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歧化装置与芳烃装置二甲苯塔分离热耦合工艺

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针对歧化装置和芳烃装置的C8 和C9 物料被重复冷凝与加热,以及设备数量多、投资大、占地多、开工程序复杂等缺点,中海石油宁波大榭石化有限公司将歧化装置的重芳烃塔与芳烃装置的二甲苯塔合并为 1 个新二甲苯塔,开发出满足C8 芳烃深度分离和C9 芳烃烷基转移的低成本分离热耦合精馏技术.结果表明:通过Petro-SIM软件模拟,该二甲苯塔分离热耦合工艺获得的C8 芳烃产品中甲苯质量分数小于0.98%,C≥9 重芳烃质量分数小于 2.51%,获得的C9 芳烃产品中C8 芳烃质量分数小于 0.21%,C≥10 重组分质量分数小于 0.07%;与传统工艺相比,热耦合工艺装置建设投资约减少 2700 万元,节省占地 6 666.7 m2,减少二氧化碳排放 9 600 t/a.
Thermal coupled process for separation of xylene tower in disproportionation unit and aromatic hydrocarbon unit
In response to the drawbacks of repeated condensing and heating of C8 and C9 feedstocks in the disproportionation unit and aromatics units,as well as the large number of equipment,high investment,large land occupation,and complex start-up proce-dures,a low cost separation thermal coupled distilla-tion technology that met the deep separation of C8 aro-matics and alkyl transfer of C9 aromatics was devel-oped by Ningbo Daxie Petrochemical Co Ltd of CNOOC.The characteristics of the distillation tech-nology was that merged the heavy aromatics tower of the disproportionation unit and the xylene tower of the aromatics unit into a new xylene tower.The results showed that through the simulation of Petro-SIM soft-ware,the mass fraction of toluene in the C8 aromatic hydrocarbon product obtained by the thermal coupled process of the xylene tower separation was less than 0.98%,the mass fraction of C≥9 heavy aromatic hy-drocarbons was less than 2.51%,and the mass frac-tion of C8 aromatic hydrocarbons in the C9 aromatic hydrocarbon product obtained was less than 0.21%,and the mass fraction of C≥10 heavy aromatic hydro-carbons was less than 0.07%.Compared with tradi-tional processes,the construction investment of the thermal coupled process unit was reduced by about 27 million Yuan,saving 6 666.7 m2 of land and re-ducing carbon dioxide emissions by 9600 t/a.

disproportionation unitaromatic hy-drocarbon unitxylene towerthermal coupled dis-tillation technologyPetro-SIM simulation software

姜志忠、刘荣博

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中海石油宁波大榭石化有限公司,浙江 宁波 315812

歧化装置 芳烃装置 二甲苯塔 热耦合精馏技术 Petro-SIM模拟软件

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(5)