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固定床氣化爐中心管配風(fēng)壓力場數(shù)值模擬
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山東省自然科學(xué)基金資助項(xiàng)目(2009ZRA01100)


Numerical Study on Pressure Field of Center Air Distribution Biomass Gasifier
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    摘要:

    氣化劑配風(fēng)工藝的改變可對氣化過程中爐內(nèi)溫度產(chǎn)生影響,經(jīng)過對比測溫實(shí)驗(yàn)得到中心管配風(fēng)工況下床層溫度高于雙層配風(fēng)工況。應(yīng)用Fluent軟件對不同配風(fēng)工藝下氣化爐壓力場進(jìn)行模擬分析,根據(jù)燃燒學(xué)理論找出熱解層壓力對氣化反應(yīng)的影響因素,結(jié)果表明:氣化劑中心管供給降低了氣化爐熱解層區(qū)域壓力,且該工況下床層壓力分布較均勻。熱解層壓力降低可增加揮發(fā)分析出量,加快反應(yīng)速率,提高爐內(nèi)溫度,從床層壓力角度詮釋了氣化爐實(shí)驗(yàn)結(jié)果,最后通過誤差分析方法檢驗(yàn)了仿真結(jié)果的準(zhǔn)確性。

    Abstract:

    Different air distribution craft should impact the temperature of biomass gasifier in the gasification process. After temperature compared test, the bed temperature in the condition of double-layer air distribution is lower than the center tube air distribution. Using the fluid analysis software Fluent to simulate the pressure field under those two crafts, the result displayed that the pressure of pyrolysis layer of biomass gasifier bed in center tube air distribution was reduced, and the pressure field became more regular. The conclusion is the volatile in pyrolysis would be more precipitated if the pressure of this field was prompted based on the combustion theory, and the reaction rate and temperature would speed up and improve. That explained the result of gasification test by the perspective of bed pressure. Finally the accuracy of simulation result was tested by the method of error analysis.

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孫宏宇,董玉平.固定床氣化爐中心管配風(fēng)壓力場數(shù)值模擬[J].農(nóng)業(yè)機(jī)械學(xué)報(bào),2011,42(1):117-121. Sun Hongyu, Dong Yuping. Numerical Study on Pressure Field of Center Air Distribution Biomass Gasifier[J]. Transactions of the Chinese Society for Agricultural Machinery,2011,42(1):117-121.

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