Simulation of CO2 capture from natural gas by cyclic pressure swing adsorption process using activated carbon

被引:14
作者
Lin, Haitao [1 ]
Lu, Jianbo [2 ]
Abed, Azher M. [3 ]
Nag, Kaushik [4 ]
Fayed, Mohamed [4 ]
Deifalla, Ahmed [5 ]
Mahfouz, Abdullah S. Bin [6 ]
Galal, Ahmed M. [7 ,8 ]
机构
[1] Yuxi Normal Univ, Yuxi 653100, Yunnan, Peoples R China
[2] Nanning Normal Univ, Guangxi Key Lab Human machine Interact & Intellige, Nanning 530001, Peoples R China
[3] Al Mustaqbal Univ Coll, Air Conditioning & Refrigerat Tech Engn Dept, Babylon 51001, Iraq
[4] Amer Univ Middle East, Coll Engn & Technol, Kuwait, Kuwait
[5] Future Univ Egypt, New Cairo 11835, Egypt
[6] Univ Jeddah, Dept Chem Engn, Asfan Rd, Jeddah 23890, Saudi Arabia
[7] Prince Sattam Bin Abdulaziz Univ, Coll Engn Wadi Alddawasir, Dept Mech Engn, Al Kharj, Saudi Arabia
[8] Mansoura Univ, Fac Engn, Prod Engn & Mech Design Dept, PO 35516, Mansoura 35516, Egypt
关键词
Adsorption; PSA-Activated carbon; CO2; capture; Simulation; METHANE; 13X;
D O I
10.1016/j.chemosphere.2023.138583
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This work presented modeling and simulation of CO2 from natural gas. One of the most promising technologies is Pressure Swing Adsorption (PSA), which is an energy-efficient and cost-effective process for separating and capturing CO2 from industrial processes and power plants. This paper provides an overview of the PSA process and its application for CO2 capture, along with a discussion of its advantages, limitations, and future research directions. This process is pressure swing adsorption (PSA) with four adsorption beds. The adsorption bed col-umns fill with activated carbon as adsorbent. In this simulation momentum, mass and energy balance are solved simultaneously. The process was designed with two beds in adsorption conditions and the other two beds in desorption conditions. The desorption cycle includes blow-down and purge steps. The linear driving force (LDF) estimates the adsorption rate in modeling this process. The extended Langmuir isotherm is used for the equilibrium between solid and gas phases. The temperature changes by heat transfer from the gas phase to solid and axial heat dispersion. The set of partial differential equations is solved using implicit finite difference.
引用
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页数:8
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