(NO)produced by combustion engines, chemical industrial plants and stationary power stations contribute to different atmospheric pollution phenomena such as photochemical smog,acid rains, stratospheric ozone depletion and human health.In recent years,great research efforts have been applied to limit the emission of NO.It is well known that the selective catalytic reduction(SCR)of NO by ammonia is the world-wide used method of removing NO from stationary sources of power plants due to its efficiency and selectivity.A variety of catalysts have been developed and applied in industrial plants in order to reduce nitric oxide by ammonia to nitrogen.Excellent summaries about these studies can be found in Refs. [1,2].In the SCR reaction,it is certain that both acidity and red-ox properties of catalysts are the controlling factors of the reactivity[3].Catalytic tests performed with various oxide cata-lysts for SCR-NO with NH3indicated that TiO2is one of the successful supports for vanadium oxide[4]. Among the large number of catalysts active in SCR-NO,the V2O5/TiO2is one of the most effective ones to achieve high activity and selectivity in an appropriate temperature window.In addition,a promoter such as WO3has been generally employed in relatively large amounts(9e10wt.%)to enhance surface acidity and the NO removal activity[5].The industrial catalysts are constituted by V2O5e WO3/TiO2or V2O5e MoO3/ TiO2monoliths;TiO2in the anatase form supports a‘‘monolayer’’of V2O5and WO3(or MoO3)deposed by impregnation.In general,the overall surface areas of the catalysts are50e100m2/g,with V2O5contents of0.5e3wt.%and WO3or MoO3contents of8e 12wt.%Typical reaction temperature(operated generally in SCR plants)is around350 C[6]. Recently,it was shown that the commercial catalyst lifetime can be prolonged by sulfation with SO2or H2SO4,the improved activity of commercial catalyst is related to the formation of new sulfate groups on the surface[7,8].The Pillared clays(PILCs)represent a convenient source to prepare catalysts because of their low cost, high surface area and porosity,thermal stability and acidity.The number of chemical reactions for which the potential application of pillared clays,whether as catalysts or as catalyst supports,has been evaluated and is continuously increasing[9].The use of pillared clays in catalytic reactions is reviewed,which emphasis on the possibilities offered from these cata-lysts to develop new processes for environmental protection,selective oxidation and refinery/biorefinery [10].It is well known that TiO2has a lower surface area and sinters more easily than Titanium pillared clay (Ti-PILC).It is also known that pure TiO2anatase does not carry Bronsted acidity,while Titanium pillared clays do.The weak Bronsted acid sites arise from structural hydroxyl groups of the clay layers.Nowa-days,there is no doubt that the Bronsted acid sites are the active centers for the SCR-NO reaction.Therefore considerable effort has been made to investigate Ti-PILC and their SCR behavior.Recently,many studies showed that Ti-Pillared clays used as support for vanadium were found as excellent catalysts for SCR-NO by NH3[11e14].It was shown that V2O5/Ti-PILC exhibited superior performance as a novel SCR-NO catalyst compared to conventional catalysts including V2O5/TiO2and V2O5/Al2O3[15].It was also proved that the SCR activity on V2O5e WO3/TiO2-PILC was higher than that on V2O5/TiO2-PILC which were highly active than V2O5e WO3/TiO2and V2O5/TiO2, respectively;especially at higher temperature[12].More recently we have shown that the addition of sulfate to Ti-PILC increased Bronsted acidity and also significantly the SCR-NO activity which was associated with the strength of surface Bronsted acidity[16].Our results strongly support that the high catalytic activity for SCR-NO process on sulphated Ti-pillared clay(STi-PILC)is directly related to the extent of sulfation.We have also reported that vanadia supported on sulphated Ti-pillared clay(V2O5/STi-PILC)was more active than vanadia supported non-sulphated Ti-pillared clay (V2O5/Ti-PILC)which was more active than STi-PILC [13].In this work,the objective was to elucidate the role of WO3on V2O5/STi-PILC.The textural,acid and red-ox properties of the catalysts have been evaluated.The WO3e V2O5/STi-PILC catalysts were tested for SCR-NO reaction and compared to V2O5/STi-PILC having the same vanadia loading.780L.Khalfallah Boudali et al./C.R.Chimie12(2009)779e7862.Experimental2.1.Catalysts preparation2.1.1.Sulfated Ti-pillared montmorillonite(STi-PILC)The initial material used for intercalation was a volclay Naþ-montmorillonite from CECA.The pil-laring solution was obtained by slowly adding TiCl4 into a H2SO4solution(3M)under vigorous stirring. Final concentration of0.82M in titanium and0.2M in H2SO4were reached by adding water,an Hþ/Ti value of0.24was thus obtained.The fresh pillaring solution was then added drop wise to500mL of a suspension containing2g of clay to obtain sulphated Titanium pillared clay(STi-PILC),in such quantities that the final Ti/clay ratio of10mmol/g was obtained[16]. After24h of stirring,the solid fraction was separated by centrifugation,then washed several times with distilled water and dried at room temperature.2.1.2.Vanadia supported by STi-PILCThe vanadia solution and the V2O5/STi-PILC cata-lyst were prepared at room temperature,as reported in Ref.[13].2.1.3.Tungsten and vanadia supported by STi-PILCThe tungsten and vanadium solution was prepared at room temperature by dissolving ammonium meta-tungstate(NH4)6H2W12O40and ammonia vanadate NH4VO3in water acidified by oxalic acid.Tungsten and vanadium supported by STi-PILC,containing 9wt.%of tungsten and3wt.%of vanadium were prepared at room temperature under vigorous stirring by incipient wetness impregnation of the sulphated Ti-PILC with the tungsten and vanadium solution.All the samples were then dried at80 C for20h and calcined at400 C for3h underflow of air.The temperature was raised at the rate of1 C/min up to400 C, maintained for3h.2.2.Characterization of the catalystsChemical compositions were determined by anal-ysis of the solutions obtained by attack of the solids by a mixture of concentratedfluorhydric and perchloric acid,then by nitric acid.Na content was obtained by atomic absorption,Ti content by colorimetry and S by gravimetry.The specific surface areas,pore and micropore volumes of the samples were determined by nitrogen physisorption atÀ196 C using a Micromeritics ASAP 2000instrument.The samples were out gassed in vacuum during5h at200 C prior to nitrogen physisorption.The X-ray diffraction patterns were recorded on a CGR theta60instrument using monochromatized CuK a radiation at l¼1.54A˚.The position of the d001 line in X-ray diffraction gave the interlayer distance and consequently the pillar height.The X-ray photoelectron spectra(XPS)were per-formed at room temperature with a Surface Science Instruments SSX-100model206spectrometer with a monochromatised AlK a source,operating at10kV and12mA.Samples calcined at400 C for3h were compressed in a small cup under a5kg/cm2pressure for30s and supported on a holding carousel.The binding energies(BE)of W4f,V2p,S2p and Ti2p lines were referenced to the C1s band at284.8eV.Temperature-programmed desorption of ammonia (NH3-TPD)was performed in a micro-reactor system with an on-line mass spectrometer(GC e MS)to examine the surface acidity of the catalysts.In each experiment and before adsorption of ammonia a sample weight about0.150g calcined and at400 C was placed in the cell,evacuated at400 C for2h under aflow of helium and then cooled to ambient temperature.Pure ammonia gas(50mL/min)was adsorbed at100 C for 20min.Then after sweeping NH3by He(50mL/min) and stabilization of the base line of the detector,the temperature was progressively increased up to400 C at a constant rate of10 C/min.The desorbed NH3amount was collected and trapped in a boric acid solution(20g/ L),then titrated by sulphuric acid(5Â10À3M)for quantitative determination.Temperature programmed H2-TPR was performed to examine the redox ability of the catalyst.TPR was measured by monitoring hydrogen consumption from a hydrogen dilute in inert gas mixture(5%H2/He) while increasing the temperature of sample at a constant rate10 C/min and maintaining a constant flow rate(60mL/min).The inlet and outlet gas composition were measured using a quadrupole mass spectrometer QMC311Balzers coupled to the system.2.3.Catalytic activity measurementThe SCR experiments were carried out in a tubular continuous-flowfixed-bed reactor between100and 400 C operating under atmospheric pressure,with a GHSV46.000hÀ1.The totalflow rate was controlled byflow meter(100mL/min).The gas mixture was:NO (0.1vol.%),NH3(0.1vol.%)and O2(2.5vol.%)in He. The catalyst amount of0.150g calcined at400 C and the space velocity were kept constant for all781L.Khalfallah Boudali et al./C.R.Chimie12(2009)779e786experiments.Each catalyst was heated for1h at 100 C under helium before adding the charge.All reported conversions were measured at steady state, under our experimental conditions,after1h at a given temperature.They were analyzed using a quadrupole mass spectrometer(QMC311Balzers).3.Results and discussion3.1.Characterization of the catalystsThe STi-PILC,used as a support for vanadia and tungsten,exhibited a high basal spacing of22A˚witha large surface area of226m2/g and pore volume of0.170cm3/g significantly higher than those of the initial clay(Naþ-Mont.)indicating a successful pil-laring process(Table1).The chemical compositions of the initial clay and the sulphated Ti-pillared clay support are also reported in Table1.The increase of TiO2and sulphur contents at the detriment of Na2O content results of pillaring and indicates the incorpo-ration of sulphated Ti-polycations between the silicate layers upon pillaring.Table2clearly shows that a significant loss of surface area and micropore volume occurs upon vanadia addition.This effect can be explained by the blocking of small pores due to the building up of the vanadia layer.The basal spacing is not significantly affected by impregnation of the support with the vanadium solution[13].When tung-sten and vanadium were deposited at the same time, the surface area also decreased as sharply as the catalyst with only vanadium.The comparison of the thermal stability of the samples was performed under similar operating conditions(Table2).For STi-PILC, the BET surface area,total pore volume and micropore volume decreased with the increase of the thermal treatment temperature but remained appreciable after calcinations at400 C.The decrease of the BET surface area is mainly due to the dehydratation and to the dehydroxylation of the Ti pillars and the sulfate species.Since microporosity is introduced by pillaring, the decrease of the micropore volume indicates a sin-tering of small pores upon calcinations.In contrast,for the samples containing vanadium and tungsten,the BET surface areas and micropore volumes increased after calcinations at400 C.This result could be explained by the structural changes occurring during the heat treatment.The dehydroxylation of vanadia and tungsten species with the increase of the calcinations temperature to400 C induces a discharge of small poresfilled with vanadium and tungsten species leading to an increase of the surface areas.For all samples,the surface areas are above150m2/g at 400 C;characterizing the thermal stability of the investigated catalysts.Table3summarizes the XPS binding energies of W, V,S and Ti present on the surface of the samples.The W4f7/2binding energy measured for the sample con-taining tungsten occurred at36.5eV and corresponds to tungsten in the6þoxidation state WO3[17].An additional BE at247.5eV was observed for W4d5/2 suggesting the existence of tungsten as W(VI)only [17].No XPS peak at32eV characteristic of metallic W was observed.The binding energy at517.1eV typical of V2p3/2was detected for all samples con-taining vanadium.The literature data show that the binding energy for V5þin V2O5is between517.4and 516.4eV,while it is between515.7and515.4eV for V4þin V2O4[17].Therefore,the observed values indicate that the vanadium is present on the surface of all catalysts investigated in the5þvalence form,as V2O5.Binding energy at near169eV was measured for the S2p[17].According to the literature data,this binding energy is typical of sulphur in the S6þoxida-tion state as in Na2SO4or Fe2(SO4)3[18].This BE was observed for all samples investigated indicating that sulphur remain in6þoxidation state,in the form of SO42À,on the surface of the catalysts after vanadium and tungsten addition.The peaks at161e162eV belonging to sulphide and at164eV to elemental sulphur were not observed.The Ti-pillared clay material showed a Ti2p binding energy values around 459eV.This suggests the presence of Ti4þ,which agrees well with the data reported in literature[17]. This similar BE identical for all the samples indicates that the Ti4þoxidation state remains unchanged before and after addition of tungsten and vanadium.Note that the intensities of the bands decreased in the case of V2p,S2p and Ti2p after W addition indicating an increasing coverage of V2O5,SO42Àand TiO2by WO3Table1Structural,textural and chemical analysis of the initial clay(Naþ-Mont.)and sulfated Ti-pillared clay(STi-PILC)support.Samples d001(A˚)S BET(m2/g)V p(cm3/g)V m p(cm3/g)Na2O(wt.%)TiO2S(wt.%)S(wt.%) Naþ-Mont.12400.0750.002 3.060.330STi-PILC222260.1700.0460.2139 1.1782L.Khalfallah Boudali et al./C.R.Chimie12(2009)779e786(data not shown).The amounts of sulphur in the Ti-pillared clay catalysts measured by the atomic surface composition evaluated as S/(Ti þV þW)atomic ratio calculated from each atomic value obtained by XPS measurements are also shown in Table 3.It is clear that the surface atomic ratio of sulphur to the sum of the cation shows a large dependency with the metal impregnation.When only vanadia was deposited,the value of S/(Ti þV þW)atomic ration decreased.It could be explained by the decrease of exposed sulphate species on the surface of the vanadia catalyst.When tungsten and vanadia were deposited at the same time,the S/(Ti þV þW)atomic ratio decreased sharply.This result could be explained by the decrease of exposed sulfate species due to the larger coverage by V 2O 5and WO 3.In conclusion,the XPS results show that the catalysts contain the mixed oxide elements in the highest oxidation state,W(VI),V(V)and Ti (IV),most probably as WO 3,V 2O 5and TiO 2with SO 42Àspecies on the surface of the pillared material catalyst.The NH 3-TPD patterns of the clay samples are shown in Fig.1.The shape of desorption pattern obtained for the STi-PILC support is very different from those recorded for the samples containing WO 3and/or V 2O 5.However,the NH 3-TPD spectra of these solids contain at least two maxima.The first peak is centered at about 230 C,while the second one,much broader,at temperature above 300 C.This ammonia desorption suggest that there are at least two distinct NH 3species adsorbed on the sulphated Ti-pillared clay surface.The low temperature peak can be related to the desorption of ammonia either physisorbed or linked to weak Bronsted acid sites,while the second peak athigh temperature can be attributed to NH 3desorbed from Lewis acid sites.It is known that the acidity of STi-PILC is essentially related to the presence of sulfate.In our previous work we have shown that the addition of sulfate to Ti-pillared clay increased significantly the total acidity and essentially the Bronsted acid sites [16,19,20].The addition of vana-dium into the STi-PILC increased the intensity of the first peak which correspond to the amount of weakly adsorbed ammonia and decreased the quantity of stronger chemisorbed NH 3molecules.Thus the addi-tion of vanadia to STi-PILC significantly changed the surface acidic properties of the support.This is in good agreement with measurements reported in earlier study that the strength of Bronsted acidity increased with V 2O 5loadings,whereas Lewis acidity,mainly observed on the Ti-PILC (sulphur free support),remained almost constant [21].For the catalyst con-taining WO 3and V 2O 5the major desorption of NH 3occurred between 150and 300 C,the peak due to weak acid sites was intense and centered at about 220 C with a decrease of the intensity of the second peak.The change in the TPD profiles can be explained by the progressive transformation of the surface acidity after V 2O 5and WO 3addition.When WO 3and V 2O 5exist simultaneously on the surface of STi-PILC,the amount of Bronsted acid sites further increases,along with a decrease in Lewis acid sites.This suggests that the addition of WO 3and V 2O 5produces more Brons-ted acid sites while some of Lewis acid sites are covered by tungsten and vanadia.The Lewis acidity observed in all Ti-pillared clay samples was related to the acidic property of TiO 2[19,20].The addition ofTable 3XPS data of the catalysts investigated.SamplesBinding energy (eV)S /(Ti þV þW)atomic ratioW4f 7/2V2p 3/2S2p Ti2p 3/2STi-PILCe e169.5(2.71)459.4(4.65)0.582V 2O 5/STi-PILCe517.2(1.41)169.3(1.20)459.2(3.13)0.264WO 3e V 2O 5/STi-PILC36.5(0.84)516.9(1.38)168.9(0.43)458.8(3.01)0.082Values in parentheses are surface compositions (%).Table 2Textural properties of the samples investigated.SamplesNon-calcined Calcined at 400 C S BET (m 2/g)V p (cm 3/g)V m p (cm 3/g)S BET (m 2/g)V p (cm 3/g)V m p (cm 3/g)STi-PILC2260.1700.0461540.1300.025V 2O 5/STi-PILC720.0910.0141550.1590.013WO 3e V 2O 5/STi-PILC810.0870.0111590.1630.015S BET ¼BET surface area,V p :Total pore volume,V m p :Micropore volume.783L.Khalfallah Boudali et al./C.R.Chimie 12(2009)779e 786V 2O 5to STi-PILC induces an increase of the total amount of NH 3adsorbed on acid sites indicating that V 2O 5contributes to the improvement of the total acidity (Table 4).In the case of the WO 3e V 2O 5/STi-PILC sample,the slight decrease of the total amount of NH 3adsorbed may be explained by the coverage of the strong acid sites,arising from sulfate species,by relatively weak acid sites of WO 3.This interpretation agrees the detection of few amount of sulphur on the surface catalyst as observed by the decrease of S/(Ti þV þW)XPS atomic ratio for the WO 3e V 2O 5/STi-PILC sample.The TPR profile of the STi-pillared clay support displays only large peak,starting near 400 C and centered at 580 C (Fig.2).It was shown and well discussed in our earlier work that the hydrogen consumption over sulphated Ti-pillared clay is due to the reduction of sulfate to essentially SO 2with little H 2S formation [22].For the V 2O 5/STi-PILC catalyst,the threshold of hydrogen consumption began at 400 C and two peaks were found centered at 506and 530 C.The first reduction peak,shifted towards lower temperature after vanadia addition,is mainly due to the sulphate reduction into essentially SO 2with few H 2S and the second hydrogen consumption is attributed to the reduction of V 5þon V 2O 5[22].The reduction of V 2O 5/STi-PILC occurs at a temperature much lower than that of STi-PILC,showing an enhancement of sulphate reduction after vanadia addition.The TPR profiles clearly indicate that V 2O 5/STi-PILC is more easily reduced than STi-PILC.Since the WO 3/TiO 2catalyst exhibits maxima above 700 C,the reduction maximum at higher temperature was attributed to the reduction of TiO 2and WO 3[23].In the case of WO 3e V 2O 5/STi-PILC,the TPR profiles displays only a large peak,starting near 400 C and centered at 515 C whereas the small peak observed at 530 C for V 2O 5/STi-PILC disappeared.However,the reduction of sulfate completely hides the reduction of vanadium.There-fore the modification in reduction properties of sulfate and of vanadia evidences the existence of a strong interaction between tungsten,vanadia and sulfate on the surface of the WO 3e V 2O 5/STi-PILC catalyst leading to better red-ox properties of this material.Table 4Total amounts of ammonia adsorbed.SamplesNH 3(m mol/g catalyst)STi-PILC175V 2O 5/STi-PILC265WO 3e V 2O 5/STi-PILC2530100200300400500600700Temperature (°C)I n t e n s i t y (a .u .)(a)(b)(c)Fig. 2.H 2consumption profile over catalysts with temperature increase during H 2-TPR:(a)STi-PILC,(b)V 2O 5/STi-PILC and (c)WO 3e V 2O 5/STi-PILC.Fig.1.NH 3-TPD profiles of:(a)STi-PILC,(b)V 2O 5/STi-PILC and (c)WO 3e V 2O 5/STi-PILC.784L.Khalfallah Boudali et al./C.R.Chimie 12(2009)779e 7863.2.SCR-NO reactionThe NO conversions for the samples investigated are compared in Fig.3.For the sulphated Ti-pillared clay,the NO conversion began at200 C and increased with reaction temperature.The SCR-NO activity of the STi-PILC support is essentially related to the presence of sulfate which enhances the Bronsted acidity of the catalyst and contributes to the improved activity at high temperature.As mentioned in our previous work, the sulphated Ti-pillared clay exhibits higher NO removal activity at high temperature than the non-sulfated ones[16].We have shown a direct correlation between the SCR-NO activity and Bronsted acidity enhanced by the sulfation.After vanadia addition onto the STi-PILC,the SCR activity began at100 C, increased with temperature up to300 C then declined slightly at high temperature due to NH3oxidation byO2giving NO.Several researches have explained that the decrease of NO conversion is not caused by the decline of the catalytic activity but by the generation of NO by NH3oxidation[1,2].Note that no NO2 formation was observed for all the SCR experiments using our catalysts.The N2O formation was observed only on catalysts with high vanadia loading(5wt.%) and above300 C as indicated in our earlier work[22].In the case of WO3e V2O5/STi-PILC and V2O5/STi-PILC with the same vanadium content(3wt.%),the SCR-NO activity is similar for the two catalysts, therefore the promoting effect of WO3is not found at high temperature(Fig.3).The identical results were observed for the same catalysts containing1.5wt.%of vanadium(data not shown).The highest NO conver-sion(97%)at350 C,was obtained only for the samples with3wt.%of vanadium.When tungsten was deposited with vanadium at the same time on the surface of sulfated Ti-pillared clay,the sulfate species seem to play a more decisive role for NO removal activity than WO3species.These results are in contradiction with previous report results on effects of WO3supported by sulphur free V2O5/TiO2catalysts [2,12].The literature also reported that the SCR-NO activities on 4.4%V2O5þ8.2%WO3/TiO2-PILC (sulphur-free TiO2-PILC)was higher than that on 4.4%V2O5/TiO2-PILC and these two catalysts were highly active in SCR-NO than 4.4%V2O5þ8.2% WO3/TiO2and4.4%V2O5/TiO2,especially at higher temperature[12].In this later study the authors concluded that the addition of WO3and V2O5further increased the activities of the TiO2-PILC catalysts. From our study,it can be concluded that the contri-bution of WO3on V2O5/STi-PILC to the SCR activity is negligible in presence of sulfate.Hence,when both tungsten and sulfate exist simultaneously on the surface of V2O5/STi-PILC,the sulfate species seem to play a more important role for NO removal activity than WO3.It has been already reported that the addition of V2O5and WO3provides a wider temperature window than the V2O5addition due to the improved reduc-ibility at low temperature and the increased acidity at high temperature[5].In this work,the surface area of all samples is similar at400 C.Accordingly,the change of SCR reactivity should be explained by just considering the TPD and TPR results.NH3-TPD showed that the addition of vanadium and tungsten increased the total acidy.Also H2-TPR indicated that the addition of V and W increased the red-ox properties of the material.However,the reasonable explanation of the similarity in activity of the WO3e V2O5/STi-PILC and V2O5/STi-PILC catalysts having the same vanadia loading(3wt.%)is the dispersion between the acid and red-ox sites.TopsØe et al.studied the V2O5/TiO2 catalyst and based on TPD,TPR and FTIR they proposed two separate catalytic functions,namely acid (V5þ-OH)and red-ox(V5þ]O)[3].The authors suggested a dual site mechanism taken place over V5þe OH and V5þ]O.From this mechanism,it was suggested that the V5þ]O be reduced to V4þe OH by the ammonia adsorbed on the neighboring V5þe OH and V4þe OH be reoxidized by gaseous oxygen.Now we try to compare our catalysts with those reported in the literature and especially the commercial SCR catalysts which consist of TiO2as support and WO3e V2O5as active phase[1,2].Nowadays,deacti-vation of the commercial SCR catalysts applied inbio 020406080100Temperature (°C)NOConversion()Fig. 3.Catalytic activity for the SCR-NO reaction on catalysts investigated:( )STi-PILC,(:)V2O5/STi-PILC and(-)WO3e V2O5/STi-PILC.785L.Khalfallah Boudali et al./C.R.Chimie12(2009)779e786。
泰山魂 Microsoft Word 文档
泰山魂远望泰山，伟岸挺拔，畅想辽阔华北平原，一山独秀，擎天而立。
夜酣人惊呼，只为看日出，懵懂随伴同行，看不见山，只有阴森森林木掩映，间或坑洼相互提醒，或远近不同路灯照行，疾走而汗如雨下，虽有同伴解腰宽带，长裤披挂于肩，阴暗处息而慢行，每或灯光处疾奔，终有同游者发现大呼曰：“今有人夜游，无衣裹体登山”，闻者狂奔，随之轰然大笑，登山之乐呜呼如此。
久而问曰：“顶峰远近否”，答曰：“近十八盘”。
良久，人语提醒，十八盘也。
虹霓灯光几许为日出，其时深夜，朦胧夜色伴灯明，盘路虽陡攀援而上不觉其危。
行进间有龛笼罩神塑，投递银币尔，吾虽不理继往。
终至南天门，有卖粥者，碗饮之，冷风嗖嗖，粥粘衣角，甚狼狈。
稍息登峰有租赁棉衣者，恃体健拒之，及峰巅不胜凄冷，塑布笼颈颅，此也谓游泰山也。
及至玉皇顶庙宇人头攒动，挤身而进见有叩首者，皆不言甚庄重，不明其意亦学而叩之，疾出问曰：“叩首者何也？”答曰：“属相祈福罢了”，顿悟而赫然不与人语心自明也。
想当年始皇登山封禅痴迷与神灵通，跪拜久而睡去，轰鸣雷电顿心身惊惧而醒，是感应天地乎？哈哈，自然万象尔，亏有李斯提灯急来引下，不然魂魄随天去未可知也。
不胜寒凉下山心切，无意留恋气象万千景色，轻雾漫来，不复可观日出，却有仙界意境，吕仙人望日石可鉴，随下天梯归去。
路遇五大夫松，油然心念千年，沿途流瀑滑石而泻青苔映隐期间。
及至半山露台，凭栏远眺，碧霞祠也，云雾缭绕，雾起谷间顺风弥漫，薄纱萦苍翠。
峰回路转，去时白带尽现眼前，十余米瀑布湍流急下，分两道水流豁然有声。
今古文人墨客登斯山，心怡若何不得而知，山下酷热半山阴雨，山巅冷风凄凄不胜脆寒，景色俊逸而浑厚，不是山脉连绵却万马奔腾，日出东海而观之，月栖乌山而眼底，黄山太秀嵩山过沉重，天下之山或灵气妖娆，或憨实无华，均不及泰山万古雄浑之气魄，不依万山磅礴以壮势，不借怪奇而哗然，昂昂乎唯我独尊。
一蓑烟雨2011年6月10日。
【策划书】团员活动登泰山策划书
【关键字】策划书非电九班党团系列活动一——登“五岳之尊”泰山策划书主办：非电九班党（团）支部时间：2012年9月非电九班党团系列活动一——登“五岳之尊”泰山活动简介一、活动主题携手同心共登泰山主要体现同学们团结合作的精神，作为一个集体，遇到问题大家能够齐心协力，共度难关。
二、活动背景8月20号，我们来自全国各地的53名国网新员工组成了一个大集体，随后虽然经历了7天的军训，但是大家互相之间仍不是很了解，班级没有凝聚力。
同时，对于大多数同学是第一次来到齐鲁大地，都很想走出校园出去看看山东省的地理与人文。
三、活动目的泰山之高，想要成功的爬到山顶对于普通的人来说都是一种挑战，班委会力图通过组织这一登泰山的活动，增强班级同学的意志与品质，培养大家的团结协作精神，增进同学之间的感情；同时泰山也是中国文化的圣地，通过这一活动也可以增加同学们对中国保守文化的了解，感受中国保守文化的魅力之处。
四、活动时间与地点时间：2012年9月15日21点至2012年9月16日12点地点：山东省泰安市泰山五、活动对象国网技术学院综合培训部非电九班部分成员。
六、组织机构和人员组织机构：非电九班党（团）支部组织人员：郑后成、鄢蜜昉活动安排一、活动筹备1.统计参加活动的同学名单；2.上网查阅登泰山攻略，制定登山路线；3.联系包车，与司机谈好时间地点与价钱；4.通知同学们出发的时间地点以及注意事项。
二、活动流程1.9月15日晚9点同学们在学校东门集合坐车去泰安。
2.晚10点左右到达泰山，由党支书郑后成同学负责给大家购票，其他同学原地休息。
3.晚11点开始登山。
4．16日凌晨4点左右到达山顶，休息并吃些东西。
5.5点50分共同看日出。
6.随后大家在山顶拍照，合影留念。
7.8点大家集合，下山。
8．中午12点大家在山下集合，做包车返回济南。
此文档是由网络收集并进行重新排版整理.word可编辑版本！。
爬山活动会议总结
爬山活动会议总结1. 引言本文档旨在对最近举行的爬山活动会议进行总结和回顾。
会议的主要目的是讨论和安排即将进行的爬山活动的细节和策划。
2. 会议概述本次会议于[日期]在[地点]召开，与会人员共计[人数]人。
会议主持人为[主持人姓名]，大家针对当前的爬山活动进行了广泛的讨论和交流。
3. 议题讨论3.1 活动日期和地点确定在会议开始阶段，我们首先确定了爬山活动的具体日期和地点。
经过大家的讨论和投票，最终确定活动时间为[日期]，地点为[地点]。
3.2 活动路线规划为了确保活动的顺利进行，我们对活动路线进行了详细规划。
在会议期间，大家积极提出了各自的意见和建议。
经过多次讨论，我们最终确定了活动的路线，包括起点、途经景点和终点。
3.3 安全措施和准备工作在会议过程中，我们也充分考虑了活动的安全性和准备工作。
大家提出了应对突发情况的措施，例如携带急救工具、制定应急预案等。
此外，我们还确定了参与者需要做好的个人装备和必备物品清单。
3.4 其他讨论事项除了活动日期、地点、路线和安全措施，我们还讨论了其他与活动相关的事项，例如费用分摊、活动形式、交通安排等。
所有的决策和讨论结果都进行了记录，并在会后进行了归档。
4. 行动计划在会议的最后阶段，我们制定了详细的行动计划。
每位参与者都被分配了具体的任务和责任。
相关的行动计划已经整理成表格，并通过邮件发送给每个参与者。
5. 结束语通过本次会议，我们对即将进行的爬山活动有了更清晰的认识。
在会议中，大家的积极参与和建设性的意见对活动规划起到了重要的促进作用。
我们相信，通过集体的努力和配合，本次爬山活动将会取得圆满成功。
感谢所有参与会议的人员，特别感谢[主持人姓名]的出色组织和主持。
期待在[活动日期]的爬山活动中与大家再次相聚！以上为本次爬山活动会议的总结和回顾，会议纪要和行动计划的详细内容请参阅附件。
[附件名称]参考文献•[引用文献1]•[引用文献2]。
泰山赞演讲稿5篇
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文档下载后可定制修改，请根据实际需要进行调整和使用，谢谢!并且，本店铺为大家提供各种类型的经典范文，如工作总结、报告大全、演讲致辞、条据书信、心得体会、党团资料、读后感、作文大全、教学资料、其他范文等等，想了解不同范文格式和写法，敬请关注!Download tips: This document is carefully compiled by this editor.I hope that after you download it, it can help you solve practical problems. The document can be customized and modified after downloading, please adjust and use it according to actual needs, thank you!In addition, this shop provides you with various types of classic sample essays, such as work summary, report encyclopedia, speeches, articles and letters, experience and experience, party and group information, after reading, composition encyclopedia, teaching materials, other sample essays, etc. I want to know the difference Please pay attention to the format and writing of the sample essay!泰山赞演讲稿5篇演讲稿的准备是需要用心的，因为是当着众人进行演说的稿件，我们在选择演讲主题的时候，一定要选择相关的演讲稿，以下是本店铺精心为您推荐的泰山赞演讲稿5篇，供大家参考。
泰安市人民政府关于印发第三十一届泰山国际登山节暨2017中国泰安
泰安市人民政府关于印发第三十一届泰山国际登山节暨2017中国泰安投资合作洽谈会总体方案的通知【法规类别】外商投资企业综合规定【发文字号】泰政发[2017]10号【发布部门】泰安市政府【发布日期】2017.08.30【实施日期】2017.08.30【时效性】现行有效【效力级别】地方规范性文件泰安市人民政府关于印发第三十一届泰山国际登山节暨2017中国泰安投资合作洽谈会总体方案的通知（泰政发〔2017〕10号）各县、市、区人民政府，市政府各部门、直属单位，省属以上驻泰各单位：现将《第三十一届泰山国际登山节暨2017中国泰安投资合作洽谈会总体方案》印发你们，请认真组织实施。
泰安市人民政府2017年8月30日第三十一届泰山国际登山节暨2017中国泰安投资合作洽谈会总体方案第三十一届泰山国际登山节暨2017中国泰安投资合作洽谈会将于2017年9月6日至12日举办。
为认真做好活动筹备、组织工作，全面展示泰安全域旅游形象，进一步拓宽经贸合作领域，制定本方案。
一、工作目标以创新、协调、绿色、开放、共享为宗旨，突出产业招商、精准招商和大项目招商，组织开展务实高效的经贸合作活动和丰富多彩的旅游、科技、文化、体育活动，集中宣传产业转型升级新成果，加快推进新旧动能转换，打造对外开放的平台、招商引资的擂台、全域旅游的名片、招才引智的盛会、文化交流的窗口、体育竞技的舞台，全面展示泰安经济社会发展成果，让世界进一步了解泰安，让泰安进一步走向世界。
二、举办单位（一）主办单位：中国登山协会、商务部投资促进事务局、山东省旅游发展委员会、山东省体育局、山东省商务厅、山东省贸促会、山东广播电视台、泰安市人民政府。
（二）承办单位：泰安市人民政府。
三、活动内容（一）开幕式和经贸板块1.活动安排：第三十一届泰山国际登山节暨2017中国泰安投资合作洽谈会开幕式、2017中国泰安投资合作洽谈会、泰安市经济社会发展成果展、第二届外国专家泰安行、泰安市经济合作项目推介会、2017百家知名外商泰安行、2017台湾工商精英泰山行、2017首届泰山国际农业机械博览会、2017第二届泰山国际福祉暨康复设备博览会、2017第二届泰山国际残疾人论坛、“叙游子乡情谋家乡发展”恳谈会暨“天南地北泰安人”“回家”系列活动、2017首届泰山（润恒城）农副产品博览会以及2017中国国际建筑钢结构及配套产业博览会等活动。
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泰山产业研究院（常用名：泰山会），成立于1993年，由于成立大会在山东召开，遂取名“泰山”，是由中国民营科技实业家协会主管的非独立法人机构。
它由中国知名且有相当影响力企业的CEO（或董事长）组成，每年只发展1家会员单位，会员单位包括联想控股、四通集团、泛海集团、远大集团、复星集团、巨人集团等15家，联想控股总裁柳传志亲任会长，段永基任理事长，顾问吴敬琏、胡德平。
[1]泰山会是中国最知名、最神秘的大型商会之一，甚至有人将其与美国骷颅会并列。