Waste to wheels: Performance comparison between pressure swing adsorption and amine-absorption technologies for upgrading biogas containing hydrogen sulfide to fuel grade standards

被引:19
作者
Abd, Ammar Ali [1 ,4 ]
Othman, Mohd Roslee [1 ]
Helwani, Zuchra [2 ]
Kim, Jinsoo [3 ]
机构
[1] Univ Sains Malaysia, Sch Chem Engn, Nibong Tebal 14300, Pulau Pinang, Malaysia
[2] Univ Riau, Dept Chem Engn, Pekanbaru 28293, Indonesia
[3] Kyung Hee Univ, Dept Chem Engn Integrated Engn, 1732 Doegyeong Daero, Yongin 17104, Gyeonggi Do, South Korea
[4] Al Qasim Green Univ, Coll Engn, Babylon 51002, Iraq
关键词
Biogas upgrading; Pressure swing adsorption; Amine absorption; Piperazine; MDEA; CO; 2; separation; CARBON-DIOXIDE ABSORPTION; CO2; CAPTURE; N-METHYLDIETHANOLAMINE; SENSITIVITY-ANALYSIS; TECHNOECONOMIC ANALYSIS; REACTION-KINETICS; AQUEOUS-SOLUTIONS; GAS; REMOVAL; MDEA;
D O I
10.1016/j.energy.2023.127060
中图分类号
O414.1 [热力学];
学科分类号
摘要
Amine-absorption and pressure swing adsorption (PSA) technologies have been regarded as attractive methods to upgrade biogas by separating acid gases such as CO2 and H2S from its main component, CH4. This paper com-pares the separation performance and energy consumption by pressure swing adsorption and amine-absorption processes in upgrading biogas containing 39.9% CO2, 0.1% H2S, and 60% CH4. PSA and amine-absorption processes were emulated using Aspen Adsorption and Aspen Hysys platforms and validated from experimental data. The results reveal that amine-absorption technology was favorable in terms of purity and recovery of products in both streams. The optimum points of the process with desirability of 99.9% were at 0.1% H2S content, 30% CO2 content, 1% piperazine concentration, and 50% MDEA concentration with biomethane purity (99.64%) and recovery (94.84%) in the product stream, and acid gases purity (94.84%) and recovery (99.97%) in the waste stream. In term of energy consumption, however, the pressure swing adsorption process recorded a lower energy requirement of 0.178 kW/molCH4 at comparable biomethane purity of 96.2% and lower methane recovery of 80% with subsequently lower acid gases purity (85.5%) and recovery (86.7%).
引用
收藏
页数:17
相关论文
共 75 条
  • [71] Influence of stripper operating parameters on the performance of amine absorption systems for post-combustion carbon capture: Part I. High pressure strippers
    Warudkar, Sumedh S.
    Cox, Kenneth R.
    Wong, Michael S.
    Hirasaki, George J.
    [J]. INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2013, 16 : 342 - 350
  • [72] Sustainable Waste-to-Energy Development in Malaysia: Appraisal of Environmental, Financial, and Public Issues Related with Energy Recovery from Municipal Solid Waste
    Yong, Zi Jun
    Bashir, Mohammed J. K.
    Ng, Choon Aun
    Sethupathi, Sumathi
    Lim, Jun Wei
    Show, Pau Loke
    [J]. PROCESSES, 2019, 7 (10)
  • [73] Biogas upgrading process via low-temperature CO2 liquefaction and separation
    Yousef, Ahmed M.
    Eldrainy, Yehia A.
    El-Maghlany, Wael M.
    Attia, Abdelhamid
    [J]. JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING, 2017, 45 : 812 - 824
  • [74] Simulation and parametric analysis of CO2 capture from natural gas using diglycolamine
    Zahid, Umer
    Al Rowaili, Fayez Nasir
    Ayodeji, Mohammed Kazeem
    Ahmed, Usama
    [J]. INTERNATIONAL JOURNAL OF GREENHOUSE GAS CONTROL, 2017, 57 : 42 - 51
  • [75] Experimental Studies of Regeneration Heat Duty for CO2 Desorption from Aqueous DETA Solution in a Randomly Packed Column
    Zhang, Xu
    Fu, Kaiyun
    Liang, Zhiwu
    Yang, Zhen
    Rongwong, Wichitpan
    Na, Yanqing
    [J]. 12TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, GHGT-12, 2014, 63 : 1497 - 1503