化工过程模拟:绿色、节能与精密控制:green, energy saving and precise control

本书特色

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《Chemical Process Simulation》将研究生学术思维训练与过程模拟实践相结合,旨在提高研究生的科学认知与工程实践能力。本书利用GROMACS, Materials Studio, Aspen Plus, MATLAB等软件,从分子动力学、相平衡、稳态模拟及动态控制等方面,重点阐述化工过程模拟的绿色、节能与精密控制技术。本书共11章内容,第1章主要介绍汽液平衡和液液平衡实验数据的回归,第2章主要介绍离子液体相行为及其热力学性质的预测,离子液体在分离混合物方面的应用,第3~5章主要介绍过程强化与集成方面的实例,主要包括膜分离、热集成、热耦合、热泵隔壁塔精馏技术,第6~11章主要介绍了萃取精馏、变压精馏、间歇精馏及反应精馏等精馏过程的动态控制案例。

《Chemical Process Simulation》可作为高等院校化工等相关专业研究生的教学参考书,也可供从事化工过程开发与设计的工程技术人员参考。

《Chemical Process Simulation》将研究生学术思维训练与过程模拟实践相结合,旨在提高研究生的科学认知与工程实践能力。本书利用GROMACS, Materials Studio, Aspen Plus, MATLAB等软件,从分子动力学、相平衡、稳态模拟及动态控制等方面,重点阐述化工过程模拟的绿色、节能与精密控制技术。本书共11章内容,第1章主要介绍汽液平衡和液液平衡实验数据的回归,第2章主要介绍离子液体相行为及其热力学性质的预测,离子液体在分离混合物方面的应用,第3~5章主要介绍过程强化与集成方面的实例,主要包括膜分离、热集成、热耦合、热泵隔壁塔精馏技术,第6~11章主要介绍了萃取精馏、变压精馏、间歇精馏及反应精馏等精馏过程的动态控制案例。

《Chemical Process Simulation》可作为高等院校化工等相关专业研究生的教学参考书,也可供从事化工过程开发与设计的工程技术人员参考。

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目录

Chapter 1 Simulation of Vapor-liquid and Liquid-liquid Equilibrium for Binary/ Ternary Systems1.1 Introduction / 11.2 Data Regression of Binary System / 11.3 Data Regression of Ternary System by NRTL / 81.4 Data Regression of Ternary System by UNIQUAC / 11References / 13  Chapter 2 Application of Green Solvents in Absorption and Extraction2.1 Introduction / 142.2 Molecular Dynamics Simulation / 142.2.1 Generating GROMACS Supported Files / 152.2.2 Defining the Unit Box and Filling Solvent / 202.2.3 Energy Minimization / 222.2.4 NVT Balance / 242.2.5 NPT Balance / 262.2.6 Finishing MD / 272.2.7 Analysis / 282.3 Simulation of Extractive Distillation Using the Ionic Liquid / 302.3.1 Analysis of Correlation Model / 302.3.2 Definition of the Ionic Liquid in Aspen Plus / 322.4 Simulation of CO2 Absorption Using the Ionic Liquid / 372.4.1 Calculation of σ-profile Value / 382.4.2 Definition of the Ionic Liquid in Aspen Plus / 432.4.3 Simulation of CO2 Capture Using the Ionic Liquid / 442.5 Simulation of Extractive Distillation Using Deep Eutectic Solvents / 492.5.1 Definition of Deep Eutectic Solvents in Aspen Plus / 502.5.2 Process Simulation / 52References / 54  Chapter 3 Membrane Separation Process3.1 Introduction / 563.2 Principle of Membrane Separation / 563.3 Separation of DMSO-water Using Membrane / 57References / 64  Chapter 4 Heat-integration and Thermally Coupled Distillation4.1 Introduction / 654.2 Steady-state Simulation of THF-methanol System with Heat- integration / 664.2.1 Simulation without Heat-integration / 664.2.2 Simulation with Partial Heat-integration / 704.2.3 Simulation with Full Heat-integration / 734.3 Thermally Coupled Distillation Process / 764.4 Energy-saving Thermally Coupled Ternary Extractive Distillation Process / 78References / 86  Chapter 5 Heat Pump Distillation for Close-boiling Mixture5.1 Introduction / 885.2 Main Forms of Heat Pump Distillation / 885.3 Heat Pump Distillation Process of Binary System Close-boiling Mixture / 90References / 99  Chapter 6 Energy-saving Side-stream Extractive Distillation Process6.1 Introduction / 1006.2 Steady-state Design of Side-stream Extractive Distillation / 1006.3 Dynamic Control of Side-stream Extractive Distillation / 1016.3.1 Control Structure with Side-stream Composition/Temperature Cascade Connection / 1056.3.2 Control Structure with S/F and Composition Controller Connection / 1056.3.3 Improved Dynamic Control Structure / 107References / 112  Chapter 7 Pressure-swing Distillation for Minimum-boiling Azeotropes7.1 Introduction / 1137.2 Converting from Steady-state to Dynamic Simulation / 1137.3 Control Structures of the Process without Heat-integration / 1167.3.1 Basic Control Structure / 1167.3.2 QR/F1 Control Structure / 1277.3.3 Control Structures of the Process with FullHeat-integration / 128References / 130  Chapter 8 Ternary Extractive Distillation System Using Mixed Entrainer8.1 Introduction / 1328.2 Converting from Steady-state to Dynamic Simulation / 1328.3 Dynamic Control of Ternary Extractive Distillation Process Using Single Solvent / 1358.3.1 Basic Control Structure / 1358.3.2 Dual Temperature Control Structure / 1408.3.3 Composition with Q R/F Control Structure / 1428.4 Dynamic Control of Ternary Extractive Distillation Process Using Mixed Entrainer / 1458.4.1 Basic Control Structure / 1458.4.2 Composition with Q R/F Control Structure / 1468.5 Comparisons of the Dynamic Performances of Two Processes / 148References / 152  Chapter 9 Hybrid Process Including Extraction and Distillation9.1 Introduction / 1539.2 Solvent Selection / 1539.3 Simulation of the Extraction Combined with Distillation Process / 1559.3.1 Extraction Combined with Heterogeneous Azeotropic Distillation Process (LEHAD) / 1559.3.2 Extraction Combined with Extractive Distillation Process (LEED) / 1609.4 Dynamic Simulation of Hybrid Extraction-distillation / 1649.4.1 Selection of Temperature-sensitive Trays / 1649.4.2 Dynamic Control of the LEHAD Process / 1679.4.3 Dynamic Control of the LEED Process / 1749.5 Energy-saving Hybrid Process with Mixed Solvent / 1819.6 Dynamics of Hybrid Process with Mixed Solvent / 1859.6.1 Selection of Temperature-sensitive Trays / 1859.6.2 Control Structure with Fixed Reflux Ratio / 187References / 190  Chapter 10 Batch Distillation Integrated with Quasi-continuous Process10.1 Introduction / 19110.2 Feasibility of Pressure-swing Batch Distillation Based on the Ternary Residue Curve Maps / 19110.3 Double Column Batch Stripper Process / 19310.3.1 Design of Double Column Batch Stripper Process / 19310.3.2 Control of Double Column Batch Stripper Process / 19610.4 Triple Column Process / 20110.4.1 Design of Triple Column Process / 20110.4.2 Control of Triple Column Process / 202References / 206  Chapter 11 Simulation of Chemical Reaction Process Based on Reaction Kinetics11.1 Introduction / 20711.2 Continuously Stirred Tank Reactor / 20811.3 Simulation of Cyclohexanone Ammoximation Process / 20911.3.1 Steady-state Simulation of Cyclohexanone Ammoximation Process / 20911.3.2 Dynamic Simulation of Cyclohexanone Ammoximation Process / 209References / 225 

封面

化工过程模拟:绿色、节能与精密控制:green, energy saving and precise control

书名:化工过程模拟:绿色、节能与精密控制:green, energy saving and precise control

作者:王英龙,崔培哲,田文德编著

页数:225页

定价:¥59.0

出版社:化学工业出版社

出版日期:2019-11-01

ISBN:9787122357243

PDF电子书大小:61MB 高清扫描完整版

百度云下载:http://www.chendianrong.com/pdf

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