CIESC Journal ›› 2025, Vol. 76 ›› Issue (S1): 297-308.DOI: 10.11949/0438-1157.20250089

• Energy and environmental engineering • Previous Articles    

Research on the coupled process of natural gas chemical absorption decarbonization and high temperature heat pump based on waste heat utilization

Ting HE(), Shuyang HUANG, Kun HUANG, Liqiong CHEN   

  1. School of Petroleum and Natural Gas Engineering, Southwest Petroleum University, Chengdu 610500, Sichuan, China
  • Received:2025-01-20 Revised:2025-03-25 Online:2025-06-26 Published:2025-06-25
  • Contact: Ting HE

基于余热利用的天然气化学吸收脱碳-高温热泵耦合流程研究

何婷(), 黄舒阳, 黄坤, 陈利琼   

  1. 西南石油大学石油与天然气工程学院,四川 成都 610500
  • 通讯作者: 何婷
  • 作者简介:何婷(1995—),女,博士,副研究员,heting199503@163.com

Abstract:

Chemical absorption using alcohol amine solution as an absorbent is currently the most widely used technology in the field of natural gas decarbonization, with advantages such as large processing capacity and good cycle stability. However, the regeneration process of chemical absorbent consumes a lot of energy. To reduce the energy consumption of chemical absorption decarbonization, a natural gas chemical absorption decarbonization high-temperature heat pump coupling process is proposed. Through the high-temperature heat pump, the waste heat from the wastewater in the gas field is used for the regeneration process of the decarbonization process, achieving energy conservation and carbon reduction. Modeling and parameter optimization of the decarbonization system using MDEA solution was carried out using Aspen HYSYS software. The results showed that the decarbonization rate of the optimized process was as high as 95%, and the unit comprehensive power consumption of the system was 0.3821 kW·h/kg CO2, which was 56.72% lower than the conventional decarbonization system (unit comprehensive power consumption of 0.8828kW·h/kg CO2).

Key words: decarbonization, high temperature heat pump, natural gas, waste heat utilization, chemical absorption, numerical simulation

摘要:

以醇胺溶液作为吸收剂的化学吸收是目前天然气脱碳领域使用最为广泛的技术,拥有处理量大、循环稳定性好等优点,但是化学吸收剂的再生过程能耗非常高。为降低化学吸收脱碳的能耗,提出了天然气化学吸收脱碳-高温热泵耦合流程,通过高温热泵将气田上的废水余热用于脱碳流程的再生过程,达到节能降碳。利用Aspen HYSYS软件对采用MDEA溶液的脱碳系统进行建模和参数优化。结果表明:经过优化,该套工艺的脱碳率高达95%,系统的单位综合能耗为0.3821 kW·h/kg CO2,相比于常规脱碳系统(单位综合能耗为0.8828 kW·h/kg CO2)降低了56.72%。

关键词: 脱碳, 高温热泵, 天然气, 余热利用, 化学吸收, 数值模拟

CLC Number: