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生物質(zhì)鼓泡流化床和循環(huán)流化床氣化對(duì)比試驗(yàn)
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國家高技術(shù)研究發(fā)展計(jì)劃(863計(jì)劃)資助項(xiàng)目(2009AA05Z409);山東省科技攻關(guān)資助項(xiàng)目(2010GGX10702)


Comparison of Bubbling Fluidized Bed and Circulating Fluidized Bed in Gasification of Biomass
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    在內(nèi)徑為Φ0.2m、高6m的流化床裝置上,利用兩種不同粒徑的石英砂,,分別進(jìn)行了高速鼓泡流化床(BFB)和循環(huán)流化床(CFB)的冷態(tài)壓力分布試驗(yàn)和熱態(tài)氣化試驗(yàn),。結(jié)果表明:冷態(tài)試驗(yàn)中,鼓泡流化床壓力分布主要集中在底部的密相區(qū),,循環(huán)流化床壓力分布更趨均勻,。熱態(tài)穩(wěn)定氣化階段,循環(huán)流化床軸向溫差只有40℃,,氣化的燃?xì)鉄嶂?、碳轉(zhuǎn)化率和氣化效率均高于鼓泡流化床,。

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    The results from biomass gasification in a pilot-scale (6m tall×0.2m internal diameter) air-blown circulating fluidized bed gasifier was tested and compared with bubbling fluidized bed gasifier. The results showed that the diameters of bed material in bubbling fluidized bed and circulating fluidized bed were different. The bubbling fluidized bed had a dense zone and bed material was homogeneous distribution in circulating fluidized bed. The temperature of the circulating fluidized bed was more uniform than bubbling fluidized bed. The carbon conversion rate, gasification efficiency and low gas heat value of circulating fluidized bed were larger than that of bubbling fluidized bed gasifier.

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范曉旭,賢建偉,初雷哲,楊立國.生物質(zhì)鼓泡流化床和循環(huán)流化床氣化對(duì)比試驗(yàn)[J].農(nóng)業(yè)機(jī)械學(xué)報(bào),2011,42(4):96-99. Fan Xiaoxu, Xian Jianwei, Chu Leizhe, Yang Liguo. Comparison of Bubbling Fluidized Bed and Circulating Fluidized Bed in Gasification of Biomass[J]. Transactions of the Chinese Society for Agricultural Machinery,2011,42(4):96-99.

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