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Improved process for the production of aviation gasoline

机译:改进的航空汽油生产工艺

摘要

A catalytically cracked naphtha or gasoline is separated into a light fraction boiling between 60 DEG and 150-200 DEG F., the upper limit being chosen so as to exclude aromatics, and a heavy fraction boiling between 170-220 DEG and 350-410 DEG F., the light fraction is alkylated with isobutane, the heavy is catalytically cracked, and fractions of aviation gasoline boiling range separated from the products are combined. The products of recracking the heavy fraction may be fractionated to separate a C4 fraction, a light naphtha, and/or ethylene which may be alkylated with isobutane to increase the yield of gasoline. An intermediate fraction of the catalytically cracked feedstock boiling between about 160 DEG or 170 DEG and 220 DEG F. is of low octane number, improving little on cracking and is preferably discarded. A heavy oil such as gas oil may be cracked at 900-1000 DEG F., preferably using silica-alumina gel as "fluidized" catalyst, and the products, after separating catalyst, fractionated to give the light and heavy fractions required, and uncondensed gases which may be treated to separate ethylene and a C4 fraction. The latter, if desired after scrubbing with sulphuric acid and steam-treating the extract to recover isobutene for rubber production, is mixed with the light fraction and alkylated with isobutane using a suitable catalyst such as sulphuric acid of above 82 per cent at 45-80 DEG F. The ethylene is alkylated, using aluminium chloride at 100-150 DEG F. and 250-350 p.s.i. The alkylates are fractionated together to separate an aviation gasoline fraction generally boiling up to 300-330 DEG F. The heavy fraction from the first fractionation is recracked in a manner similar to the initial cracking, but generally at 700-950 DEG F., whereby isoparaffins and aromatics are produced and olefins removed. From the products, an aviation naphtha fraction mainly boiling at 190-335 DEG F. is separated and blended with the light alkylate fraction. Isobutane and olefins may be recovered for use in the alkylations. Examples compare the results of alkylation and recracking of selected light and heavy fractions, viz. 60-150 DEG and 220-410 DEG F. fractions of catalytically cracked naphtha.
机译:催化裂化的石脑油或汽油被分为沸点为60-150-200°F的轻馏分,选择上限以排除芳烃,沸点为170-220-350-410的重馏分。 F.,将轻馏分用异丁烷烷基化,将重馏分催化裂化,并将从产物中分离出的航空汽油沸程馏分合并。重馏分的产物可以被分馏以分离出C 4馏分,轻石脑油和/或乙烯,其可以用异丁烷烷基化以增加汽油的收率。沸点在约160°F或170°F至220°F之间的催化裂化原料的中间馏分的辛烷值低,裂化几乎没有改善,优选将其丢弃。重油例如粗柴油可以在900-1000°F下裂化,优选使用二氧化硅-氧化铝凝胶作为“流化”催化剂,并且分离催化剂后将产物分馏以得到所需的轻质和重质馏分,并且不冷凝可以处理以分离乙烯和C4馏分的气体。如果需要,可将后者与硫酸洗涤后再进行蒸汽处理,以回收用于橡胶生产的异丁烯,然后将其与轻质馏分混合,并使用合适的催化剂(如硫酸,其硫酸含量为82%以上,于45-80烷基化)用100-150°F和250-350 psi的氯化铝将乙烯烷基化将烷基化物一起分馏以分离通常沸点高达300-330°F的航空汽油馏分。以与初始裂化相似的方式将第一次馏分的重馏分进行再裂化,但通常在700-950°F下进行,生产异链烷烃和芳烃,并除去烯烃。从产物中分离出主要在190-335°F沸腾的航空石脑油馏分并与轻质烷基化物馏分混合。可以回收异丁烷和烯烃用于烷基化。实施例比较了选择的轻质和重质馏分的烷基化和再裂化的结果,即。催化裂化石脑油的60-150°F和220-410°F馏分。

著录项

  • 公开/公告号GB587813A

    专利类型

  • 公开/公告日1947-05-06

    原文格式PDF

  • 申请/专利权人 STANDARD OIL DEVELOPMENT COMPANY;

    申请/专利号GB19450001461

  • 发明设计人

    申请日1945-01-17

  • 分类号C07C9/14;

  • 国家 GB

  • 入库时间 2022-08-24 02:51:40

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