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Improvements in or relating to the production of lubricating oils form crude oils and the like by treatment with hydrogen at high temperatures and pressures

机译:通过在高温和高压下用氢气处理,对原油或类似产品的润滑油生产进行了改进或与之相关

摘要

PICT:0352775/III/1 Lubricating oils are produced from heavy oils by passing the latter and gases rich in hydrogen in opposite directions through a deep bed of catalytic material at a temperature in excess of 700 DEG F. and under a pressure considerably in excess of atmospheric, and separately withdrawing liquid oil and gas from the catalytic bed. Heavy oil is passed rapidly through a heating coil 4 into the top of a vertical reaction drum packed with catalytic material while gas rich in hydrogen is forced through a heating coil 6 into the base of the drum which is maintained at the desired temperature by the heat of the incoming materials or may be heated internally. Gas and such light oil vapours as are formed are withdrawn through a line 8, heat exchanger 9, condenser 16 to a separator 11 from which the gases are returned to the system through a line 13, exchanger 9, purifier 14 and pump 15. The liquid oil is withdrawn with reduction of pressure through a pipe 18 and heat exchanger 19 to a flash tower 21 provided with heating coils 25, 24 and cooling coil 26. The vapours evolved are condensed in a condenser 28 and separated from gases in a separator 29, while the residual oil is evacuated through a heat exchanger 36 and cooler 37 to storage. The crude oil is preheated by passage through the heat exchangers 19, 36 and coil 26. The catalyst comprises preferably chromium and molybdenum oxides compressed in lump form or carried on resistant materials, e.g. kaolin in brick form. Formation of low boiling products is restricted to 5-20 per cent of the feed and temperatures of 700-825 DEG F. and pressures of 50-200 atmospheres are specified.
机译:润滑油是由重油和重氢组成的重油沿相反的方向在温度超过700°F且压力较大的情况下通过催化材料的深床层而制得的。超过大气压力,并分别从催化床中抽出液态石油和天然气。重油迅速通过加热盘管4进入装有催化材料的垂直反应鼓的顶部,而富含氢气的气体则通过加热盘管6进入鼓的底部,通过加热将其保持在所需温度下可能会内部进料或被加热。形成的气体和此类轻油蒸气通过管线8,热交换器9,冷凝器16进入分离器11,气体通过管线13,交换器9,净化器14和泵15从中返回系统。液体油在减压下通过管道18和热交换器19被抽出到设有加热盘管25、24和冷却盘管26的闪蒸塔21。所产生的蒸气在冷凝器28中冷凝,并在分离器29中与气体分离。然后,剩余油通过热交换器36和冷却器37被抽空到储存。原油通过通过热交换器19、36和盘管26而被预热。催化剂优选包括以块状压缩或负载在例如铁,镍,铁,铝,铁,镍,铁,镍,铁,镍,铁,铝,镍,铁,镍,铝,镍,镁,铬,镍,铁,镍,铝,镍,铬,钼,镍,铁,镍,铁,铝,镍,铁,铝,镍,铁,铝,镍,铁,镍,铁,镍,铁,镍,铁,镍,铁,镍,铁,镍,铁,镍等构成的金属氧化物。高岭土以砖的形式。低沸点产物的形成限于进料的5-20%,温度为700-825°F,压力规定为50-200个大气压。

著录项

  • 公开/公告号GB352775A

    专利类型

  • 公开/公告日1931-07-16

    原文格式PDF

  • 申请/专利权人 STANDARD OIL DEVELOPMENT COMPANY;

    申请/专利号GB19300024224

  • 发明设计人

    申请日1930-08-13

  • 分类号C10G47/00;

  • 国家 GB

  • 入库时间 2022-08-24 08:20:20

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