首页|最大规模浅冷油吸收法C1/C2分离技术工业应用实践

最大规模浅冷油吸收法C1/C2分离技术工业应用实践

Large scale industrial application practice of C1/C2 separation technology by shallow cold oil absorption method

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某公司采用浅冷油吸收法干气回收专利技术新建了一套C1/C2分离装置,以正丁烷为吸收剂吸收干气中的碳二馏分,再以重石脑油为吸收剂回收燃料气中夹带的碳四馏分,得到富乙烷气、轻烃和粗氢气分别送入乙烯装置、液化气分离装置和PSA装置.该分离装置规模达到了 1.6Mt/a,可以实现将20 Mt/a炼化一体化项目中炼油装置的干气全部加工.装置投产运行1年后进行了标定,结果显示,乙烷回收率和纯度分别达到了 92.7%和93.7%,产品分布良好,综合能耗达标,表明该技术的选择成熟可靠,值得推广应用.
A company has built a new set of C1/C2 separation unit using the patented shallow cold oil absorption method for dry gas recovery technology licensed by Beijing Research Institute of Chemical Industry,which uses n-butane as the absorbent to absorb C2 fraction in the dry gas,and then uses heavy naphtha as the absorbent to recover C4 fractions entrained in the fuel gas to obtain ethane-rich gas,light hydrocarbon and crude hydrogen,which are sent to the ethylene unit,liquefied gas separation unit and PSA unit,respectively.The scale of the unit reaches 1.6 Mt/a,which can process all the dry gas of the refining unit in the 20 Mt/a refining and chemical integration project.The unit runs stably after start-up,and is calibrated after one year of operation.The results show that the recovery rate and purity of ethane reaches 92.7%and 93.7%,respectively.The product distributes well,and the comprehensive energy consumption meets the standard.It is verified that this technology is mature and reliable,and it is worthy of popularization and application.

shallow cold oil absorption methodC1/C2 separation unitsaturated dry gasmixed dry gasethane recovery rate

魏文、田海波、王大为、张灵

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浙江石油化工有限公司,浙江 舟山 316000

浅冷油吸收法 C1/C2分离装置 饱和干气 混合干气 乙烷回收率

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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