Enhanced trace pollutants removal efficiency and hydrogen production in rice straw gasification using hot gas cleaning system

2019 ◽  
Vol 44 (6) ◽  
pp. 3363-3372 ◽  
Author(s):  
Ngo Thi Ngoc Lan Thao ◽  
Kung-Yuh Chiang ◽  
Hou-Peng Wan ◽  
Wei-Chun Hung ◽  
Chiung-Fang Liu
2014 ◽  
Vol 12 (10) ◽  
pp. 1005-1011 ◽  
Author(s):  
Kung-Yuh Chiang ◽  
Ming-Hui Lin ◽  
Cheng-Han Lu ◽  
Kuang-Li Chien ◽  
Yun-His Lin

Energy ◽  
2013 ◽  
Vol 50 ◽  
pp. 47-53 ◽  
Author(s):  
Kung-Yuh Chiang ◽  
Cheng-Han Lu ◽  
Ming-Hui Lin ◽  
Kuang-Li Chien

1994 ◽  
Vol 116 (2) ◽  
pp. 338-344 ◽  
Author(s):  
R. A. Newby ◽  
R. L. Bannister

The United States electric industry is entering a period where growth and the aging of existing plants will mandate a decision on whether to repower, add capacity, or do both. The power generation cycle of choice, today, is the combined cycle that utilizes the Brayton and Rankine cycles. The combustion turbine in a combined cycle can be used in a repowering mode or in a greenfield plant installation. Today’s fuel of choice for new combined cycle power generation is natural gas. However, due to a 300-year supply of coal within the United States, the fuel of the future will include coal. Westinghouse has supported the development of coal-fueled gas turbine technology over the past thirty years. Working with the U.S. Department of Energy and other organizations, Westinghouse is actively pursuing the development and commercialization of several coal-fueled processes. To protect the combustion turbine and environment from emissions generated during coal conversion (gasification/combustion) a gas cleanup system must be used. This paper reports on the status of fuel gas cleaning technology and describes the Westinghouse approach to developing an advanced hot gas cleaning system that contains component systems that remove particulate, sulfur, and alkali vapors. The basic process uses ceramic barrier filters for multiple cleaning functions.


Author(s):  
R. A. Newby ◽  
R. L. Bannister

The United States electric industry is entering a period where growth and the aging of existing plants will mandate a decision on whether to repower, add capacity or do both. The power generation cycle of choice, today, is the combined cycle that utilizes the Brayton and Rankine cycles. The combustion turbine in a combined cycle can be used in a repowering mode or in a greenfield plant installation. Today’s fuel of choice for new combined cycle power generation is natural gas. However, due to a 300-year supply of coal within the United States, the fuel-of-the future will include coal. Westinghouse has supported the development of coal-fueled gas turbine technology over the past thirty years. Working with the U.S. Department of Energy and other organizations, Westinghouse is actively pursuing the development and commercialization of several coal-fueled processes. To protect the combustion turbine and environment from emissions generated during coal conversion (gasification/combustion) a gas cleanup system must be used. This paper reports on the status of fuel gas cleaning technology and describes the Westinghouse approach to developing an advanced hot gas cleaning system that contains component systems that remove particulate, sulfur, and alkali vapors. The basic process uses ceramic barrier filters for multiple cleaning functions.


Catalysts ◽  
2021 ◽  
Vol 11 (10) ◽  
pp. 1231
Author(s):  
Grazyna Straczewski ◽  
Robert Mai ◽  
Uta Gerhards ◽  
Krassimir Garbev ◽  
Hans Leibold

Tar in the product gas of biomass gasifiers reduces the efficiency of gasification processes and causes fouling of system components and pipework. Therefore, an efficient tar conversion in the product gas is a key step of effective and reliable syngas production. One of the most promising approaches is the catalytic decomposition of the tar species combined with hot syngas cleaning. The catalyst must be able to convert tar components in the synthesis gas at temperatures of around 700 °C downstream of the gasifier without preheating. A Ni-based doped catalyst with high activity in tar conversion was developed and characterized in detail. An appropriate composition of transition metals was applied to minimize catalyst coking. Precious metals (Pt, Pd, Rh, or a combination of two of them) were added to the catalyst in small quantities. Depending on the hot gas cleaning system used, both transition metals and precious metals were co-impregnated on pellets or on a ceramic filter material. In the case of a pelletized-type catalyst, the hot gas cleaning system revealed a conversion above 80% for 70 and 110 h. The catalyst composed of Ni, Fe, and Cr oxides, promoted with Pt and impregnated on a ceramic fiber filter composed of Al2O3(44%)/SiO2(56%), was the most active catalyst for a compact cleaning system. This catalyst was catalytically active with a naphthalene conversion of around 93% over 95 h without catalyst deactivation.


2014 ◽  
Vol 117 ◽  
pp. 17-22 ◽  
Author(s):  
Fengkui Yin ◽  
Jianglong Yu ◽  
Sushil Gupta ◽  
Shaoyan Wang ◽  
Dongmei Wang ◽  
...  

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