网站地图| 免费获取|
毕业论文网
  • 网站首页|
  • 论文范文|
  • 论文降重|
  • 职称论文发表|
  • 合作期刊|
  • 论文下载|
  • 计算机论文|
  • 外文翻译|
  • 免费论文|
  • 论文资料|
  • 论文开题报告
搜索

当前位置:毕业论文网 -> 论文范文 -> 化学工程与工艺 -> 复合萃取精馏分离乙酸乙酯-乙醇-水混合体系的研究
机械模具数控资料设计| 土木工程论文范文| 化学工程与工艺论文| 采矿专业设计| 工业工程论文| 热能与动力工程| 材料科学工程| 轻化工程| 焊工钳工技师论文| 给水排水工程|
食品科学生物技术论文| 服装设计论文资料| 理工科资料设计论文| 包装工程论文| 印刷工程论文| 化工与材料论文| 生物工程论文| 制药工程| 机械模具免费论文| 交通工程论文|

复合萃取精馏分离乙酸乙酯-乙醇-水混合体系的研究

本文ID:LW67162 文档字数:17284 价格:¥128.00 → 信用说明

扫一扫 扫一扫
复合萃取精馏分离乙酸乙酯-乙醇-水混合体系的研究

文档编号:HG319   文档字数:17284

摘  要
    本文综述分析了国内外有关乙酸乙酯一乙醇一水体系分离现状,提出了复合萃取精馏工艺流程,选择水为分离乙酸乙酯和乙醇的萃取剂,甘油为分离乙酸乙酯和水的萃取剂。
采用气相色谱法测定乙酸乙酯、乙醇、水在甘油中的无限稀释活度系数,用单参数法关联乙酸乙酯-甘油、乙醇-甘油、水-甘油二元体系的模型参数。设计单级循环式汽液平衡釜,系统的测定了乙酸乙-乙醇、乙醇-水、乙酸乙酯-乙醇-水、乙酸乙酯-乙醇-甘油、乙醇-水-甘油及乙酸乙酯-乙醇-水-甘油体系的VLE,采用最小方差法关联Wilson, UNIQUAC, NRTL, Margules,Van Laar模型中该体系的相互作用参数。
模拟结果表明:Wilson模型关联误差最小,同时建立了二元、三元、四元模拟框图并用NEWTON-RAPSON法关联二元、三元、四元汽液平衡数据,并与实测数据进行比较。为复合萃取精馏模拟计算及进一步实验研究提供了理论依据和基础数据。
关键词:萃取剂,复合萃取精馏,甘油,汽液平衡,模型参数
Abstract
    The recent processes of separation ethyl acetate-ethanol-water mixture were reviewed in this paper. Azeotropic distillation,membrane separation,liquid-liquid extraction, extractive distillation processes were studied and discussed. On the basis of predecessors,the composite extractive distillation was put forward first by which high purity ethyl acetate can be obtained one time.
The interaction of solvents,ethyl acetate,ethanol and water were studied in detail, relative volatility of ethyl acetate/ethanol and ethyl acetate/water were tested under different solvents. Combined with other influencing factors,water was selected as extractive agent for ethyl acetate-ethanol system and glycerol for ethyl acetate-water system. VLE  data  of  ethanol-water, ethyl acetate-ethanol and ethanol-ethyl acetate-water, ethanol-water-glycerol, ethyl acetate-ethanol-glycerol and ethanol-ethyl acetate-water-glycerol were tested by the simple single equilibrium caldron .The interactive parameters of Wilson, UNIQUAC, NRTL, Margules. Van Laar equation were correlated by the method of  Minimum Variance .The results showed that Wilson equation had the minor absolute error. Diagram of two phases system simulation calculation, Diagram of three phases system simulation calculation and Diagram of four phases system simulation calculation were given,the binary,ternary and quaternary VLE data were simulated according to interactive parameters. The results of calculation data were coincided with experiment data, and providedbasic data for the separation calculation of ethyl acetate-ethanol-water.
The paper can provide theoretical basis and industrial produce for the simulation and calculation of composite extractive distillation and further studies on experiments.
Keywords: Extraction agent;Composite extractive distillation;Glycerol;VLE;Model parameter

目   录
1 概述 1
1.1  前言 1
1.2  国内外研究现状及趋势 4
2  复合萃取溶剂的筛选 11
2. 1  国内外萃取剂筛选现状 11
2. 2  复合萃取剂筛选 13
2. 3  实验部分 15
3  汽液平衡数据的测定及关联 19
3. 1  概述 19
3. 2  实验方案筛选 19
3. 3  无限稀释活度系数的测定 20
3. 4  汽液平衡数据的测定 22
3. 5  小结 35
结论 36
参考文献 37
致谢 40

复合萃取精馏分离乙酸乙酯-乙醇-水混合体系的研究由毕业论文网(www.huoyuandh.com)会员上传。
原创论文资料流程 相关论文
上一篇:化工行业循环经济的指标及效果评价 下一篇:对已内酰胺二步重排的研究
推荐论文 本专业最新论文
Tags:复合 萃取 分离 乙酸 乙醇 混合 体系 研究 2014-03-12 12:43:13【返回顶部】
发表论文

联系方式 | 论文说明 | 网站地图 | 免费获取 | 钻石会员 | 硕士论文资料


毕业论文网提供论文范文,论文代发,原创论文资料

本站部分文章来自网友投稿上传,如发现侵犯了您的版权,请联系指出,本站及时确认并删除  E-mail: 17304545@qq.com

Copyright@ 2009-2020 毕业论文网 版权所有