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    • 1. 发明申请
    • Alkylation process using chloroaluminate ionic liquid catalysts
    • 使用氯铝酸盐离子液体催化剂的烷基化方法
    • US20060135839A1
    • 2006-06-22
    • US11021165
    • 2004-12-21
    • Saleh ElomariSteve TrumbullHye Kyung TimkenRobert Cleverdon
    • Saleh ElomariSteve TrumbullHye Kyung TimkenRobert Cleverdon
    • C07C2/58
    • C10G29/205C07C2/58C10G50/00C07C9/16
    • A process for the production of a high quality gasoline blending components from refinery process streams by the alkylation of light isoparaffins with olefins using an ionic liquid catalyst is disclosed. The process includes reacting a refinery stream containing isopentane and/or isobutane with a refinery stream containing ethylene and/or propylene and butylenes under alkylation conditions in the presence of a chloroaluminate ionic liquid catalyst comprising a hydrocarbyl substituted pyridinium halide or a hydrocarbyl substituted imidazolium halide of the general formulas A and B, respectively. Where R=H, methyl, ethyl, propyl, butyl, pentyl or hexyl group and X is a halide and preferably a chloride, and R1 and R2=H, methyl, ethyl, propyl, butyl, pentyl or hexyl group and where R1 and R2 may or may not be the same.
    • 公开了一种通过使用离子液体催化剂通过烯烃使轻质异链烷烃烷基化从炼厂工艺流中生产高品质汽油调和组分的方法。 该方法包括在烷基化条件下,在氯铝酸盐离子液体催化剂存在下使包含异戊烷和/或异丁烷的炼油厂物流与含有乙烯和/或丙烯和丁烯的炼油厂物流反应,所述氯铝酸盐离子液体催化剂包含烃基取代的吡啶鎓卤化物或烃基取代的咪唑鎓卤化物 分别是通式A和B。 其中R = H,甲基,乙基,丙基,丁基,戊基或己基,X是卤化物,优选氯化物,R1和R2 = H,甲基,乙基,丙基,丁基,戊基或己基,其中R1和 R2可能或可能不一样。
    • 3. 发明授权
    • Alkylation process using chloroaluminate ionic liquid catalysts
    • 使用氯铝酸盐离子液体催化剂的烷基化方法
    • US07432409B2
    • 2008-10-07
    • US11021165
    • 2004-12-21
    • Saleh ElomariSteve TrumbullHye Kyung C. TimkenRobert Cleverdon
    • Saleh ElomariSteve TrumbullHye Kyung C. TimkenRobert Cleverdon
    • C07C2/54
    • C10G29/205C07C2/58C10G50/00C07C9/16
    • A process for the production of a high quality gasoline blending components from refinery process streams by the alkylation of light isoparaffins with olefins using an ionic liquid catalyst is disclosed. The process includes reacting a refinery stream containing isopentane and/or isobutane with a refinery stream containing ethylene and/or propylene and butylenes under alkylation conditions in the presence of a chloroaluminate ionic liquid catalyst comprising a hydrocarbyl substituted pyridinium chloroaluminate or a hydrocarbyl substituted imidazolium chloroaluminate of the general formulas A and B, respectively. Where R═H, methlyl, ethyl, propyl, butyl, pentyl or hexyl group and X is a chloroaluminate, and R1 and R2=H, methyl, ethyl, propyl, butyl, pentyl or hexyl group and where R1 and R2 may or may not be the same.
    • 公开了一种通过使用离子液体催化剂通过烯烃使轻质异链烷烃烷基化从炼厂工艺流中生产高品质汽油调和组分的方法。 该方法包括在烷基化条件下,在氯铝酸盐离子液体催化剂存在下使包含异戊烷和/或异丁烷的炼油厂物流与含有乙烯和/或丙烯和丁烯的炼油厂物流反应,所述氯铝酸盐离子液体催化剂包含烃基取代的氯铝酸吡啶鎓或氯铝酸盐的烃基取代的咪唑鎓氯铝酸盐 分别是通式A和B。 其中RH,甲基,乙基,丙基,丁基,戊基或己基,X是氯铝酸盐,R1和R2 = H,甲基,乙基,丙基,丁基,戊基或己基,其中R 1和R 2可以是或不是 一样。
    • 7. 发明授权
    • Isolating lubricating oils from subsurface shale formations
    • 隔离地下页岩层的润滑油
    • US08992771B2
    • 2015-03-31
    • US13481303
    • 2012-05-25
    • Marcus Oliver WigandSaleh ElomariRobert Martin Carlson
    • Marcus Oliver WigandSaleh ElomariRobert Martin Carlson
    • C10G1/04E21B43/16E21B43/22E21B43/34C10M101/02C10M105/04C10M177/00F17D1/16
    • C10M101/02C10M105/04C10M177/00C10N2260/02E21B43/16E21B43/34F17D1/16Y10T137/0391
    • Disclosed herein are methods for isolating heavy saturated hydrocarbons from a subsurface shale formation comprising kerogen and an extractible organics component. These methods can be used to provide a bright stock product. The process comprises extracting an extractible organics component from subsurface shale formations comprising kerogen and the extractible organics component in an inorganic matrix and isolating a heavy hydrocarbon fraction comprising saturated beta-carotene. The methods utilize a hydrocarbon solvent to at least partially solubilize the extractible organics component. Among other factors, these processes are based on the discovery that the extractible organics is composed of a heavy hydrocarbon component containing saturated beta-carotene. The saturated beta-carotene product is a valuable commercial product. The presently disclosed processes are more environmentally benign, more economical, and more efficient in producing commercial products and in providing access to kerogen.
    • 本文公开了从含有干酪根和可提取的有机物组分的地下页岩层中分离重饱和烃的方法。 这些方法可用于提供光亮的原料产品。 该方法包括从含有无机基质中的干酪根和可萃取的有机物组分的地下页岩层中提取可提取的有机物组分,并分离包含饱和β-胡萝卜素的重质烃馏分。 该方法利用烃溶剂至少部分增溶可萃取的有机物成分。 除其他因素之外,这些方法是基于以下发现:可萃取的有机物由含有饱和β-胡萝卜素的重质烃组分组成。 饱和β-胡萝卜素产品是有价值的商业产品。 目前公开的方法在生产商业产品和提供对油母质的接触方面更环保,更经济,更有效。