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  • 化工過程模擬:綠色,節能與精密控制(Chemical Process Simulation
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    【作者】 王英龍、崔培哲、田文德 
    【出版社】化學工業出版社 
    【ISBN】9787122357243
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    內容介紹



    ISBN編號:9787122357243
    書名:化工過程模擬-綠色、節能與精密控制 化工過程模擬-綠色、節能與精密控制
    作者:王英龍、崔培哲、田文德

    代碼:59
    開本:16開
    是否是套裝:否

    出版社名稱:化學工業出版社

        
        
    "

    化工過程模擬:綠色,節能與精密控制(Chemical Pro

    作  者: 王英龍、崔培哲、田文德 編著 著
    size="731x8"
    定  價: 59
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    出?版?社: 化學工業出版社
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    出版日期: 2019年11月01日
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    頁  數: 225
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    裝  幀: 平裝
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    ISBN: 9787122357243
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    目錄
    ●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
    內容虛線

    內容簡介

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    《Chemical Process Simulation》將研究生學術思維訓練與過程模擬實踐相結合,旨在提高研究生的科學認知與工程實踐能力。本書利用GROMACS, Materials Studio, Aspen Plus, MATLAB等軟件,從分子動力學、相平衡、穩態模擬及動態控制等方面,重點闡述化工過程模擬的綠色、節能與精密控制技術。本書共11章內容,章主要介紹汽液平衡和液液平衡實驗數據的回歸,第2章主要介紹離子液體相行為及其熱力學性質的預測,離子液體在分離混合物方面的應用,第3~5章主要介紹過程強化與集成方面的實例,主要包括膜分離、熱集成、熱耦合、熱泵隔壁塔精餾技術,第6~11章主要介紹了萃取精餾、變壓精餾、間歇精餾及反應精餾等精餾過程的動態控制案例。《Chemical Process Simulation》可作為高等院校化工等相關專業研究生的教學參考書,也可供從事化工過程開發與設......

    作者簡介

    王英龍、崔培哲、田文德 編著 著

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