Post-combustion CO2 capture from a natural gas combined cycle power plant using activated carbon adsorption

被引:114
作者
Jiang, L. [1 ]
Gonzalez-Diaz, A. [1 ]
Ling-Chin, J. [1 ]
Roskilly, A. P. [1 ]
Smallbone, A. J. [1 ]
机构
[1] Newcastle Univ, Sir Joseph Swan Ctr Energy Res, Newcastle Upon Tyne, Tyne & Wear, England
基金
英国工程与自然科学研究理事会;
关键词
Post-combustion CO2 capture; Natural gas combined cycle; Adsorption; Absorption; Economic analysis; PRESSURE SWING ADSORPTION; THERMODYNAMIC ANALYSIS; PHYSICAL ADSORPTION; DIOXIDE CAPTURE; SOLID SORBENTS; PERFORMANCE; STORAGE; DESIGN; SIMULATIONS; TECHNOLOGY;
D O I
10.1016/j.apenergy.2019.04.006
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
As fossil fuel power plants have emitted significant quantity of carbon dioxide (CO2) into the atmosphere which aggravates climate change, capturing and storing such emissions is key to mitigate the issue. An adsorption system based on a physical adsorbent i.e. activated carbon is first assessed to capture CO2 emissions from a natural gas combined cycle. Then a subcritical sequential supplementary firing combined cycle with CO2 capture is used to analyse the effect of CO2 concentration. Analyses are carried out in terms of power loss and thermal efficiency. To evaluate the advantages of post-combustion CO2 capture using activated carbon, results are compared with systems using a commercial absorbent, i.e. monoethanolamine and a chemical adsorbent i.e. polyethyleneimine/silica. The net efficiency of natural gas combined cycle using activated carbon increases slightly from 50.8% to 51.1% due to the lower regeneration temperature at 358 K. The performance of the system using PEI/silica is almost the same as that using activated carbon at 368 K. Although the thermal energy required to regenerate the activated carbon is relatively high, a significant improvement of net efficiency is observed with increased partial pressure. Economic analysis indicates that the systems using activated carbon is a competitive alternative for CO2 capture. It is concluded activated carbon is relatively more advantageous than monoethanolamine in terms of efficiency and cost, which could be further improved with enhanced heat and mass recovery.
引用
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页码:1 / 15
页数:15
相关论文
共 65 条
[11]  
Chen E., 2017, SENIOR DESIGN REPORT
[12]   Techno-economic analysis of a hybrid CO2 capture system for natural gas combined cycles with selective exhaust gas recirculation [J].
Diego, Maria Elena ;
Bellas, Jean-Michel ;
Pourkashanian, Mohamed .
APPLIED ENERGY, 2018, 215 :778-791
[13]   Making gas-CCS a commercial reality: The challenges of scaling up [J].
Diego, Maria Elena ;
Akram, Muhammad ;
Bellas, Jean-Michel ;
Finney, Karen N. ;
Pourkashanian, Mohamed .
GREENHOUSE GASES-SCIENCE AND TECHNOLOGY, 2017, 7 (05) :778-801
[14]  
DOE/NETL, 2013, CAP COST SCAL METH Q
[15]  
Franco F., 2012, EUROPEAN BEST PRACTI
[16]   Assessment of solid sorbents as a competitive post-combustion CO2 capture technology [J].
Glier, Justin C. ;
Rubin, Edward S. .
GHGT-11, 2013, 37 :65-72
[17]   Monoethanolamine degradation:: O2 mass transfer effects under CO2 capture conditions [J].
Goff, GS ;
Rochelle, GT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (20) :6400-6408
[18]  
Gonzalez Dfaz A, 2016, THESIS
[19]   Results from testing of Aker Solutions advanced amine solvents at CO2 Technology Centre Mongstad [J].
Gorset, Oddvar ;
Knudsen, Jacob Nygaard ;
Bade, Otto Morten ;
Askestad, Inga .
12TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, GHGT-12, 2014, 63 :6267-6280
[20]   Adsorbents for the post-combustion capture of CO2 using rapid temperature swing or vacuum swing adsorption [J].
Hedin, Niklas ;
Andersson, Linnea ;
Bergstrom, Lennart ;
Yan, Jinyue .
APPLIED ENERGY, 2013, 104 :418-433