Method and catalyst for removing contaminants from hydrocarbonaceous
fluids using a copper-group via metal-alumina catalyst
    21.
    发明授权
    Method and catalyst for removing contaminants from hydrocarbonaceous fluids using a copper-group via metal-alumina catalyst 失效
    使用铜基金属 - 氧化铝催化剂从含烃流体中除去污染物的方法和催化剂

    公开(公告)号:US4601998A

    公开(公告)日:1986-07-22

    申请号:US723694

    申请日:1985-04-16

    CPC分类号: C10G45/04 B01J23/85

    摘要: There is provided a method and catalyst for removing catalyst-poisoning impurities or contaminants such as arsenic, iron and nickel from hydrocarbonaceous fluids, particularly shale oil and fractions thereof. More particularly there is provided a method of removal of such impurities by contacting the fluids with a copper-Group VIA metal-alumina catalyst. For example, a copper-molybdenum-alumina catalyst may be used as a guard bed material in a step preceding most refining operations, such as desulfurization, denitrogenation, catalytic hydrogenation, etc.

    摘要翻译: 提供了一种从含烃流体,特别是页岩油及其馏分中除去催化剂中毒杂质或污染物如砷,铁和镍的方法和催化剂。 更具体地,提供了通过使流体与铜基团VIA金属 - 氧化铝催化剂接触来除去这些杂质的方法。 例如,可以在大多数精炼操作之前的步骤中使用铜 - 钼 - 氧化铝催化剂作为保护床材料,例如脱硫,脱氮,催化氢化等。

    Production of ethylbenzene
    22.
    发明授权
    Production of ethylbenzene 失效
    生产乙苯

    公开(公告)号:US5334795A

    公开(公告)日:1994-08-02

    申请号:US967954

    申请日:1992-10-27

    IPC分类号: C07C2/66

    CPC分类号: C07C2/66 C07C2529/70

    摘要: Ethylbenzene is produced by the alkylation of benzene with ethylene in the presence of an alkylation catalyst having a particular structure defined by its X-ray diffraction pattern. A preferred catalyst is the zeolite MCM-22. The process is typically carried out at a temperature of 300.degree. to 1000.degree. F. but the catalyst provides sufficient activity for the reaction to be carried out at temperatures below 700.degree. F. Liquid phase operation is preferred, giving a lower yield of polyethylated products. The use of the selected catalyst also results in a reduction of the xylene impurity level to values below 500 ppm in the product.

    摘要翻译: 在具有由其X射线衍射图形定义的特定结构的烷基化催化剂存在下,通过苯与乙烯的烷基化生产乙苯。 优选的催化剂是沸石MCM-22。 该方法通常在300至1000°F的温度下进行,但催化剂提供足够的活性以使反应在低于700°F的温度下进行。液相操作是优选的,从而降低聚乙烯化产物的产率 。 使用所选择的催化剂还导致二甲苯杂质水平降低到产品中低于500ppm的值。

    Process for making a blended lubricant
    23.
    发明授权
    Process for making a blended lubricant 失效
    制造混合润滑剂的方法

    公开(公告)号:US5306416A

    公开(公告)日:1994-04-26

    申请号:US898365

    申请日:1992-06-15

    摘要: A blended mineral oil lubricant is made having a higher viscosity index than predicted by calculating the viscosity index from an ASTM standard method designated D 341-87 or by calculating the average of the actual VI based on the proportion of each component of the blend. The lubricant is treated with a peroxide compound, preferably an organic peroxide such as di-tertiary butyl peroxide to increase the viscosity index. The treated lubricant is blended with a lubricant of lower viscosity index to achieve a blended lubricant having an enhanced viscosity index. The lubricant charge stock and blending component can be a wax-derived lubricant fraction or a conventional light neutral or heavy neutral mineral oil.

    摘要翻译: 制备混合矿物油润滑剂,其具有比通过由标准D 341-87的ASTM标准方法计算粘度指数更高的粘度指数,或通过基于混合物各组分的比例计算实际VI的平均值。 润滑剂用过氧化物化合物,优选有机过氧化物如二叔丁基过氧化物处理以增加粘度指数。 将经处理的润滑剂与较低粘度指数的润滑剂混合以获得具有增强粘度指数的混合润滑剂。 润滑剂装料和共混组分可以是蜡衍生的润滑剂部分或常规的轻质中性或重质中性矿物油。

    Isobutene and isoamylene production
    24.
    发明授权
    Isobutene and isoamylene production 失效
    异丁烯和异戊烯生产

    公开(公告)号:US5304694A

    公开(公告)日:1994-04-19

    申请号:US883638

    申请日:1992-05-15

    摘要: Catalytic conversion of a C.sub.2 -C.sub.5 alkane, e.g., isobutane and/or isopentane, to isoalkenes, e.g., isobutene and/or isopentene, respectively, is undertaken in the presence of an aromatic recycle stream which provides the heat of reaction for the conversion which is endothermic, in the absence of hydrogen.

    摘要翻译: C2-C5烷烃如异丁烷和/或异戊烷分别转化为异烯烃,例如异丁烯和/或异戊烯,分别在芳烃再循环料流的存在下进行,其提供了转化反应热, 在没有氢的情况下是吸热的。

    Catalytic oligomerization process using modified mesoporous crystalline
material
    26.
    发明授权
    Catalytic oligomerization process using modified mesoporous crystalline material 失效
    使用改性介孔结晶材料的催化低聚方法

    公开(公告)号:US5260501A

    公开(公告)日:1993-11-09

    申请号:US920944

    申请日:1992-07-28

    IPC分类号: C07C2/10 C07C2/12

    摘要: A novel oligomerization catalyst and process for upgrading olefins employing new synthetic catalyst of ultra-large pore crystalline material. The new crystalline material exhibits unusually large sorption capacity demonstrated by its benzene adsorption capacity of greater than about 15 grams benzene/100 grams at 50 torr and 25.degree. C., a hexagonal electron diffraction pattern that can be indexed with a d.sub.100 value greater than about 18 Angstrom Units and a hexagonal arrangement of uniformly sized pores with a maximum perpendicular cross section of at least about 13 Angstrom units; and the porous crystalline material is impregnated with at least one oligomerization promoting metal, such as Groups VIIIA metals, preferably nickel.The new process is provided for catalytic oligomerization of olefin feedstock which comprises contacting the feedstock under catalytic conversion conditions with the metal-modified acid metallosilicate solid catalyst having the structure of MCM-41 with hexagonal honeycomb lattice structure consisting essentially of uniform pores in the range of about 20 to 100 Angstroms. The oligomerization reaction is very selective, especially when conducted at temperature of 60.degree. to 120.degree. C. Low severity reaction permits excellent conversion of lower olefins at pressure of about 100-13,000 kPa range and moderate space velocity.

    摘要翻译: 一种新型低聚催化剂和使用新型超大孔结晶材料合成催化剂改质烯烃的方法。 新的结晶材料表现出非常大的吸附能力,其吸附能力在50托和25℃时苯吸附能力大于约15克苯/ 100克,可以用大于约100的d100值进行指数的六方电子衍射图 18埃单位和具有至少约13埃单位的最大垂直横截面的均匀尺寸孔的六边形排列; 并且多孔结晶材料用至少一种低聚促进金属浸渍,例如第VIIIA族金属,优选镍。 提供了用于烯烃原料的催化低聚的新方法,其包括在催化转化条件下使原料与具有MCM-41结构的金属改性的酸式金属硅酸盐固体催化剂接触,六方蜂窝晶格结构基本上由均匀的孔组成, 约20至100埃。 低聚反应是非常有选择性的,特别是在60℃至120℃的温度下进行。低强度反应允许在约100-13000kPa范围和适度的空间速度的压力下对低级烯烃进行极好的转化。

    Aromatics alkylation process
    27.
    发明授权
    Aromatics alkylation process 失效
    芳烃烷基化方法

    公开(公告)号:US5191135A

    公开(公告)日:1993-03-02

    申请号:US673925

    申请日:1991-03-25

    IPC分类号: C07C2/66

    摘要: Long chain alkyl substituted aromatic compounds, particularly alkylated naphthalenes, are produced by the alkylation of aromatics, e.g. naphthalene, with an olefin or other alkylating agent possessing at least 6 carbon atoms, usually 12 to 20 carbon atoms, in the presence of a zeolite alkylation catalyst, preferably a large pore size zeolite such as zeolite Y and in the presence of from about 0.5 to 3.0 weight percent water, preferably 1.0 to 3.0 weight percent. The use of the water co-feed increases the selectivity of the alkylation for the production of long chain mono-alkyl substituted naphthalenes in preference to more highly substituted products and also increases activity and catalyst stability.

    摘要翻译: 长链烷基取代的芳族化合物,特别是烷基化萘,通过芳族化合物的烷基化,例如, 萘与具有至少6个碳原子,通常12-20个碳原子的烯烃或其它烷基化剂在沸石烷基化催化剂,优选大孔沸石如沸石Y的存在下并在约0.5的存在下反应 至3.0重量%的水,优选1.0至3.0重量%。 使用水共进料增加了烷基化用于生产长链单烷基取代萘的选择性,优于更高取代的产物,并且还增加了活性和催化剂的稳定性。

    Light cycle oil conversion
    28.
    发明授权
    Light cycle oil conversion 失效
    轻循环油转化

    公开(公告)号:US5171916A

    公开(公告)日:1992-12-15

    申请号:US715269

    申请日:1991-06-14

    IPC分类号: C10G29/20

    CPC分类号: C10G29/205

    摘要: Alkylated aromatic functional fluids are prepared by alkylating a light cycle oil with an alkylating agent, such as an alpha C.sub.14 -olefin or coker gas oil, over a crystalline metallosiicate catalyst, preferably an aluminosilicate, including MCM-22, USY or an acid treated kaolin clay. The process produces an improved light cycle oil in which the heteroatom content of the oil is reduced and a high quality synthetic alkylated aromatic functional fluid base stock boiling above 600.degree. F. The reactor temperature can be elevated to increase the functional fluid yield and the extent of heteroatom removal.

    摘要翻译: 烷基化芳族官能流体通过在结晶金属化合催化剂,优选包括MCM-22,USY或酸处理的高岭土的铝硅酸盐上,用烷基化剂如αC 14 - 烯烃或焦化瓦斯油将轻质循环油烷基化来制备 粘土。 该方法产生改进的轻循环油,其中油的杂原子含量降低,高质量的合成烷基化芳族官能液基料沸点高于600°F。可以提高反应器温度以增加功能流体产率和程度 的杂原子去除。

    Method of noble metal-zeolite catalyst activation with Bronsted acid
compound
    29.
    发明授权
    Method of noble metal-zeolite catalyst activation with Bronsted acid compound 失效
    用布朗斯台德酸化合物对贵金属 - 沸石催化剂活化的方法

    公开(公告)号:US4826792A

    公开(公告)日:1989-05-02

    申请号:US193151

    申请日:1988-05-05

    摘要: A method for reactivating noble metal-containing zeolites containing sulfur oxide poisoned noble metal such as oxygen regenerated platinum zeolite beta catalysts, by contacting the catalyst with an acidic aqueous solution having a pH below about 7. The solution contains a Bronsted acid compound having a dissociation constant ranging from about 1.times.10.sup.-14 to about 2.times.10.sup.-1.

    摘要翻译: 通过使催化剂与pH低于约7的酸性水溶液接触,使含有硫氧化物中毒的贵金属如贵金属贵金属如氧再生的铂沸石β催化剂再生的方法。该溶液含有具有解离性的布朗斯台德酸化合物 常数范围为约1×10-14至约2×10 -1。