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汽油降苯增产芳烃的工艺优化研究

Process optimization for reducing benzene in gasoline and increasing aromatics production

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针对某公司S-Zorb装置脱硫后汽油中间馏分含有高达40%以上的C6~C8芳烃组分且苯含量高的现状,提出对汽油进行精密切割,切割出中间馏分进而达到降苯增产芳烃的目的.对汽油精密切割的3种工艺方案进行模拟计算和分析对比,包括设备投资、能耗和运行成本等,最终确定了"分馏塔带汽提塔"的工艺流程技术.分馏塔带汽提塔的工艺具有设备投资小、能耗低、流程简单、运行成本低的优势.
The middle distillate of gasoline after desulfurization in a certain company's S-Zorb unit contains high content of benzene and over 40%C6-C8 aromatic components.Therefore,a gasoline precise cutting idea is proposed to cut out the middle distillate to achieve the goal of reducing benzene content and increasing aromatics production.Three kinds of process schemes for gasoline precision cutting are simulated,analyzed and compared in the aspects of equipment investment,energy consumption and operation cost.Through optimization and comparison,the"fractionation tower with stripping tower"process scheme is determined as the optimal one,which has the advantages of low equipment investment,low energy consumption,simple process,and low operation cost.

desulfurizationdecrease of benzene contentgasolinefractionationaromatics

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中海油石化工程有限公司,山东青岛 266101

脱硫 降苯 汽油 分馏 芳烃

2024

现代化工
中国化工信息中心

现代化工

CSTPCD北大核心
影响因子:0.553
ISSN:0253-4320
年,卷(期):2024.44(3)
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