首页> 外国专利> Dewaxing by a combination centrifuge/catalytic process including solvent deoiling

Dewaxing by a combination centrifuge/catalytic process including solvent deoiling

机译:通过包括溶剂脱油在内的离心/催化组合工艺脱蜡

摘要

A hydrocarbon dewaxing process comprising the steps of: P P(a) chilling the waxy hydrocarbon feed to be dewaxed in the absence of solvent to crystallize a portion of the hard wax;P P(b) introducing the hydrocarbon feed to be dewaxed into a centrifuge;P P(c) centrifuging the solvent free hydrocarbon feed thereby generating two streams, stream (I) comprising a major portion of oil with a minor portion of entrained wax, stream (II) comprising a major portion of wax with a minor portion of entrained oil; PP(d) adding a dewaxing solvent to stream (II) generating a slurry A;PP (e) feeding slurry A to a centrifuge thereby separating slurry A into an oil-solvent stream (III) and a wax- solvent stream (IV);PP (f) passing the oil-solvent stream (III) to a membrane separation unit wherein the stream is separated into a recycle solvent stream and an oil- solvent stream of reduced solvent content (stream V);PP(g) passing oil-solvent stream (V) to an oil recovery unit wherein the stream is separated into a recycle solvent stream and an oil stream (VI); PP(h) passing the wax-solvent stream (IV) of step (e) to a wax recovery unit wherein the stream is separated into a recycle solvent stream and a recovered wax product stream;PP(i) combining wax-oil stream (I) of step (c) with oil stream (VI) of step (g) and passing the combined stream to a catalytic dewaxing unit wherein the combined waxy oil stream, in the presence of hydrogen, is contacted with a catalyst and has its wax content reduced, thereby generating a dewaxed oil product stream.
机译:一种烃脱蜡方法,包括以下步骤:(a)在不存在溶剂的情况下将要脱蜡的蜡状烃进料冷却,以使一部分硬蜡结晶; > >(b)引入将待脱蜡的碳氢化合物进料到离心机中;(c)离心无溶剂的碳氢化合物进料,从而产生两股物流(物流(I),该物流包含大部分油和少量夹带的蜡), II)包含大部分蜡和少量夹带的油;

(d)向流(II)中添加脱蜡溶剂以生成浆料A;

(e)将浆料A送入离心机,从而将浆料A分离为油溶剂流(III) )和蜡-溶剂流(IV);(P)(f)使油-溶剂流(III)进入膜分离单元,其中该流被分离为循环溶剂流和油-溶剂流降低的溶剂含量(流V); P(g)通过油溶剂流(V)到油回收单元,其中该流被分离成再循环溶剂流和油流(VI);

(h)使步骤(e)的蜡溶剂流(IV)进入蜡回收单元,其中该流被分为循环溶剂流和回收的蜡产物流; >(i)将步骤(c)的蜡-油料流(I)与步骤(g)的油料流(VI)合并,并在氢气存在下将合并的料流送至催化脱蜡单元,其中合并的蜡状油料流使其与催化剂接触并降低其蜡含量,从而产生脱蜡的油产品流。

著录项

  • 公开/公告号US4477333A

    专利类型

  • 公开/公告日1984-10-16

    原文格式PDF

  • 申请/专利权人 EXXON RESEARCH AND ENGINEERING CO.;

    申请/专利号US19830552701

  • 发明设计人 MAHMOUD M. HAFEZ;

    申请日1983-11-17

  • 分类号C10G73/02;C10G73/06;C10G73/28;

  • 国家 US

  • 入库时间 2022-08-22 08:37:15

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