Catalytic cracking process
    23.
    发明授权
    Catalytic cracking process 失效
    催化裂化过程

    公开(公告)号:US4784750A

    公开(公告)日:1988-11-15

    申请号:US870595

    申请日:1986-06-04

    CPC classification number: C10G11/05 B01J29/084

    Abstract: The invention concerns a hydrocarbon cracking catalyst containing a mixture of amorphous matrix with a zeolite, the zeolite having a SiO.sub.2 /Al.sub.2 O.sub.3 molar ratio ranging from about 8 to 70, a sodium content lower than 0.15% by weight, a parameter a.sub..degree. of elementary mesh from 24.55 to 24.24.times.10.sup.-10 m, a capacity C.sub.Na to retake sodium ions, expressed in grams of sodium per 100 grams of modified zeolite, higher than 0.85, a specific surface higher than 400 m.sup.2.g.sup.-1, a sodium ion uptake steam adsorption capacity at 25.degree. C. (with a P/Po ratio of 0.10) higher than 6% by weight, a pore distribution such that from 1 to 20% of the pore volume is pores of a diameter ranging from 20 to 80.10.sup.-10 m, the remaining pore volume being essentially pores of a diameter lower than 20.10.sup.-10 m, the matrix being characterized by the following textural properties:S .gtoreq.100 m.sup.2.g.sup.-1TPV .gtoreq.0.4 cm.sup.3.g.sup.-1PV.sub.75 .gtoreq.0.25 cm.sup.3.g.sup.-1PV.sub.75 /TPV .gtoreq.0.5

    Abstract translation: 本发明涉及一种含有无定形基质与沸石混合物的烃裂解催化剂,该沸石的SiO 2 / Al 2 O 3摩尔比约为8-70,钠含量低于0.15%(重量),参数a DEG基本网格 从24.55至24.24×10-10 m,CNa重新获得钠离子,以每克100克改性沸石钠表示,高于0.85,比表面积高于400 m2.g-1,钠离子吸收蒸汽 吸附容量在25℃(P / Po比为0.10)高于6重量%,孔分布使得孔体积的1至20%是直径为20至80.10-10的孔 m,剩余的孔体积基本上是直径小于20.10-10μm的孔,该基体的特征在于以下结构性质:S> = 100m 2·g-1 TPV> / = 0.4cm 3·g-1 PV 75 > = 0.25cm 3·g -1 PV75 / TPV> / = 0。

    Method of hydrocracking paraffins emanating from the Fischer-Tropsch
process using catalysts based on H-Y zeolite
    30.
    发明授权
    Method of hydrocracking paraffins emanating from the Fischer-Tropsch process using catalysts based on H-Y zeolite 失效
    使用基于H-Y沸石的催化剂从费 - 托方法发出的链烷烃的加氢裂化方法

    公开(公告)号:US5345019A

    公开(公告)日:1994-09-06

    申请号:US886225

    申请日:1992-05-21

    CPC classification number: C10G65/10 Y10S585/946

    Abstract: A method of hydrocracking charges emanating from the Fischer-Tropsch process, in which:(a) hydrogen is reacted with the charge in contact with a catalyst 1 in a first reaction zone, the said catalyst 1 comprising at least one alumina-based matrix and at least one hydro-dehydrogenation component;(b) the effluent from the first reaction zone is put into contact with a catalyst 2 in a second reaction zone, the said catalyst 2 comprising:20 to 97% by weight of at least one matrix;3 to 80% by weight of at least one Y zeolite in hydrogen form,the said zeolite being characterized by an SiO.sub.2 /Al.sub.2 O.sub.3 molar ratio of over 4.5:1, a sodium content of less than 1% by weight determined on a zeolite calcined at 1100.degree. C.; an a.sub.o crystal parameter of the elemental mesh of less than 24.70.times.10.sup.-10 m; and a specific surface area determined by the BET method of over 400 m.sup.2.g.sup.-1 ;and at least one hydro-dehydrogenation component.

    Abstract translation: 一种从费 - 托法生产的加氢裂化装料的方法,其中:(a)在第一反应区中使氢气与与催化剂1接触的电荷反应,所述催化剂1包含至少一种基于氧化铝的基体和 至少一种氢脱氢组分; (b)来自第一反应区的流出物与第二反应区中的催化剂2接触,所述催化剂2包含:至少一种基质的20至97重量%; 3至80重量%的至少一种氢形式的Y沸石,所述沸石的特征在于SiO 2 / Al 2 O 3摩尔比超过4.5:1,钠含量小于1重量%,在沸石上煅烧 1100℃。 元素网的ao晶体参数小于24.70x10-10 m; 并且通过BET法测定的比表面积超过400m 2·g -1; 和至少一种氢脱氢组分。

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