Horse 发表于 2012-11-5 17:36:28

Distillation Design and Control Using Aspen Simulation, 2nd Edition

这几天和wiley中国的联系下,前面11章应该基本差不多,可以直接用公子小白翻译的,后面的几章打算召集英文好的兄弟来一起翻译。
论坛里面有不少在国外上学的兄弟,如果有时间有兴趣的话,可以联系下我。英语水平要好,因为要出版,太烂了丢人。
争取中文版和英文版在2013年的3月份同步出版。我联系willey版权方和Publishing。
让我们为中国的化工界留下一点东西,做一点值得做的有意义的事情。
我们来一起完成这个伟大的任务。需要校对的是chapter1~11,chapter12~16是在第一版的基础上新增的,需要翻译和校对。

This book uses the commercial simulator Aspen Plus to develop rigorous simulations of single distillation columns and sequences of columns. Methods are illustrated for designing the economic optimum distillation column from a steady-state standpoint. Total annual cost, which includes both capital and energy costs, is used as the objective function to be minimized. Other issues such as robustness to disturbances and sensitivity to uncertainties in physical properties, tray efficiencies and market requirements are also considered. Another unique feature is coverage of the design and control of petroleum fractionators, which is non-existent in any design books. Aspen Dynamics are then used to explore the dynamics of these designs and to develop effective control structures.
The new edition updates and expands on the first edition and adds new chapters on the divided wall column a more widely applied method and carbon dioxide capture from stack gas. Also discussed is the use of dynamic simulation to study safety issues (high pressure and temperatures) in the event of operating failures (loss of cooling water), an update on the discussion of Aspen Plus analysis tools for ternary distillation columns and azeotropic separation, and a discussion of control structures and process configurations for handling the very significant column turndowns (very low feed flowrates) required in chemical plants coupled with power generation processes or inherently intermittent “green” energy sources (solar and wind).

Preface

Chapter 1 – Fundamentals of VLE

1.1 Vapor pressure

1.2 Binary VLE phase diagrams

1.3 Physical property methods

1.4 Relative volatility

1.5 Bubblepoint calculations

1.6 Ternary diagrams

1.7 VLE non-ideality

1.8 Residue curves for ternary systems

1.9 Distillation Boundaries

1.10 Conclusion

Chapter 2 – Analysis of Distillation Columns

2.1 Design degrees of freedom

2.2 Binary McCabe-Thiele method

2.3 Approximate multi-component methods

2.4 Conceptual design of ternary systems

2.5 Conclusion

Chapter 3 – SettingUp a Steady-State Simulation

3.1 Configuring a new simulation

3.2 Specifying chemical components and physical properties

3.3 Specifying stream properties

3.4 Specifying parameters of equipment

3.5 Running the simulation

3.6 Using design spec/vary function

3.7 Finding the optimum feed tray and minimum conditions

3.8 Column sizing

3.9 Using Conceptual Design

3.10 Conclusion

Chapter 4 – Distillation Economic Optimization

4.1 Heuristic optimization

4.2 Economic basis

4.3 Results

4.4 Operating optimization

4.5 Optimum pressure for vacuum columns

4.6 Conclusion

Chapter 5 – More Complex Distillation Systems

5.1 Extractive distillation

5.2 Heterogeneous azeotropic distillation

5.3 Pressure-swing azeotropic distillation

5.4 Heat-integrated columns

5.5 Conclusion

Chapter 6 – Steady-State Calculations for Control Structure Selection

6.1 Control structure alternatives

6.2 Feed-composition sensitivity analysis

6.3 Temperature control tray selection

6.4 Conclusion

Chapter 7 – Converting from Steady State to Dynamic Simulation

7.1 Equipment sizing

7.2 Exporting to Aspen Dynamics

7.3 Opening the dynamic simulation in Aspen Dynamics

7.4 Installing basic controllers

7.5 Installing temperature and composition controllers

7.6 Performance evaluation

7.7 Conclusion

Chapter 8 – Control of More Complex Columns

8.1 Extractive distillation process

8.2 Columns with partial condensers

8.3 Control of heat-integrated distillation columns

8.4 Control of azeotropic columns/decanter system

8.5 Unusual Control Structure

8.6 Conclusion

Chapter 9 – Reactive Distillation

9.1 Introduction

9.2 Types of reactive distillation systems

9.3 TAME process basics

9.4 TAME reaction kinetics and VLE

9.5 Plantwide control structure

9.6 Conclusion

Chapter 10 – Control of Sidestream Columns

10.1 Liquid sidestream column

10.2 Vapor sidestream column

10.3 Liquid sidestream column with stripper

10.4 Vapor sidestream column with rectifier

10.5 Sidestream purge column

10.6 Conclusion

Chapter 11 – Control of Petroleum Fractionators

11.1 Petroleum fractions

11.2 Characterization of crude oil            

11.3 Steady-state design of preflash column

11.4 Control of preflash column

11.5 Steady-state design of pipestill

11.6 Control of pipestill

11.7 Conclusion

Chapter 12 – Design and Control of Divided-Wall Columns

12.1 Introduction

12.2 Steady-state design

12.3 Control of divided-wall columns

12.4 Control of conventional column process

12.5 Conclusion and Discussion

Chapter 13 – Dynamic Safety Analysis

13.1 – Introduction

13.2 – Safety scenarios

13.3 – Process studied

13.4 – Basic Radfrac models

13.5 Dynamic simulations

13.6 Comparison of dynamic responses

13.7 Other Issues

13.8 Conclusion

Chapter 14 – Carbon Dioxide Capture

14.1 – Carbon dioxide removal in low-pressure air combustion power plants

14.2 – Carbon dioxide removal in high-pressure IGCC power plants

14.3 – Conclusion

Chapter 15 – Distillation Turndown

15.1 Introduction

15.2 Control problem

15.3 Process studied

15.4 Dynamic Performance for ramp disturbances

15.5 Dynamic performance for step disturbances

15.6 Other control structures

15.7 Conclusion

Chapter 16 – Pressure-Compensated Temperature Control in Distillation Columns

16.1 Introduction

16.2 Numerical example studied

16.3 Conventional control structure selection

16.4 Temperature/pressure/composition relationships

16.5 Implementation in Aspen Dynamics

16.6 Comparison of dynamic results

16.7 Conclusion

http://meng.horse/xwb/images/bgimg/icon_logo.png 该贴已经同步到 Horse的微博

kljay007 发表于 2012-11-5 17:36:28

尕元子 发表于 2013-5-4 19:16
马哥能给我一份完整的英文版的吗,我现在只有1~11章啊。没12章以后的,谢谢你了,我qq:272910145

请问,你那有12章以后的了么???

jiangjibao 发表于 2012-11-5 17:36:28

希望这个翻译早点问世真的很需要一部好的书籍啊

just4AP 发表于 2012-11-5 17:36:28

很期待有中文版本
不知道目前進展到哪裡?
希望可以趕快購買到

imeagor 发表于 2012-11-5 17:36:28

不知道进展如何,期待哟,若有需要我可以加入翻译行列

siyuelu 发表于 2012-11-5 17:36:28

果然很吊炸天啊。竟然又翻译了。不知道现在出版没有

406613254 发表于 2012-11-5 17:36:28

很强大的样子啊!期待中文出版啊!

Cory0971 发表于 2012-11-5 17:36:28

什么时候在印刷啊 都买不到了

shineway2008 发表于 2012-11-5 17:36:28

楼主加油,期待大作横空出世!

轩辕枫 发表于 2012-11-5 17:36:28

加油吧,能力不足,只待出版

风子爱上欣 发表于 2012-11-5 17:36:28

马兄 碉堡了。。。马后炮 真不错 。。。

chenhaijunsjy 发表于 2012-11-5 17:36:28

无私的楼主为群众服务

ectxcqm 发表于 2012-11-5 17:36:28

看不到内容在哪里下载

快乐蓝天/aiq 发表于 2012-11-5 17:36:28

正在学习 灰常感谢~~

北辰hc 发表于 2012-11-5 17:36:28

感谢马哥,太感谢

1592203609 发表于 2012-11-5 17:36:28

呵呵,进展如何?

小柳 发表于 2012-11-5 18:23:11

很支持啊,可惜我有心无力。大家加油!!{:1106_362:}

微博评论 发表于 2012-11-5 18:25:51

@west_volcano 看好你哦~

http://meng.horse/xwb/images/bgimg/icon_logo.png 来自 皮卡丘007 的新浪微博

liulingjun 发表于 2012-11-5 18:31:02

{:1106_362:}予人玫瑰,手留余香

tdl522 发表于 2012-11-5 18:40:04

有图有真相,顶起来!

xmy101 发表于 2012-11-5 18:43:35

{:1106_362:}{:1106_362:}
我看不错噢 谢谢楼主!马后炮化工论坛越来越好!

lihaiyong826 发表于 2012-11-5 18:49:12

争取在第二版出版之前把第一版看好,{:1106_362:}

Fadingaway 发表于 2012-11-5 19:00:18

支持,可惜我英语太差

四海同心→芷 发表于 2012-11-5 19:00:35

希望早日能够看到电子版的``{:1106_362:}

hunter2002 发表于 2012-11-5 20:20:16

分享的内容在哪里

zyx-iccas 发表于 2012-11-5 20:40:50

感谢楼主,功德无量,期待中

璇雅 发表于 2012-11-5 21:06:37

支持支持{:1106_362:}

caral 发表于 2012-11-5 21:24:49

从今天开始,我要 时常光顾 马后炮,支持马哥,支持飞梦同学~~{:1106_362:}

Horse 发表于 2012-11-5 21:31:49

zyx-iccas 发表于 2012-11-5 20:40 static/image/common/back.gif
感谢楼主,功德无量,期待中

非常感谢兄弟的支持。。。。我这几天争取尽快和willey公司确认好,

Horse 发表于 2012-11-5 21:34:59

众人拾柴火焰高。。。。团队的力量是强大的。。
倍感欣慰,谢谢大家的支持。

aikuic 发表于 2012-11-5 21:43:30

支持楼主,希望楼主早日完成这个伟大工作

liyinping 发表于 2012-11-5 21:44:49

{:1106_362:}感谢楼主,这么好的资料和我们分享,O(∩_∩)O谢谢!

pdsnzk1972 发表于 2012-11-5 21:47:57

支持下啊,楼主辛苦,希望能早日看到电子版的文件。

liyinping 发表于 2012-11-5 21:47:58

期待成果,我也很想出一份力,但是我的英语翻译真的不能拿来去出版啊{:1106_362:}

Horse 发表于 2012-11-5 21:58:10

liyinping 发表于 2012-11-5 21:47 static/image/common/back.gif
期待成果,我也很想出一份力,但是我的英语翻译真的不能拿来去出版啊

非常感谢了。有心意就不错了。
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