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    Process for making a lube base stock from a lower molecular weight feedstock
    112.
    发明授权
    Process for making a lube base stock from a lower molecular weight feedstock 失效
    从较低分子量原料制备润滑油基料的方法

    公开(公告)号：US06398946B1

    公开(公告)日：2002-06-04

    申请号：US09470053

    申请日：1999-12-22

    申请人： Dennis J. O'Rear ,  Thomas V. Harris

    发明人： Dennis J. O'Rear ,  Thomas V. Harris

    IPC分类号： C10G5702

    CPC分类号： C10M177/00 ,  C10G50/02 ,  C10G57/02 ,  C10M107/10 ,  C10N2270/00 ,  Y10S208/95

    摘要： A process for making a lube base stock wherein a highly paraffinic feedstock (with boiling points within the range of from 258° to 1100° F.) is dehydrogenated to produce an olefinic feedstock, which is oligomerized to produce an oligomerized product, which is separated into a lighter fraction and a heavier fraction. That heavier fraction has a flash point within the lube base oil range.

    摘要翻译： 制备润滑基料的方法，其中高度链烷烃原料（沸点在258°至1100°F的范围内）被脱氢以产生烯烃原料，其被低聚以产生低聚产物，其被分离 变成更轻的部分和更重的部分。 较重的馏分在润滑油基础油范围内具有闪点。

    Process for producing polypropylene from C3 olefins selectively produced by a two stage fluid catalytic cracking process
    113.
    发明授权
    Process for producing polypropylene from C3 olefins selectively produced by a two stage fluid catalytic cracking process 失效
    通过两阶段流化催化裂化方法选择性生产的C3烯烃生产聚丙烯的方法

    公开(公告)号：US06258257B1

    公开(公告)日：2001-07-10

    申请号：US09517551

    申请日：2000-03-02

    申请人： George A. Swan, III ,  Michael W. Bedell ,  Paul K. Ladwig ,  John E. Asplin ,  Gordon F. Stuntz ,  William A. Wachter ,  B. Erik Henry

    发明人： George A. Swan, III ,  Michael W. Bedell ,  Paul K. Ladwig ,  John E. Asplin ,  Gordon F. Stuntz ,  William A. Wachter ,  B. Erik Henry

    IPC分类号： C10G5102

    CPC分类号： C10G57/02 ,  C10G2400/20

    摘要： A process for producing polymers from olefins selectively produced by a two stage process for selectively producing C2 to C4 olefins from a gas oil or resid is disclosed herein. The gas oil or resid is reacted in a first stage comprising a fluid catalytic cracking unit wherein it is converted in the presence of conventional large pore zeolitic catalyst to reaction products, including a naphtha boiling range stream. The naphtha boiling range stream is introduced into a second stage comprising a process unit containing a reaction zone, a stripping zone, a catalyst regeneration zone, and a fractionation zone. The naphtha feed is contacted in the reaction zone with a catalyst containing from about 10 to 50 wt. % of a crystalline zeolite having an average pore diameter less than about 0.7 nanometers at reaction conditions which include temperatures ranging from about 500 to 650° C. and a hydrocarbon partial pressure from about 10 to 40 psia. Vapor products are collected overhead and the catalyst particles are passed through the stripping zone on the way to the catalyst regeneration zone. Volatiles are stripped with steam in the stripping zone and the catalyst particles are sent to the catalyst regeneration zone where coke is burned from the catalyst, which is then recycled to the reaction zone.

    摘要翻译： 本文公开了一种通过二级方法选择性制备聚合物的方法，用于从瓦斯油或渣油中选择性地生产C2至C4烯烃。 瓦斯油或渣油在包括流化催化裂化装置的第一阶段中反应，其中在常规大孔沸石催化剂存在下将其转化为包括石脑油沸程的反应产物。 将石脑油沸程流引入包含含有反应区，汽提区，催化剂再生区和分馏区的处理单元的第二阶段。 石脑油进料在反应区中与含有约10至50wt。 在包括约500至650℃的温度和约10至40psia的烃分压的反应条件下具有平均孔径小于约0.7纳米的结晶沸石的百分比。 蒸气产物被顶部收集，催化剂颗粒在通向催化剂再生区的途中通过汽提区。 挥发物在汽提区中用蒸汽汽提，并将催化剂颗粒送入催化剂再生区，其中焦炭从催化剂燃烧，然后再循环到反应区。

    Multistage integrated process for upgrading olefins
    115.
    发明授权
    Multistage integrated process for upgrading olefins 失效
    用于升级烯烃的多级综合工艺

    公开(公告)号：US5000837A

    公开(公告)日：1991-03-19

    申请号：US339466

    申请日：1989-04-17

    申请人： Mohsen N. Harandi

    发明人： Mohsen N. Harandi

    IPC分类号： C10G11/18 ,  C10G57/02

    CPC分类号： C10G11/18 ,  C10G57/02

    摘要： An improvement in gasoline octane without substantial decrease in overall yield is obtained in an integrated process combining a fluidized catalytic cracking reaction and a low severity fluidized catalyst olefin oligomerization reaction when crystalline medium pore shape selective zeolite catalyst particles are withdrawn in partially deactivated form from the oligomerization reaction stage and added as part of the active catalyst in the FCC reaction.

    摘要翻译： 当结晶介质孔形状选择性沸石催化剂颗粒以部分失活的形式从低聚反应中取出时，在结合流化催化裂化反应和低严重性流化催化剂烯烃低聚反应的一体化方法中获得汽油辛烷值的改善，而总收率没有显着降低 在FCC反应中作为活性催化剂的一部分加入。