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71.发明申请PROCESS FOR THE REDUCTION OF GASOLINE BENZENE CONTENT BY ALKYLATION WITH DILUTE ETHYLENE 有权通过与稀释乙烯进行烷基化还原汽油苯含量的方法公开(公告)号：US20110306809A1
公开(公告)日：2011-12-15
申请号：US12813533
申请日：2010-06-11
CPC分类号： C07C2/66 , C07C2529/70 , C07C15/073
摘要： The process converts ethylene in a dilute ethylene stream and dilute benzene in an aromatic containing stream via alkylation to heavier hydrocarbons. The catalyst may be a zeolite such as UZM-8. The catalyst is resistant to feed impurities such as hydrogen sulfide, carbon oxides, and hydrogen and selectively converts benzene. At least 40 wt-% of the ethylene in the dilute ethylene stream and at least 20 wt-% of the benzene in the dilute benzene stream can be converted to heavier hydrocarbons.
摘要翻译： 该方法将稀乙烯流中的乙烯和通过烷基化的含芳烃的物流中的苯稀释成较重的烃。 催化剂可以是沸石如UZM-8。 该催化剂耐受诸如硫化氢，碳氧化物和氢气的杂质，并选择性地转化苯。 稀乙烯流中至少40重量％的乙烯和稀苯流中至少20重量％的苯可以转化为较重的烃。
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72.发明申请Acid Washed Silica Supported Catalysts and Their Use in Olefin Metathesis 有权酸洗二氧化硅负载催化剂及其在烯烃复分解中的应用公开(公告)号：US20110196185A1
公开(公告)日：2011-08-11
申请号：US12701508
申请日：2010-02-05
CPC分类号： B01J23/30 , B01J21/08 , B01J35/1019 , B01J35/1023 , B01J37/0207 , B01J37/06 , C07C6/04 , C07C2521/08 , C07C2523/30 , Y02P20/52 , Y02P20/582 , C07C11/06
摘要： Acid washing of silica supports, used for supported tungsten catalysts, improves the activity of the resulting catalyst (i.e., its conversion level at a given temperature) for the metathesis of olefins, without compromising its selectivity to the desired conversion product(s). Exemplary catalysts and processes include those for the production of valuable light olefins such as propylene from a hydrocarbon feedstock comprising ethylene and butylene.
摘要翻译： 用于支撑的钨催化剂的二氧化硅载体的酸洗可改善所得催化剂的活性（即，在给定温度下的转化水平）用于烯烃的复分解，而不损害其对所需转化产物的选择性。 示例性催化剂和方法包括用于从包含乙烯和丁烯的烃原料生产有价值的轻质烯烃如丙烯的催化剂和方法。
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73.发明申请Support Properties of Silica Supported Catalysts and Their Use in Olefin Metathesis 有权二氧化硅负载催化剂的支持性质及其在烯烃复分解中的应用公开(公告)号：US20110196184A1
公开(公告)日：2011-08-11
申请号：US12701503
申请日：2010-02-05
CPC分类号： B01J23/30 , B01J21/08 , B01J29/0341 , B01J35/023 , B01J35/1019 , B01J35/1023 , B01J35/1061 , B01J37/0201 , B01J37/18 , C07C6/04 , C07C2521/08 , C07C2523/30 , Y02P20/52 , Y02P20/582 , Y02P30/42 , C07C11/06
摘要： Silica supports having a surface area from about 250 m2/g to about 600 m2/g and an average pore diameter from about 45 Å to about 170 Å, used for supported tungsten catalysts, improves the activity of the resulting catalyst (i.e., its conversion level at a given temperature) for the metathesis of olefins, without compromising its selectivity to the desired conversion product(s). Exemplary catalysts and processes include those for the production of valuable light olefins such as propylene from a hydrocarbon feedstock comprising ethylene and butylene.
摘要翻译： 用于负载型钨催化剂的表面积为约250m 2 / g至约600m 2 / g，平均孔径为约45至约为170的二氧化硅载体改善了所得催化剂的活性（即其转化率 在给定温度下的水平）用于烯烃的复分解，而不损害其对所需转化产物的选择性。 示例性催化剂和方法包括用于从包含乙烯和丁烯的烃原料生产有价值的轻质烯烃如丙烯的催化剂和方法。
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公开(公告)号：US20110155635A1
公开(公告)日：2011-06-30
申请号：US12945765
申请日：2010-11-12
申请人： Manuela Serban , Alakananda Bhattacharyya , Beckay J. Mezza , Kurt Vanden Bussche , Christopher P. Nicholas , Warren K. Bennion
发明人： Manuela Serban , Alakananda Bhattacharyya , Beckay J. Mezza , Kurt Vanden Bussche , Christopher P. Nicholas , Warren K. Bennion
CPC分类号： C10G21/06 , C10G21/12 , C10G21/20 , C10G21/24 , C10G21/28 , C10G55/02 , C10G57/00 , C10G2300/107 , C10G2300/1077 , C10G2300/205 , C10G2300/206 , C10G2300/4081 , C10G2300/44 , C10G2300/805
摘要： A process for removing a metal from a resid feed includes contacting the resid feed comprising the metal with a resid-immiscible ionic liquid to produce a resid and resid-immiscible ionic liquid mixture, and separating the mixture to produce a resid effluent having a reduced metal content relative to the resid feed.
摘要翻译： 用于从渣油中除去金属的方法包括将包含金属的残渣进料与残渣不混溶的离子液体接触以产生渣油和残渣不混溶的离子液体混合物，并分离混合物以产生具有还原金属的残渣流出物 相对于残留饲料的内容。
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