Optimization of an Existing 130 Tonne per Day CO2 Capture Plant from a Flue Gas Slipstream of a Coal Power Plant

被引:9
作者
Aboudheir, Ahmed [1 ]
Elmoudir, Walid [1 ]
机构
[1] HTC Purenergy Inc, Regina, SK S4P 0S7, Canada
来源
GHGT-11 | 2013年 / 37卷
关键词
CO2 capture plant; rate based modelling; optimization; coal power plant; food grade CO2;
D O I
10.1016/j.egypro.2013.06.026
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
An optimization study has been conducted on an existing 130 tonne per day carbon dioxide capture plant. A rate-based modelling approach is used to simulate the performance of the CO2 capture plant using actual plant process flow-sheet and operating parameters. The average absolute deviation of the predicted parameters from the measured parameters is within 8%. The developed rate-based model is then used to plan the operating conditions for optimum utilization of the resources. Based on the results obtained from the process optimization, it is possible to minimize the operating cost and enhance the production capacity of the CO2 capture plant at minimum additional investment. (C) 2013 The Authors. Published by Elsevier Ltd. Open access under CC BY-NC-ND license. Selection and/or peer-review under responsibility of GHGT
引用
收藏
页码:1509 / 1516
页数:8
相关论文
共 3 条
[1]  
Katti S. S., 1986, 65 ANN CONV GAS PROC
[2]   Rate-based modeling of reactive absorption of CO2 and H2S into aqueous methyldiethanolamine [J].
Pacheco, MA ;
Rochelle, GT .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (10) :4107-4117
[3]  
Sardar Hisham., 1984, AICHE ANN M SAN FRAN