Efficient electrochemical refrigeration power plant using natural gas with ∼100% CO2 capture

被引:18
作者
Al-musleh, Easa I. [1 ]
Mallapragada, Dharik S. [1 ]
Agrawal, Rakesh [1 ]
机构
[1] Purdue Univ, Sch Chem Engn, W Lafayette, IN 47907 USA
基金
美国国家科学基金会;
关键词
Liquefied natural gas; Carbon capture and sequestration; Solid oxide fuel cell; Refrigeration; CARBON CAPTURE; ENERGY; CYCLE; EMISSION; STORAGE; BIOGAS; MODEL;
D O I
10.1016/j.jpowsour.2014.09.184
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
We propose an efficient Natural Gas (NG) based Solid Oxide Fuel Cell (SOFC) power plant equipped with similar to 100% CO2 capture. The power plant uses a unique refrigeration based process to capture and liquefy CO2 from the SOFC exhaust. The capture of CO2 is carried out via condensation and purification using two rectifying columns operating at different pressures. The uncondensed gas mixture, comprising of relatively high purity unconverted fuel, is recycled to the SOFC and found to boost the power generation of the SOFC by 22%, when compared to a stand alone SOFC. If Liquefied Natural Gas (LNG) is available at the plant gate, then the refrigeration available from its evaporation is used for CO2 Capture and Liquefaction (CO2CL). If NG is utilized, then a Mixed Refrigerant (MR) vapor compression cycle is utilized for CO2CL. Alternatively, the necessary refrigeration can be supplied by evaporating the captured liquid CO2 at a lower pressure, which is then compressed to supercritical pressures for pipeline transportation. From rigorous simulations, the power generation efficiency of the proposed processes is found to be 70-76% based on lower heating value (LHV). The benefit of the proposed processes is evident when the efficiency of 73% for a conventional SOFC-Gas turbine power plant without CO2 capture is compared with an equivalent efficiency of 71.2% for the proposed process with CO2CL. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:130 / 141
页数:12
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