Flow Uniformity of Catalytic Burner for Off-Gas Combustion of Molten Carbonate Fuel Cell

Author(s):  
Sangseok Yu ◽  
Seokyeon Im ◽  
Young Duk Lee ◽  
Kook Young Ahn ◽  
Sangmin Lee

A catalytic combustor is a device to burn out the fuel by surface combustion that is used for the combustion of anode off-gas of molten carbonate fuel cell. By employing the catalytic combustor, the purified exhaust gas is able to be recirculated into the cathode channel for CO2 supply to improve thermal efficiency. The design of catalytic combustor depends on many parameters but the flow uniformity is particularly important during the emergency shut-down of fuel cell stack. Right before the temperature control of catalytic combustor is not yet activated, the catalytic combustor should burn out more than two times of rated amount of fuel flow rate. At the over-loaded condition, assurance of flow uniformity at the inlet of catalytic combustor can reduce the damage of catalytic burner caused by local hot zone. In this study, the flow uniformity of the catalytic combustor is investigated in two steps such as preliminary step with model combustor and main analysis step with practical 250 kW catalytic combustor. The 0.5 kW and 5 kW class combustors are applied for preliminary step. In preliminary step, the model combustor is used to determine supporting matters for the flow uniformity. Inlet direction of mixing chamber below the catalytic combustor is also examined in the preliminary step. In the main analysis step, flow uniformity of scale-up combustor has been examined with selected supporting matter and inlet direction into mixing chamber. Geometric and operating parameters are investigated. In particular, the flow rate at off-design operating condition has been examined.

Author(s):  
Sangmin Lee ◽  
Kook Young Ahn ◽  
Young Duk Lee ◽  
Jaeyoung Han ◽  
Seokyeon Im ◽  
...  

A catalytic combustor is a device to burn off fuel by surface combustion that is used for the combustion of anode off-gas of molten carbonate fuel cells by employing the catalytic combustor. Purified exhaust gas can be recirculated into the cathode channel for CO2 supply to improve thermal efficiency. The design of a catalytic combustor depends on many parameters, but flow uniformity is particularly important during the emergency shut-down of a fuel cell stack. Before the temperature control of a catalytic combustor is activated, the catalytic combustor should burn off more than two times the rated amount of the fuel flow rate. Under overload conditions, assurance of flow uniformity at the inlet of the catalytic combustor can reduce damage to the catalytic burner that can be caused by a local hot zone. In this study, flow uniformity of the catalytic combustor was investigated in two steps: a preliminary step with a model combustor and a main analysis step with a practical 250 kW catalytic combustor. Models of the 0.5 and 5 kW class combustors were used in the preliminary step. In the preliminary step the model combustors were used to determine supporting matters for flow uniformity. The inlet direction of the mixing chamber below the catalytic combustor was also examined in the preliminary step. In the main analysis step the flow uniformity of the scale-up combustor was examined with selected supporting matter and inlet direction into the mixing chamber. Geometric and operating parameters were investigated. In particular, the flow rate under off-design operating conditions was examined.


2016 ◽  
Vol 7 (2) ◽  
pp. 91-96
Author(s):  
Choong-Gon Lee ◽  
Yu-Jeong Kim ◽  
Tae-Kyun Kim ◽  
Sang-Woo Lee

1985 ◽  
Vol 16 (7) ◽  
Author(s):  
C. E. BAUMGARTNER ◽  
R. H. ARENDT ◽  
C. D. IACOVANGELO ◽  
B. R. KARAS

Author(s):  
Mehdi Mehrpooya ◽  
Parimah Bahramian ◽  
Fathollah Pourfayaz ◽  
Hadi Katooli ◽  
Mostafa Delpisheh

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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