Steady‐State Composition Profiles in Mixed Molten Salt Electrochemical Devices: II . Molten Carbonate Fuel Cell Analogs

1979 ◽  
Vol 126 (4) ◽  
pp. 527-534 ◽  
Author(s):  
C. E. Vallet ◽  
J. Braunstein
Keyword(s):  
Steady State ◽  
Fuel Cell ◽  
Molten Salt ◽  
Molten Carbonate Fuel Cell ◽  
Molten Carbonate ◽  
Composition Profiles ◽  
Electrochemical Devices ◽  
Carbonate Fuel Cell ◽  
State Composition

Characteristics of Solid Fuel Oxidation in a Molten Carbonate Fuel Cell

2016 ◽  
Vol 7 (2) ◽  
pp. 91-96
Author(s):  
Choong-Gon Lee ◽  
Yu-Jeong Kim ◽  
Tae-Kyun Kim ◽  
Sang-Woo Lee
Keyword(s):  
Fuel Cell ◽  
Solid Fuel ◽  
Molten Carbonate Fuel Cell ◽  
Molten Carbonate ◽  
Fuel Oxidation ◽  
Carbonate Fuel Cell

ChemInform Abstract: MOLTEN CARBONATE FUEL CELL CATHODE MATERIALS STUDY

1985 ◽  
Vol 16 (7) ◽  
Author(s):  
C. E. BAUMGARTNER ◽  
R. H. ARENDT ◽  
C. D. IACOVANGELO ◽  
B. R. KARAS
Keyword(s):  
Fuel Cell ◽  
Cathode Materials ◽  
Molten Carbonate Fuel Cell ◽  
Molten Carbonate ◽  
Fuel Cell Cathode ◽  
Carbonate Fuel Cell ◽  
Cell Cathode

scholarly journals A novel hybrid liquefied natural gas process with absorption refrigeration integrated with molten carbonate fuel cell

2021 ◽  
Author(s):  
Mehdi Mehrpooya ◽  
Parimah Bahramian ◽  
Fathollah Pourfayaz ◽  
Hadi Katooli ◽  
Mostafa Delpisheh
Keyword(s):  
Energy Consumption ◽  
Fuel Cell ◽  
Natural Gas ◽  
Hybrid System ◽  
Liquefied Natural Gas ◽  
Molten Carbonate Fuel Cell ◽  
Cooling Load ◽  
Absorption Refrigeration ◽  
Molten Carbonate ◽  
Carbonate Fuel Cell

Abstract The production of liquefied natural gas (LNG) is a high energy-consuming process. The study of ways to reduce energy consumption and consequently to reduce operational costs is imperative. Toward this purpose, this study proposes a hybrid system adopting a mixed refrigerant for the liquefaction of natural gas that is precooled with an ammonia/water absorption refrigeration (AR) cycle utilizing the exhaust heat of a molten carbonate fuel cell, 700°C and 2.74 bar, coupled with a gas turbine and a bottoming Brayton super-critical carbon dioxide cycle. The inauguration of the ammonia/water AR cycle to the LNG process increases the cooling load of the cycle by 10%, providing a 28.3-MW cooling load duty while having a 0.45 coefficient of performance. Employing the hybrid system reduces energy consumption, attaining 85% overall thermal efficiency, 53% electrical efficiency and 35% fuel cell efficiency. The hybrid system produces 6300 kg.mol.h−1 of LNG and 146.55 MW of electrical power. Thereafter, exergy and sensitivity analyses are implemented and, accordingly, the fuel cell had an 83% share of the exergy destruction and the whole system obtained a 95% exergy efficiency.

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