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The micro-explosion strength of emulsified heavy oil droplets in catalytic cracking process

机译:乳化重油滴催化裂化过程的微爆强度

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The emulsified feedstock technique applies the secondary atomization mechanism to heavy oil catalytic cracking process, which can significantly improve the atomization of feedstock and result in a more desirable product distribution. A model of micro-explosion strength of emulsion droplets in riser reactor is proposed in this paper. Model calculation shows that the superheat limit of emulsified heavy oil is 307.7 degrees C at atmospheric pressure, and the micro-explosion strength increases with the size of dispersed water sub-droplets. The theoretical prediction was validated experimentally through feedstock emulsification tests and catalytic cracking experiments. Results indicate that with an increase of the water content in feedstock emulsification, the size of dispersed water sub-droplets in emulsified oil rises, and thus the micro-explosion strength of emulsion droplets in riser reactor increases, which results in a higher light oil yield and lower coke and dry gas yields of catalytic cracking. Compared with pure heavy oil feedstock, the light oil yield rises by 2%, and the yields of coke and dry gas decline by 1.23% and 0.17% respectively for emulsified feedstock at 5% water content. (C) 2016 Elsevier B.V. All rights reserved.
机译:乳化原料技术将二次雾化机理应用于重油催化裂化工艺中,可以显着改善原料的雾化并产生更理想的产品分布。提出了提升管反应器中乳剂微滴爆炸强度的模型。模型计算表明,在大气压力下,乳化重油的过热极限为307.7℃,其微爆炸强度随分散的水液滴的大小而增加。通过原料乳化试验和催化裂化实验对理论预测进行了实验验证。结果表明,随着原料乳化中水含量的增加,乳化油中分散的水分散液滴的大小增加,从而提升管反应器中乳化液滴的微爆炸强度增加,从而导致轻油产量更高降低焦炭和干气催化裂化的收率。与纯重油原料相比,乳化原料在水含量为5%时,轻油产率提高了2%,焦炭和干气产率分别降低了1.23%和0.17%。 (C)2016 Elsevier B.V.保留所有权利。

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