Published January 2021 | Version v1
Journal article

Combined energy consumption and CO2 capture management: Improved acid gas removal process integrated with CO2 liquefaction

  • 1. School of Chemical Engineering, South China University of Technology, Guangzhou, 510640 (China)
  • 2. Centre of Excellence for Green Technology, University of Nottingham Malaysia Campus, Jalan Broga, 43500, Semenyih (Malaysia)
  • 3. Guangdong Key Laboratory of Green Chemical Products Technology, South China University of Technology, Guangzhou, 510640 (China)

Description

Highlights: • A novel Int-Rectisol process integrated with CO2 liquefaction was proposed. • The new process decreased energy consumption from 389.1 MJ to 204.3 MJ for capturing 1 kg of CO2. • The new process improved the CO2 capture rate from 46.7% to 85% and decreased the exergy destruction by 20.95 MW. • The new process reduced the capital investment and the total product cost by 12.4% and 8.7%, respectively. Energy management is always facing a trade-off among the constrains of efficiency, energy consumption and CO2 capture rate. For example, the Rectisol wash is a promising and efficient purification process for acid gas removal. However, this process has the problems of high cold energy consumption and low CO2 capture rate. To solve the problems, this paper proposed an improved integrated Rectisol (Int-Rectisol) process with CO2 partial liquefaction. This paper demonstrated how to comprehensively reduce the energy consumption by liquefying part of the CO2 from the treated syngas before absorption. The decreased CO2 concentration in the syngas consequently reduced the methanol solvent consumption and regeneration in the process. Meanwhile, less solvent circulation and regeneration further reduced the energy consumption of the overall process. Process modeling and simulation was conducted in Aspen Plus. The techno-economic performance was then evaluated and compared with the conventional process. The results showed that the solvent circulation in the Int-Rectisol process reduced by 46.5% and the energy consumption decreased from 389.1 MJ to 204.3 MJ for capturing 1 kg of CO2. Meanwhile, the CO2 capture rate also increased from 46.7% to 85%. The exergy analysis showed that the exergy destruction in the Int-Rectisol was 20.95 MW less than the Rectisol process. As for the economic benefit, the Int-Rectisol process reduced the total capital investment and the total product cost by 12.4% and 8.7%, respectively.

Availability note (English)

Available from http://dx.doi.org/10.1016/j.energy.2020.119032

Additional details

Identifiers

DOI
10.1016/j.energy.2020.119032;
PII
S0360544220321393;

Publishing Information

Journal Title
Energy (Oxford)
Journal Volume
215
Journal Page Range
vp.
ISSN
0360-5442
CODEN
ENEYDS

Optional Information

Copyright
Copyright (c) 2020 Elsevier Ltd. All rights reserved.