ImageVerifierCode 换一换
格式:PPTX , 页数:21 ,大小:2.43MB ,
资源ID:7342356      下载积分:10 金币
快捷注册下载
登录下载
邮箱/手机:
温馨提示:
快捷下载时,用户名和密码都是您填写的邮箱或者手机号,方便查询和重复下载(系统自动生成)。 如填写123,账号就是123,密码也是123。
特别说明:
请自助下载,系统不会自动发送文件的哦; 如果您已付费,想二次下载,请登录后访问:我的下载记录
支付方式: 支付宝    微信支付   
验证码:   换一换

开通VIP
 

温馨提示:由于个人手机设置不同,如果发现不能下载,请复制以下地址【https://www.zixin.com.cn/docdown/7342356.html】到电脑端继续下载(重复下载【60天内】不扣币)。

已注册用户请登录:
账号:
密码:
验证码:   换一换
  忘记密码?
三方登录: 微信登录   QQ登录  

开通VIP折扣优惠下载文档

            查看会员权益                  [ 下载后找不到文档?]

填表反馈(24小时):  下载求助     关注领币    退款申请

开具发票请登录PC端进行申请

   平台协调中心        【在线客服】        免费申请共赢上传

权利声明

1、咨信平台为文档C2C交易模式,即用户上传的文档直接被用户下载,收益归上传人(含作者)所有;本站仅是提供信息存储空间和展示预览,仅对用户上传内容的表现方式做保护处理,对上载内容不做任何修改或编辑。所展示的作品文档包括内容和图片全部来源于网络用户和作者上传投稿,我们不确定上传用户享有完全著作权,根据《信息网络传播权保护条例》,如果侵犯了您的版权、权益或隐私,请联系我们,核实后会尽快下架及时删除,并可随时和客服了解处理情况,尊重保护知识产权我们共同努力。
2、文档的总页数、文档格式和文档大小以系统显示为准(内容中显示的页数不一定正确),网站客服只以系统显示的页数、文件格式、文档大小作为仲裁依据,个别因单元格分列造成显示页码不一将协商解决,平台无法对文档的真实性、完整性、权威性、准确性、专业性及其观点立场做任何保证或承诺,下载前须认真查看,确认无误后再购买,务必慎重购买;若有违法违纪将进行移交司法处理,若涉侵权平台将进行基本处罚并下架。
3、本站所有内容均由用户上传,付费前请自行鉴别,如您付费,意味着您已接受本站规则且自行承担风险,本站不进行额外附加服务,虚拟产品一经售出概不退款(未进行购买下载可退充值款),文档一经付费(服务费)、不意味着购买了该文档的版权,仅供个人/单位学习、研究之用,不得用于商业用途,未经授权,严禁复制、发行、汇编、翻译或者网络传播等,侵权必究。
4、如你看到网页展示的文档有www.zixin.com.cn水印,是因预览和防盗链等技术需要对页面进行转换压缩成图而已,我们并不对上传的文档进行任何编辑或修改,文档下载后都不会有水印标识(原文档上传前个别存留的除外),下载后原文更清晰;试题试卷类文档,如果标题没有明确说明有答案则都视为没有答案,请知晓;PPT和DOC文档可被视为“模板”,允许上传人保留章节、目录结构的情况下删减部份的内容;PDF文档不管是原文档转换或图片扫描而得,本站不作要求视为允许,下载前可先查看【教您几个在下载文档中可以更好的避免被坑】。
5、本文档所展示的图片、画像、字体、音乐的版权可能需版权方额外授权,请谨慎使用;网站提供的党政主题相关内容(国旗、国徽、党徽--等)目的在于配合国家政策宣传,仅限个人学习分享使用,禁止用于任何广告和商用目的。
6、文档遇到问题,请及时联系平台进行协调解决,联系【微信客服】、【QQ客服】,若有其他问题请点击或扫码反馈【服务填表】;文档侵犯商业秘密、侵犯著作权、侵犯人身权等,请点击“【版权申诉】”,意见反馈和侵权处理邮箱:1219186828@qq.com;也可以拔打客服电话:0574-28810668;投诉电话:18658249818。

注意事项

本文(博士面试答辩英文版科研陈述.pptx)为本站上传会员【a199****6536】主动上传,咨信网仅是提供信息存储空间和展示预览,仅对用户上传内容的表现方式做保护处理,对上载内容不做任何修改或编辑。 若此文所含内容侵犯了您的版权或隐私,请立即通知咨信网(发送邮件至1219186828@qq.com、拔打电话4009-655-100或【 微信客服】、【 QQ客服】),核实后会尽快下架及时删除,并可随时和客服了解处理情况,尊重保护知识产权我们共同努力。
温馨提示:如果因为网速或其他原因下载失败请重新下载,重复下载【60天内】不扣币。 服务填表

博士面试答辩英文版科研陈述.pptx

1、单击此处编辑母版标题样式,单击此处编辑母版文本样式,第二级,第三级,第四级,第五级,2019/11/23,#,申请者,:-,申请导师,:-,2015,年,3,月,25,日,-,大学博士申请科研陈述,Outline,1.PersonalInformation,2.Research Progress During Graduate Period,3.Research Topics and Interests,1.PersonalInformation,Education,:,09/2012-06/2015.Food Science,State Key Laboratory of Tea Plant

2、 Biology and Utilization,Anhui Agricultural University.,09/2008-06/2012.B.Eng.,Food Science and Engineering,Anhui Agricultural University.,09/2008-06/2012.Chu Zhou High School.,Awards,:,National Encouragement Scholarship,Professional Third-class Scholarship,Triple A Outstanding Student,Outstanding S

3、tudent Leaders,School Outstanding Graduation Thesis,etc.,PersonalInformation,LanguageProficiency:,Ability to search and read English literature skillfully from all kinds of English database.Ability to write English papers independently.,ComputerSkills:,Microsoft office,Endnote,Origin,Omnic,Photoshop

4、Spass,Chemical Office,XPert Highscore Plus,etc.,2.,Research Progress During Graduate Period,Water-drinking fluorosis covered about,2.2,million km,2,1.4,millions of people,Limitations of traditional adsorbent,:,(,1,),Narrow pH range,(,2,),Low adsorption capacity,(,3,),Secondary pollution,Fig.2-1 Dis

5、tribution of fluorosis in China,2.1 Background,:,Distribution of fluorosis in China,2.,Research Progress During Graduate Period,2.2 Removal of fluoride from drinking water using tea waste loaded with Al/Fe oxides,Fig,.2-2 Graphical abstract of,tea waste loaded with Al/Fe oxides,2.,Research Progress

6、During Graduate Period,Fig.2-3 Effect of pH on the q,e,of biosorbents,Table 2-1 The adsorption capacity of fluoride,q,0,of activated alumina was,1.45,mg/g at pH 7(Jagtap,2012).,2.2 Removal of fluoride from drinking water using tea waste,loaded with,Al/Fe oxides,pH of drinking water:6.0-8.0,Research

7、Progress,2.2 Removal of fluoride from drinking water using tea waste loaded with Al/Fe oxides,Fig.2-4 Residual concentration of Fe(a)and Al(b)in fluoride solution with pH after adsorption,pH of drinking water:6.0-8.0,2.,Research Progress During Graduate Period,2.,Research Progress During Graduate Pe

8、riod,2.3 Tea waste supported Al oxides nanoparticles with help of Anionic polyacrylamide(Tea-APAM-Al),Fig.2-4.Molecular structure of APAM,Carboxylic acid,functional groups of organic acids have demonstrated a,positive effect,on enhancement of,fluoride adsorption,from aqueous(Velazquez-Jimenez,2014;L

9、i,2013;Wang,2011).,2.,Research Progress During Graduate Period,2.3 Tea waste supported Al oxides nanoparticles with help of Anionic polyacrylamide(Tea-APAM-Al),Fig.2-5 SEM images of Tea-Al(a)and Tea-APAM-Al(b),Table 2-2 Surface area,pore volume and pore diameter of biosorbents.,15 times,16 times,2.,

10、Research Progress During Graduate Period,2.3 Tea waste supported Al oxides nanoparticles with help of Anionic polyacrylamide(Tea-APAM-Al),Fig.2-6.Effect of pH on the adsorption capacity of biosorbents,pH of drinking water:6.0-8.0,Table 2-3 The adsorption capacity of fluoride,q,0,of activated alumina

11、 was,1.45,mg/g at pH 7(Jagtap,2012),29 times,2.,Research Progress During Graduate Period,Fig.2-4.Molecular structure of APAM,2.3 Tea waste supported Al oxides nanoparticles with help of Anionic polyacrylamide(Tea-APAM-Al),Fig.2-7 Concentration of fluoride and sulfate ions in solution as a function o

12、f contact time with initial fluoride concentration of 30 mg/L,The results indicated that,anion exchange with sulfate ions,was one of the,important mechanisms,for fluoride removal,2.,Research Progress During Graduate Period,2.3 Tea waste supported Al oxides nanoparticles with help of Anionic polyacry

13、lamide(Tea-APAM-Al),The band at 1109 cm,-1,disappeared after adsorption of fluoride implying that,SO,4,2,had played an,important role,in fluoride removal.,Fig.2-8.FTIR spectra of biosorbents,2.,Research Progress During Graduate Period,2.3 Tea waste supported Al oxides nanoparticles with help of Anio

14、nic polyacrylamide(Tea-APAM-Al),Tea-APAM-Al showed a remarkable increase from 4.02%to 15.99%in comparison to Tea-Al.,The quantity of sulfate ion could be increased with the participation of APAM among the loading progress.,Sulfate ions might be replaced by fluoride,which was consistent with the resu

15、lts of FTIR and adsorption experiments.,Table 2-4 XPS analysis of Tea-Al,Tea-APAM-Al before and after fluoride adsorption,NaF,:,684.5,eV,The results suggested that Al atoms participated in fluoride adsorption process.,A,new F(1s)peak was found at 685.5 eV,which was higher than the 684.5 eV for,NaF,s

16、ignifying that surface reactions had,occurred.,2.,Research Progress During Graduate Period,2.3 Tea waste supported Al oxides nanoparticles with help of Anionic polyacrylamide(Tea-APAM-Al),Fig.2-9 XPS spectra of the Al 2p(a)and F 1s(b)of Tea-APAM-Al before and after adsorption,2.,Research Progress Du

17、ring Graduate Period,2.3 Tea waste supported Al oxides nanoparticles with help of Anionic polyacrylamide(Tea-APAM-Al),Table 2-5 Chemical parameters of ground water before and after treatment with Tea-APAM-Al,2.,Research Progress During Graduate Period,Summarize:,Two kinds of,Tea-Al-Fe exhibited supe

18、rior fluoride adsorption than traditional adsorbents.,Tea-Al-Fe could be used to remove fluoride without pH adjustment.,The residual concentrations of Al and Fe in drinking water adsorbed by Tea-Al-Fe at different pH ranges from 5.0 to 10.0 were below the WHO standard.,2.,Research Progress During Gr

19、aduate Period,Publications,1,2,3,4,5,3.Research Topics and Interests,3.1 The potential abilities of polysaccharide and its derivatives to remove fluoride or heavy metals from water,3.Research Topics and Interests,3.,2 Synergistic interaction for treatment of diabetic,Tea polysaccharide,Tea polyphenols,Medicine for treatment of diabetic,Mouse Model,Cell Model,S,ynergistic interaction for treatment of diabetic,Proposed mechanisms,Thank you!,

移动网页_全站_页脚广告1

关于我们      便捷服务       自信AI       AI导航        抽奖活动

©2010-2026 宁波自信网络信息技术有限公司  版权所有

客服电话:0574-28810668  投诉电话:18658249818

gongan.png浙公网安备33021202000488号   

icp.png浙ICP备2021020529号-1  |  浙B2-20240490  

关注我们 :微信公众号    抖音    微博    LOFTER 

客服