Influence of Catalyst Weight/Biomass Flow Rate Ratio on Gas Production in the Catalytic Pyrolysis of Pine Sawdust at Low Temperatures

Pine sawdust catalytic pyrolysis has been studied in a fluidized bed at temperatures of 650 and 700 °C. The experimental work was carried out in a bench-scale plant based on Waterloo Fast Pyrolysis Process (WFPP) technology. The Ni−Al catalyst used was prepared by coprecipitation with a molar ratio...

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Veröffentlicht in:Industrial & engineering chemistry research 1998-10, Vol.37 (10), p.3812-3819
Hauptverfasser: Garcia, Lucia, Salvador, María L, Arauzo, Jesús, Bilbao, Rafael
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container_end_page 3819
container_issue 10
container_start_page 3812
container_title Industrial & engineering chemistry research
container_volume 37
creator Garcia, Lucia
Salvador, María L
Arauzo, Jesús
Bilbao, Rafael
description Pine sawdust catalytic pyrolysis has been studied in a fluidized bed at temperatures of 650 and 700 °C. The experimental work was carried out in a bench-scale plant based on Waterloo Fast Pyrolysis Process (WFPP) technology. The Ni−Al catalyst used was prepared by coprecipitation with a molar ratio 1:2 (Ni−Al) and calcined at 750 °C for 3 h. The catalyst was not reduced prior to the biomass reaction. The influence of the catalyst weight/biomass flow rate ratio (W/mb) on the product distribution and on the quality of the gas product obtained was analyzed. An increase of the W/mb ratio increases the total gas yield and diminishes the liquid yield. When the W/mb ratio increases, H2 and CO yields increase while CO2, CH4, and C2 yields decrease. For W/mb ratios ≥ 0.4 h, no significant modifications are observed on the initial yields of different gases, and it is confirmed that under these conditions the initial gas composition is similar to that for thermodynamic equilibrium. For W/mb ratios < 0.4 h, a simple first-order kinetic equation has been suggested for H2 and CO formation.
doi_str_mv 10.1021/ie9801960
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Eng. Chem. Res</addtitle><description>Pine sawdust catalytic pyrolysis has been studied in a fluidized bed at temperatures of 650 and 700 °C. The experimental work was carried out in a bench-scale plant based on Waterloo Fast Pyrolysis Process (WFPP) technology. The Ni−Al catalyst used was prepared by coprecipitation with a molar ratio 1:2 (Ni−Al) and calcined at 750 °C for 3 h. The catalyst was not reduced prior to the biomass reaction. The influence of the catalyst weight/biomass flow rate ratio (W/mb) on the product distribution and on the quality of the gas product obtained was analyzed. An increase of the W/mb ratio increases the total gas yield and diminishes the liquid yield. When the W/mb ratio increases, H2 and CO yields increase while CO2, CH4, and C2 yields decrease. For W/mb ratios ≥ 0.4 h, no significant modifications are observed on the initial yields of different gases, and it is confirmed that under these conditions the initial gas composition is similar to that for thermodynamic equilibrium. 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Eng. Chem. Res</addtitle><date>1998-10-05</date><risdate>1998</risdate><volume>37</volume><issue>10</issue><spage>3812</spage><epage>3819</epage><pages>3812-3819</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><coden>IECRED</coden><abstract>Pine sawdust catalytic pyrolysis has been studied in a fluidized bed at temperatures of 650 and 700 °C. The experimental work was carried out in a bench-scale plant based on Waterloo Fast Pyrolysis Process (WFPP) technology. The Ni−Al catalyst used was prepared by coprecipitation with a molar ratio 1:2 (Ni−Al) and calcined at 750 °C for 3 h. The catalyst was not reduced prior to the biomass reaction. The influence of the catalyst weight/biomass flow rate ratio (W/mb) on the product distribution and on the quality of the gas product obtained was analyzed. An increase of the W/mb ratio increases the total gas yield and diminishes the liquid yield. When the W/mb ratio increases, H2 and CO yields increase while CO2, CH4, and C2 yields decrease. For W/mb ratios ≥ 0.4 h, no significant modifications are observed on the initial yields of different gases, and it is confirmed that under these conditions the initial gas composition is similar to that for thermodynamic equilibrium. For W/mb ratios &lt; 0.4 h, a simple first-order kinetic equation has been suggested for H2 and CO formation.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/ie9801960</doi><tpages>8</tpages></addata></record>
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source ACS_美国化学学会期刊(与NSTL共建)
subjects 09 BIOMASS FUELS
Agriculture, rearing and food industries wastes
Applied sciences
Biomass
CARBON DIOXIDE
CATALYSTS
CHEMICAL REACTION YIELD
Energy
Exact sciences and technology
FLOW RATE
KINETIC EQUATIONS
METHANE
Natural energy
Pollution
PYROLYSIS
SYNTHESIS GAS
Wastes
WOOD WASTES
title Influence of Catalyst Weight/Biomass Flow Rate Ratio on Gas Production in the Catalytic Pyrolysis of Pine Sawdust at Low Temperatures
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