首页> 外文会议>Proceedings of the 17th World Petroleum Congress >OPTIMISATION OF THE MEXICAN REFINING SYSTEM FOR LOW SULPHUR DIESEL PRODUCTION
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OPTIMISATION OF THE MEXICAN REFINING SYSTEM FOR LOW SULPHUR DIESEL PRODUCTION

机译:低硫柴油生产中墨西哥炼油系统的优化

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The Mexican refining industry is facing the challenge of producing ultra-clean fuels, while processing increasingly proportions of heavy and sour crude oil. Of particular relevance in the strategies devised for optimising the overall domestic petroleum industry, are the actions for assuring the supply of low sulphur diesel within a schedule that considers different stages for achieving reductions from 500 to 300 ppm in the near future, to 50 ppm for the year 2006. Other specifications considered are cetane, aromatics, density and distillation points. The Mexican Refining System includes 6 refineries with a total processing of 8,140.6 m~3/h. Diesel feedstock is mainly constituted by atmospheric gasoil; all streams are hydrotreated in 14 units operating in average at 52.6 x 105 N/m~2 g. that produce diesel fuel with less than 500 ppm sulphur. Future streams to be incorporated, resulting from ongoing projects, include cracked products from coking and FCC plants. Additionally the refinery reconfiguration in progress will permit the processing of a higher proportion of heavy crude oil, representing a movement from 2.2% to 2.6% sulphur in the crude blend. The reported strategies in this paper are based on a formal mathematical model and an optimisation exercise, considering operating condition adjustments, catalyst replacement, revamp and new installations. Technology projects for process and catalyst development were considered as scenarios for the decision taking process.
机译:墨西哥的炼油行业面临着生产超清洁燃料的挑战,同时需要加工越来越多的重,高酸原油。在优化整个国内石油行业的战略中,与计划中的特别相关的是确保时间表内的低硫柴油供应,这些时间表考虑了在不远的将来实现从500ppm减少到300ppm的不同阶段的目标。年份为2006。考虑的其他规格为十六烷,芳烃,密度和蒸馏点。墨西哥精炼系统包括6个精炼厂,总处理量为8,140.6 m〜3 / h。柴油原料主要由大气瓦斯油组成。所有料流均以14个单元进行加氢处理,平均运行速度为52.6 x 105 N / m〜2 g。产生的硫含量低于500 ppm的柴油。由于正在进行的项目而将合并的未来物流,包括焦化和FCC工厂的裂解产品。另外,进行中的炼油厂改组将允许加工更高比例的重质原油,即,原油混合物中的硫从2.2%移至2.6%。本文中报告的策略基于正式的数学模型和优化实践,其中考虑了运行条件调整,催化剂更换,改造和新安装。用于流程和催化剂开发的技术项目被视为决策流程的方案。

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