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17 条记录 (耗时 0.033 秒)

    High density recycle gas for reforming process
    7.
    发明授权
    High density recycle gas for reforming process 失效
    用于重整过程的高密度循环气

    公开(公告)号：US4615793A

    公开(公告)日：1986-10-07

    申请号：US579742

    申请日：1984-02-13

    申请人： Lawrence W. Jossens

    发明人： Lawrence W. Jossens

    IPC分类号： C10G35/095 ,  C10G35/06

    CPC分类号： C10G35/095

    摘要： A hydrocarbon feed is contacted with a reforming catalyst in a reaction vessel to produce a reformate, hydrogen, methane, and ethane are stripped from the reformate in a first separator, C.sub.3 -C.sub.5 hydrocarbons are stripped from the stripped reformate in a second separator, and then a portion of the hydrogen, methane, and ethane; and substantially all of the C.sub.3 -C.sub.5 hydrocarbons are recycled to the reaction vessel as heat carrier.

    摘要翻译： 将碳氢化合物进料与反应容器中的重整催化剂接触以产生重整油，氢气，甲烷和乙烷在第一分离器中从重整产物中汽提，在第二分离器中将C3-C5烃从汽提的重整产物中汽提， 然后一部分氢，甲烷和乙烷; 并且基本上所有的C3-C5烃都作为热载体再循环到反应容器中。

    Upgrading fischer-Tropsch and petroleum-derived naphthas and distillates
    8.
    发明授权
    Upgrading fischer-Tropsch and petroleum-derived naphthas and distillates 失效
    升级费 - 托和石油衍生的石脑油和馏出物

    公开(公告)号：US06863802B2

    公开(公告)日：2005-03-08

    申请号：US10059382

    申请日：2002-01-31

    申请人： Dennis J. O'Rear ,  Lawrence W. Jossens

    发明人： Dennis J. O'Rear ,  Lawrence W. Jossens

    IPC分类号： C10G65/00 ,  C10G69/08 ,  C10G69/14 ,  C10G35/04 ,  C10G35/06

    CPC分类号： C10G69/08 ,  C10G45/02 ,  C10G65/00 ,  C10G2300/1022 ,  C10G2400/02 ,  C10G2400/06 ,  C10G2400/10

    摘要： A process for upgrading at least one of a Fischer-Tropsch naphtha and a Fischer-Tropsch distillate to produce at least one of a gasoline component, a distillate fuel or a lube base feedstock component. The process includes reforming a Fischer-Tropsch naphtha to produce hydrogen by-product and a gasoline component with a research octane rating of at least about 80. The process further includes upgrading a Fischer-Tropsch distillate using the hydrogen by-product to produce a distillate fuel and/or a lube base feedstock component.

    摘要翻译： 一种用于升级费 - 托石脑油和费 - 托馏出物中的至少一种以产生汽油组分，馏出燃料或润滑油基料原料组分中的至少一种的方法。 该方法包括重整费 - 托石脑油以产生氢副产物和研究辛烷值为至少约80的汽油组分。该方法还包括使用氢副产物升级费 - 托馏出物以产生馏出物 燃料和/或润滑油基料原料组分。

    Catalytic cracking process with vanadium passivation and improved
    9.
    发明授权
    Catalytic cracking process with vanadium passivation and improved 失效
    催化裂化过程与钒钝化和改进

    公开(公告)号：US5002653A

    公开(公告)日：1991-03-26

    申请号：US459097

    申请日：1989-12-29

    申请人： James V. Kennedy ,  Lawrence W. Jossens

    发明人： James V. Kennedy ,  Lawrence W. Jossens

    IPC分类号： C10G11/05

    CPC分类号： C10G11/05

    摘要： A catalytic cracking process is disclosed employing a dual component cracking catalyst system comprising zeolite as a first component and a mixture of a calcium/magnesium-containing material and a magnesium-containing material as a second component. The preferred calcium/magnesium-containing material is dolomite and the preferred magnesium-containing material is sepiolite.

    摘要翻译： 公开了使用包含沸石作为第一组分和含钙/镁的材料和含镁材料的混合物作为第二组分的双组分裂化催化剂体系的催化裂化方法。 优选的含钙/镁的材料是白云石，优选的含镁材料是海泡石。

    Dehydrocyclization process
    10.
    发明授权
    Dehydrocyclization process 失效
    脱氢环化过程

    公开(公告)号：US4650565A

    公开(公告)日：1987-03-17

    申请号：US426376

    申请日：1982-09-29

    申请人： Robert L. Jacobson ,  Lawrence W. Jossens

    发明人： Robert L. Jacobson ,  Lawrence W. Jossens

    IPC分类号： B01J29/068 ,  C10G35/095 ,  C10G35/06 ,  C07C2/52

    CPC分类号： B01J29/068 ,  C10G35/095

    摘要： A process is disclosed wherein a naphtha feed is contacted in a reaction vessel with a dehydrocyclization catalyst comprising a large-pore zeolite containing at least one Group VIII metal to produce an aromatics product and a gaseous stream, the aromatics product is separated from the gaseous stream and is passed through a molecular sieve which adsorbs paraffins present in the aromatics product, then the gaseous stream is used to strip the paraffins from the molecular sieve, and the gaseous stream and the paraffins are recycled to the reaction vessel. Preferably, the dehydrocyclization catalyst comprises a type L zeolite containing from 8% to 15% by weight barium and from 0.6% to 1.0% by weight platinum, wherein at least 80% of the crystals of the type L zeolite are larger than 1000 Angstroms, and an inorganic binder selected from the group consisting of silica, alumina, and aluminosilicates.

    摘要翻译： 公开了一种方法，其中使石脑油进料在反应容器中与脱氢环化催化剂接触，所述脱氢环化催化剂包含含有至少一种VIII族金属的大孔沸石以产生芳族化合物产物和气态物流，所述芳烃产物与气流 并通过吸附存在于芳族化合物产物中的链烷烃的分子筛，然后使用气流从分子筛中剥离链烷烃，并将气态物流和链烷烃再循环到反应容器中。 优选地，脱氢环化催化剂包括含有8重量％至15重量％的钡和0.6重量％至1.0重量％的铂的L型沸石，其中至少80％的L型沸石的晶体大于1000埃， 和选自二氧化硅，氧化铝和铝硅酸盐的无机粘合剂。