2250-h long term operation of a water gas shift pilot plant processing tar-rich product gas from an industrial scale dual fluidized bed biomass steam gasification plant
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- 作者：Michael Krausslera ; michael.kraussler@bioenergy2020.eu" class="auth_mail" title="E-mail the corresponding author ; Matthias Binderb ; Hermann Hofbauera ; b
- 关键词：Biomass ; Dual fluidized bed ; Steam gasification ; Water gas shift ; Hydrogen
- 刊名：International Journal of Hydrogen Energy
- 出版年：2016
- 出版时间：27 April 2016
- 年：2016
- 卷：41
- 期：15
- 页码：6247-6258
- 全文大小：1228 K
文摘
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A WGS pilot plant was operated with tar-rich product gas from dual fluidized bed biomass steam gasification.
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The WGS pilot plant was continuously operated for about 2250 h.
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A commercial Fe/Cr based catalyst was employed.
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No deactivation of the catalyst could be observed during the about 2250 h of operation.
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The volumetric CO content in the product gas could be lowered from about 25% to below 2%.