首页|直馏柴油加氢改质多产优质乙烯裂解原料

直馏柴油加氢改质多产优质乙烯裂解原料

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采用柴油缓和加氢裂化技术对直馏柴油进行改质,考察不同工艺条件对直馏柴油转化率以及加氢裂化产物性质的影响.结果表明:在反应压力为 7.0 MPa,体积空速为 2.0 h-1 的条件下,随着反应温度由340℃升高至 350℃,直馏柴油的转化率由 16%提高至 50%;随着转化率的提高,全馏分柴油的芳烃指数降低,链烷烃质量分数增加;在反应温度为 345℃的条件下,初馏点~91.0℃石脑油馏分段的链烷烃质量分数为78%,用作乙烯裂解原料时,乙烯收率为 29.2%,乙烯+丙烯+丁二烯(三烯)收率为 62.0%;大于 234℃~终馏点柴油窄馏分段的链烷烃质量分数大于 60%,用作乙烯裂解原料时,乙烯收率为 31.9%,三烯收率为 64.6%.
Producing more high quality ethylene cracking feedstock by hydrogenation modification of straight-run diesel
Straight-run diesel was modified by mild hydrocracking process.The effect of different process conditions on the conversion rate of straight-run diesel and the properties of hydrocracking prod-ucts was investigated.The results showed that under the conditions of reaction pressure of 7.0 MPa and volume space velocity of 2.0 h-1,the conversion rate of straight-run diesel oil increased from 16%to 50%with the increasing of reaction temperature from 340℃to 350℃.With the increasing of con-version rate,the aromatics index of total distillate diesel decreased and the mass fraction of paraffin in-creased.Under the condition of reaction temperature of 345℃,the paraffin mass fraction of naphtha from initial distillation point to 91.0℃was 78%,and the ethylene yield was 29.2%and the triene(ethylene,propylene,butadiene)yield was 62.0%as ethylene cracking raw material.When the paraffin mass frac-tion of narrow fraction of diesel oil from 234℃to fi-nal distillation point was more than 60%,the ethy-lene yield was 31.9%and the triene yield was 64.6%as ethylene cracking raw material.

straight-run dieselethylene crack-ing feedstockhydrogenation modificationmolecular refiningparaffinethylene yield

王燕、张占全、雷俊伟、郭荣、王春燕、吴培、李荣观、侯远东

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中国石油石油化工研究院,北京 102206

直馏柴油 乙烯裂解原料 加氢改质 分子炼油 链烷烃 乙烯收率

中国石油项目

22-LH-66-05

2024

石化技术与应用
兰州石化公司石油化工研究院

石化技术与应用

CSTPCD
影响因子:0.491
ISSN:1009-0045
年,卷(期):2024.42(2)
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