Reforming using a bound halided zeolite catalyst
    3.
    发明授权
    Reforming using a bound halided zeolite catalyst 有权
    使用结合的卤化沸石催化剂进行重整

    公开(公告)号:US06190539B1

    公开(公告)日:2001-02-20

    申请号:US09200053

    申请日:1998-11-24

    IPC分类号: C10G3506

    摘要: A catalytic reforming process comprising the catalytic conversion of hydrocarbons to aromatics, said process comprising treating a halided zeolite catalyst (hiz-cat) containing a Group VIII metal at commercial startup conditions and then reforming hydrocarbons, wherein said catalyst is prepared by washing a bound zeolite catalyst base or a bound zeolite catalyst before halide addition. A preferred hiz-cat is a non-acidic Pt K L-zeolite catalyst prepared by a process that includes the steps of preparing a calcined silica-bound K L-zeolite catalyst base; washing said bound zeolite catalyst base with a liquid comprising water; and incorporating Pt and halogen-containing compound(s) comprising chlorine and fluorine into said washed catalyst base. Ammonium chloride and ammonium fluoride are preferred halide sources.

    摘要翻译: 一种催化重整方法,包括将烃催化转化成芳族化合物,所述方法包括在商业启动条件下处理含有第Ⅷ族金属的卤化沸石催化剂(氢氧化钾),然后重整烃,其中所述催化剂是通过洗涤结合的沸石 催化剂底物或结合的沸石催化剂。 优选的咪唑是通过包括以下步骤制备的非酸性Pt K L-沸石催化剂,所述方法包括制备煅烧二氧化硅结合的KL-沸石催化剂基质的步骤; 用包含水的液体洗涤所述结合的沸石催化剂基质; 并将含有氯和氟的Pt和含卤素的化合物掺入所述洗涤的催化剂基质中。 氯化铵和氟化铵是优选的卤化物源。

    Reforming process with catalyst pretreatment
    5.
    发明授权
    Reforming process with catalyst pretreatment 失效
    催化剂预处理改性工艺

    公开(公告)号:US5914028A

    公开(公告)日:1999-06-22

    申请号:US781433

    申请日:1997-01-10

    摘要: A catalytic reforming process using a halided zeolite catalyst containing platinum in a metal-coated reactor system where, prior to catalyst loading and reforming, halide acid is removed from the catalyst. The process comprises providing a reforming reactor system having a metal coating; providing a halided zeolite catalyst containing platinum prepared by a method which includes removing volatile halide acid; loading said catalyst into said reactor system; and catalytically reforming hydrocarbons to aromatics, wherein metal from the metal-coated reactor system does not deactivate the catalyst. The coating metal preferably comprises tin and the zeolite catalyst is preferably a platinum L-zeolite catalyst. The invention is also a method for reducing catalyst contamination from a metal which was used to coat a reactor system. The method comprises pretreating a halided catalyst with hydrogen to remove volatile halide acid. The resulting catalyst is then loaded into a metal-coated reactor system and hydrocarbons are converted.

    摘要翻译: 在金属涂覆的反应器系统中使用含有铂的卤化沸石催化剂的催化重整方法,其中在催化剂负载和重整之前,从催化剂中除去卤化物酸。 该方法包括提供具有金属涂层的重整反应器系统; 提供含有铂的卤化沸石催化剂,其通过包括除去挥发性卤酸的方法制备; 将所述催化剂装入所述反应器系统; 并将烃催化重整成芳族化合物,其中来自金属涂覆的反应器系统的金属不使催化剂失活。 涂覆金属优选包含锡,并且沸石催化剂优选为铂L-沸石催化剂。 本发明还是一种减少用于涂覆反应器系统的金属的催化剂污染的方法。 该方法包括用氢去除卤化催化剂以除去挥发性卤酸。 然后将所得催化剂装载到金属涂覆的反应器系统中,并转化烃。

    Method for removing sulfur to ultra low levels for protection of
reforming catalysts
    7.
    发明授权
    Method for removing sulfur to ultra low levels for protection of reforming catalysts 失效
    将硫除去至超低水平以保护重整催化剂的方法

    公开(公告)号:US5322615A

    公开(公告)日:1994-06-21

    申请号:US804600

    申请日:1991-12-10

    CPC分类号: C10G69/08 C10G67/06

    摘要: Provided is a method for removing residual sulfur from a hydrotreated naphtha feedstock. The process comprises contacting the naphtha feedstock with a first solid sulfur sorbent comprising a metal on a support to thereby form a first effluent. The effluent is then contacted with a sulfur conversion catalyst comprising a Group VIII metal in the presence of hydrogen, with the resulting effluent being contacted with a second solid sulfur sorbent containing a Group IA or IIA metal, to thereby lower the sulfur content of the feedstock to less than 10 ppb, and to as low as 1 ppb or less. The feedstock can then be safely used with highly sulfur sensitive zeolitic reforming catalysts without adversely affecting the useful life of the catalyst.

    摘要翻译: 提供了从加氢处理的石脑油原料中除去残留硫的方法。 该方法包括使石脑油原料与载体上包含金属的第一固体硫吸附剂接触,从而形成第一流出物。 然后在氢的存在下,将流出物与包含VIII族金属的硫转化催化剂接触,所得流出物与含有IA或IIA族金属的第二固体硫吸附剂接触,从而降低原料的硫含量 至少于10ppb,低至1ppb或更低。 然后可以将原料安全地用于高度敏感的沸石重整催化剂,而不会不利地影响催化剂的使用寿命。