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Effect of Process Parameters on Slow Pyrolysis of Rice Straw: Product Yield and Energy Analysis

机译:工艺参数对稻草慢热解的影响:产品产量和能量分析

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Slow pyrolysis of rice straw was carried out in a bench-scale fixed bed pyrolysis reactor. The effect of pyrolysis temperatures (300, 400, 500, and 600 °C) and residence time (1, 2, and 3 h) on product yield distribution and energy yield was studied. The biochar yield decreased from 57.87-31.25 wt.% with a rise in pyrolysis temperature and residence time. The percentage of carbon increased from 65.92-86.01%, while the percentage of hydrogen and oxygen decreased from 5.14-1.62% and 25.16-9.77%, respectively, with an increase in temperature and residence time. A similar trend observed in bio-oil characterization. The biochar yield initially increased from 300-500 °C and then reduced. The gas yield gradually increased from 11.91-28.16 %, with a rise in pyrolysis temperature and residence time. The concentration of CO and CO2 decreased gradually from 41.81-29.66% and 54.02-38.46%, while H2 and CH4 increased from 1.9-19.22% and 2.3-10.54%, respectively. The energy yield of biochar decreased from 63.76-39.94%, while bio-oil and gas yield increased from 25.02-40.73 % and 4.96-19.23%, respectively, with an increase in pyrolysis temperature and residence time.
机译:稻草慢热解是在长凳固定床热解反应器中进行的。研究了热解温度(300,400,500和600℃)和停留时间(1,2和3小时)对产物产量分布和能量产率的影响。生物炭产率从57.87-31.25重量%下降。%在热解温和停留时间上升。碳的百分比增加到65.92-86.01%,而氢气和氧的百分比分别从5.14-1.62%和25.16-9.77%下降,温度和停留时间增加。生物油特征中观察到的类似趋势。生物炭产率最初从300-500℃增加,然后减少。气体产量从11.91-28.16%逐渐增加,热解温和停留时间升高。 CO和CO的浓度 2 逐渐减少41.81-29.66%和54.02-38.46%,而H 2 和ch. 4 从1.9-19.22%和2.3-10.54%增加。生物炭的能量产量从63.76-39.94%下降,而生物油和天然气产量分别从25.02-40.73%和4.96-19.23%增加,随着热解温和停留时间增加。

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