作者：张培昆 著
页数：192
出版社：冶金工业出版社
出版日期：2024
ISBN：9787502497842
电子书格式：pdf/epub/txt
内容简介
本书旨在从材料、装置、系统及应用四个方面全面阐述变温吸附法知识，共分5章。书中介绍了吸附材料与气固吸附理论、吸附等温线方程、变温吸附装置、变温吸附系统以及变温吸附的应用与进展。本书既介绍了吸附剂材料、气固吸附理论以及吸附等温线等基础理论知识，又介绍了吸附器结构、加热方法、流程组织等密切联系工程实际的知识，有利于增强读者理论联系实际、分析和解决实际问题的能力。本书可作为化学工程、热能工程、环境工程等专业技术人员和工人的培训教材，也可供高等院校有关专业的师生参考。
作者简介
张培昆，北京科技大学副教授，硕士生导师，英国伯明翰大学访问学者。2011年毕业于北京科技大学，获博士学位。主要研究领域为能量的转换与高效利用，长期从事空气低温分离新工艺、吸附过程动力学与新型吸附循环、储能与节能新技术、低品位余热发电新循环、能源系统优化等方面研究与产业化工作。先后主持完成 自然科学青年基金、 重点研发计划子课题、 博士点基金等 和省部级项目；参编出版四部著作，发表论文20余篇，申请/授权 发明专利20余项；获 高等学校科技进步奖二等奖。
目录
Chapter 1 Adsorbent Materials
1.1 Common adsorbent types
1.1.1 Silica gel
1.1.2 Zeolite molecular sieve
1.1.3 Activated alumina
1.2 Equilibrium adsorption capacity
1.3 Adsorption isotherm models
1.3.1 Type I isotherm equations
1.3.2 Type Ⅱisotherm equations
References
Chapter 2 Extended Langmuir Model for Predicting Multilayer Adsorption
2.1 Model development
2.2 Example analysis
2.2.1 Example 1：water vapor adsorption on activated alumina
2.2.2 Example 2：water vapor adsorption on zeolite 13x
2.3 Conclusions
Nomenclature
References
Chapter 3 Principle and Numerical Simulation of Temperature Swing Adsorption Air Pre-purification Units
3.1 The principle of air pre-purification units
3.1.1 Adsorbers
3.1.2 The switching cycle
3.1.3 Heating method
3.2 Numerical simulation of air pre-purification process
3.2.1 Physical model
3.2.2 Conservation equations
3.2.3 Mass transfer calculations
3.2.4 Heat transfer calculations
3.2.5 Isotherm equation selection
3.2.6 Adsorption equilibrium data correlation
3.2.7 Initial conditions，boundary conditions
3.2.8 Cyclic steady-state conditions
3.2.9 Numerical method
3.3 Case study
3.3.1 Case introduction
3.3.2 Results and discussions
Nomenclature
References
Chapter 4 Operating Strategies of Temperature Swing Adsorption Air Pre-purification Units
4.1 Operation strategies of air pre-purification units for safe production
4.1.1 Analysis of the reasons for CO? exceeding the standard
4.1.2 Adsorbent bed filling and its effect on purification performance
4.2 Operation strategies of air pre-purification units for varying conditions
4.2.1 Analysis of the impact of adsorption inlet gas parameters
4.2.2 Analysis of the effects of regeneration inlet parameters
4.3 Potential multi-adsorber process organization for air pre-purification units
References
Chapter 5 Three-bed Temperature Swing Adsorption Process for Air Pre-purification
5.1 Process description
5.1.1 The two-bed TSA-APU and its energy-saving potential
1.1 Common adsorbent types
1.1.1 Silica gel
1.1.2 Zeolite molecular sieve
1.1.3 Activated alumina
1.2 Equilibrium adsorption capacity
1.3 Adsorption isotherm models
1.3.1 Type I isotherm equations
1.3.2 Type Ⅱisotherm equations
References
Chapter 2 Extended Langmuir Model for Predicting Multilayer Adsorption
2.1 Model development
2.2 Example analysis
2.2.1 Example 1：water vapor adsorption on activated alumina
2.2.2 Example 2：water vapor adsorption on zeolite 13x
2.3 Conclusions
Nomenclature
References
Chapter 3 Principle and Numerical Simulation of Temperature Swing Adsorption Air Pre-purification Units
3.1 The principle of air pre-purification units
3.1.1 Adsorbers
3.1.2 The switching cycle
3.1.3 Heating method
3.2 Numerical simulation of air pre-purification process
3.2.1 Physical model
3.2.2 Conservation equations
3.2.3 Mass transfer calculations
3.2.4 Heat transfer calculations
3.2.5 Isotherm equation selection
3.2.6 Adsorption equilibrium data correlation
3.2.7 Initial conditions，boundary conditions
3.2.8 Cyclic steady-state conditions
3.2.9 Numerical method
3.3 Case study
3.3.1 Case introduction
3.3.2 Results and discussions
Nomenclature
References
Chapter 4 Operating Strategies of Temperature Swing Adsorption Air Pre-purification Units
4.1 Operation strategies of air pre-purification units for safe production
4.1.1 Analysis of the reasons for CO? exceeding the standard
4.1.2 Adsorbent bed filling and its effect on purification performance
4.2 Operation strategies of air pre-purification units for varying conditions
4.2.1 Analysis of the impact of adsorption inlet gas parameters
4.2.2 Analysis of the effects of regeneration inlet parameters
4.3 Potential multi-adsorber process organization for air pre-purification units
References
Chapter 5 Three-bed Temperature Swing Adsorption Process for Air Pre-purification
5.1 Process description
5.1.1 The two-bed TSA-APU and its energy-saving potential
