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首页> 外文期刊>Powder Technology: An International Journal on the Science and Technology of Wet and Dry Particulate Systems >Impact of K2CO3 catalyst loading on the CO2-gasification of Genesse raw coal and low-ash product
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Impact of K2CO3 catalyst loading on the CO2-gasification of Genesse raw coal and low-ash product

机译:K2CO3催化剂负载量对Genesse原煤和低灰分产品CO2气化的影响

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摘要

In this study, the effects of K2CO3 addition to Genesse sub-bituminous coal, before and after ash reduction, on conversion and gasification rate were investigated for CO2 gasification at 700-800 degrees C. For the uncatalyzed samples, no significant changes in gasification rate and char conversion were observed for the low-ash product (12 wt% ash) compared to the raw coal (33 wt% ash). However, with the addition of 10 wt potassium catalyst, the low-ash product exhibited a higher gasification rate than the raw coal. An increase of the catalyst loading up to 50 wt% resulted in a decline of the gasification rate for both coal samples. The activation energy increased with conversion and at higher K2CO3 loadings. Kinetic modeling showed that the extended-random pore model fits the experimental data well for both coal samples and supported the speculation that excess catalyst blocks pores, resulting a reduction in gasification rate. (C) 2016 Elsevier B.V. All rights reserved.
机译:在这项研究中,研究了在还原灰分之前和之后向Genesse次烟煤中添加K2CO3对转化率和气化速率的影响,该转化率和气化速率是在700-800摄氏度下CO2气化的。对于未催化的样品,气化速率没有显着变化与原煤(灰分33 wt%)相比,低灰分产品(灰分12 wt%)的碳转化率和焦炭转化率得到观察。然而,通过添加10wt%的钾催化剂,低灰分产品显示出比原煤更高的气化速率。两种煤样品中催化剂负载量增加至50 wt%导致气化速率下降。活化能随转化率的增加和在较高的K2CO3负载下增加。动力学建模表明,扩展随机孔隙模型非常适合两种煤样品的实验数据,并支持推测催化剂过量堵塞孔隙,导致气化速率降低。 (C)2016 Elsevier B.V.保留所有权利。

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