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53 条记录 (耗时 0.049 秒)

    Diesel fuel formulation for reduced emissions
    13.
    发明授权
    Diesel fuel formulation for reduced emissions 有权
    用于减少排放的柴油燃料配方

    公开(公告)号：US07208078B2

    公开(公告)日：2007-04-24

    申请号：US10393167

    申请日：2003-03-20

    申请人： Walter Weissman ,  John T. Farrell ,  Shizuo Sasaki ,  Kazuhiro Akihama ,  Kiyomi Nakakita

    发明人： Walter Weissman ,  John T. Farrell ,  Shizuo Sasaki ,  Kazuhiro Akihama ,  Kiyomi Nakakita

    IPC分类号： C10L1/08

    CPC分类号： C10L1/08

    摘要： The invention is directed to a method and formula for producing a fuel having reduced particulate emissions from an internal combustion engine. The fuel taught herein is characterized as having a cetane number ranging from about 45 to about 65, a T95 distillation property of less than about 370° C., and having NR, AR, cetane number and T95 defined by the relation: PEI=156+Z1×(cetane#−49)+Z2×(NR−14)+Z3×(AR−25)+Z4×(T95−315° C.) Where Z1 ranges from abut 0.67 to about 1.06, Z2 ranges from about 0.9 to about 1.28, Z3 ranges from about 2.54 to about 2.80, Z4 ranges from about 0.1 to about 0.4, NR is a defined correlation of the naphthene rings content in the fuel, and AR is a defined correlation of the aromatic rings content in the fuel.

    摘要翻译： 本发明涉及一种用于生产具有减少的来自内燃机的颗粒物排放的燃料的方法和配方。 本文教导的燃料的特征在于具有约45至约65的十六烷值，小于约370℃的T 95 C蒸馏性能，并且具有NR，AR，十六烷值和T 由<？in-line-formula description =“In-line Formulas”end =“lead”？> PEI = 156 + Z <1> 定义的< 十六烷-49）+ Z 2 x（NR-14）+ Z 3 x（AR-25）+ Z 4 x（T 95℃-315℃）<？in-line-formula description =“In-line Formulas”end =“tail”？>其中Z <1> 范围为0.67 至约1.06，Z 2范围为约0.9至约1.28，Z 3 3范围为约2.54至约2.80，Z 4范围为约 0.1至约0.4，NR是燃料中环烷烃环含量的确定相关性，AR是燃料中芳环含量的确定相关性。

    Onboard fuel separation apparatus for an automobile
    15.
    发明授权
    Onboard fuel separation apparatus for an automobile 失效
    车载式燃油分离装置

    公开(公告)号：US06972093B2

    公开(公告)日：2005-12-06

    申请号：US10248592

    申请日：2003-01-30

    申请人： Randall D. Partridge ,  Walter Weissman ,  Takanori Ueda ,  Yoshihiro Iwashita

    发明人： Randall D. Partridge ,  Walter Weissman ,  Takanori Ueda ,  Yoshihiro Iwashita

    IPC分类号： F02M33/00 ,  C10G31/11 ,  F02D19/06 ,  F02D33/00 ,  F02M25/00 ,  F02M37/00 ,  B01D63/00 ,  F02N17/08

    CPC分类号： F02D33/006 ,  C10G31/11 ,  F02D19/0649 ,  F02D19/0665 ,  F02D19/0671 ,  F02M25/00 ,  F02M37/0064 ,  F02M37/0088 ,  F02M43/00 ,  F02M69/046 ,  Y02T10/36

    摘要： An onboard fuel separation apparatus separates a material fuel (gasoline) into a high-octane fuel having a higher octane value than the material fuel and a low-octane fuel having a lower octane value than the material fuel using a separation membrane which selectively allows high-octane value components (such as aromatic components) permeate through the membrane. The apparatus increases the ratio of the amount of the high-octane value components permeating through the membrane to the amount of the high-octane value components contained in the material fuel by, (A) Controlling the temperature of the material fuel supplied to the membrane (B) Increasing partial pressure of the low-octane value components on the high-octane fuel side of the membrane and removing volatiles from the permeate, and (C) Bypassing volatiles in the material feed around the membrane.

    摘要翻译： 车载燃料分离装置将材料燃料（汽油）分离成具有比材料燃料高的辛烷值的高辛烷值燃料和具有比材料燃料低的辛烷值的低辛烷值燃料，其使用选择性地允许高的辛烷值 - 辛烷值成分（如芳香族成分）渗透膜。 该设备增加通过膜渗透的高辛烷值成分的量与材料燃料中含有的高辛烷值成分的量的比例，（A）控制供给膜的材料燃料的温度 （B）增加隔膜的高辛烷值燃料侧的低辛烷值成分的分压，并从渗透物中除去挥发物，（C）绕膜周围的物料进料旁路挥发物。

    Reactivating iridium and selenium containing catalysts with hydrogen halide and oxygen
    17.
    发明授权
    Reactivating iridium and selenium containing catalysts with hydrogen halide and oxygen 失效
    用卤化氢和氧气重新激活含铱和硒的催化剂

    公开(公告)号：US4491635A

    公开(公告)日：1985-01-01

    申请号：US547874

    申请日：1983-11-02

    申请人： Shun C. Fung ,  Walter Weissman ,  James L. Carter ,  Walter S. Kmak

    发明人： Shun C. Fung ,  Walter Weissman ,  James L. Carter ,  Walter S. Kmak

    IPC分类号： B01J23/96 ,  B01J27/30 ,  C10G35/09 ,  B01J27/02 ,  C10G35/085

    CPC分类号： B01J27/30 ,  B01J23/96 ,  C10G35/09

    摘要： A process is disclosed for reactivating an agglomerated iridium and selenium containing catalyst and particularly platinum-iridium-selenium on alumina reforming catalysts. The process includes contacting a substantially decoked agglomerated catalyst with a reducing gas such as hydrogen to reduce agglomerated iridium oxides present to the free metal, a hydrogen halide pretreatment step to increase the halogen level of the catalyst to about 1.3 weight percent and above, and a redispersion step involving hydrogen halide and elemental oxygen. Use of hydrogen halide and elemental oxygen in the redispersion treatment eliminates the need for use of elemental chlorine gas. If no iridium oxides are initially present, the hydrogen reduction step is optional.

    摘要翻译： 公开了一种用于在氧化铝重整催化剂上重新激活附聚的铱和含硒催化剂，特别是铂 - 铱 - 硒的方法。 该方法包括将基本上已经过的团聚的催化剂与诸如氢的还原气体接触以减少存在于游离金属中的附聚的铱氧化物，将催化剂的卤素水平提高至约1.3重量％以上的卤化氢预处理步骤，以及 再分散步骤涉及卤化氢和元素氧。 在再分散处理中使用卤化氢和元素氧消除了使用元素氯气的需要。 如果最初不存在氧化铱，氢还原步骤是任选的。

    Reactivating iridium-containing catalysts with hydrogen halide and oxygen
    18.
    发明授权
    Reactivating iridium-containing catalysts with hydrogen halide and oxygen 失效
    用卤化氢和氧气再活化含铱催化剂

    公开(公告)号：US4444897A

    公开(公告)日：1984-04-24

    申请号：US374978

    申请日：1982-05-05

    申请人： Shun C. Fung ,  Walter Weissman ,  James L. Carter ,  Walter S. Kmak

    发明人： Shun C. Fung ,  Walter Weissman ,  James L. Carter ,  Walter S. Kmak

    IPC分类号： B01J23/96 ,  B01J23/46 ,  B01J23/64 ,  C10G35/085

    CPC分类号： B01J23/96

    摘要： A process is disclosed for reactivating an agglomerated iridium-containing catalyst and particularly platinum-iridium on alumina reforming catalysts. The process includes contacting a substantially decoked agglomerated catalyst with a reducing gas such as hydrogen to reduce agglomerated iridium oxides present to the free metal, a hydrogen halide pretreatment step to increase the halogen level of the catalyst to about 1.3 weight percent and above, and a redispersion step involving hydrogen halide and elemental oxygen. Use of hydrogen halide and elemental oxygen in the redispersion treatment eliminates the need for use of elemental chlorine gas. If no iridium oxides are initially present, the hydrogen reduction step is optional.

    摘要翻译： 公开了一种重新激活含铱的催化剂，特别是在氧化铝重整催化剂上的铂 - 铱的方法。 该方法包括将基本上已经过的团聚的催化剂与诸如氢的还原气体接触以减少存在于游离金属中的附聚的铱氧化物，将催化剂的卤素水平提高至约1.3重量％以上的卤化氢预处理步骤，以及 再分散步骤涉及卤化氢和元素氧。 在再分散处理中使用卤化氢和元素氧消除了使用元素氯气的需要。 如果最初不存在氧化铱，氢还原步骤是任选的。

    Catalytic cracking process with simultaneous production of a low BTU fuel gas and catalyst regeneration
    19.
    发明授权
    Catalytic cracking process with simultaneous production of a low BTU fuel gas and catalyst regeneration 失效
    催化裂化过程同时生产低BTU燃料气体和催化剂再生

    公开(公告)号：US4421637A

    公开(公告)日：1983-12-20

    申请号：US332161

    申请日：1981-12-18

    申请人： Dane C. Grenoble ,  Walter Weissman

    发明人： Dane C. Grenoble ,  Walter Weissman

    IPC分类号： C01B3/36 ,  C01B3/38 ,  C10G11/04

    CPC分类号： C10G11/04 ,  C01B3/363 ,  C01B3/386 ,  C01B2203/0233 ,  C01B2203/0261 ,  C01B2203/0283 ,  C01B2203/0811 ,  C01B2203/1041 ,  C01B2203/1082 ,  C01B2203/1094 ,  C01B2203/1247 ,  C01B2203/1258 ,  Y02P20/584

    摘要： A process for catalytically cracking a hydrocarbon with simultaneous production of a low BTU fuel gas and catalyst regeneration comprising contacting a hydrocarbon feed, at elevated temperature and in a cracking zone, with a solid acid catalyst comprising a catalytic metal oxide component wherein said metal is selected from the group consisting essentially of (a) tungsten, niobium and mixtures thereof (b) mixture of (a) with tantalum, hafnium, chromium, titanium, zirconium and mixtures thereof, said oxide component being supported on a silica-containing inorganic refractory metal oxide support having a silica content less than 50 wt. % of the total support, to produce a cracked product and a deactivated catalyst and regenerating the deactive catalyst to produce a low BTU gas rich in CO, a gas rich in H.sub.2, or both and recirculating the regenerated catalyst back to the cracking zone, said catalyst being steamed prior to use at a temperature at least 600.degree. C. In a preferred embodiment, the catalyst support will comprise a mixture of silica and .gamma.-alumina.

    摘要翻译： 一种同时生产低BTU燃料气体和催化剂再生的催化裂化烃的方法，包括使烃进料在升高的温度和在裂化区中与包含催化金属氧化物组分的固体酸催化剂接触，其中所述金属被选择 由（a）钨，铌及其混合物组成的组（b）（a）与钽，铪，铬，钛，​​锆及其混合物的混合物，所述氧化物组分负载在含二氧化硅的无机难熔金属 氧化物载体，其二氧化硅含量小于50wt。 产生裂化产物和失活的催化剂并再生该活性催化剂以产生富含CO，富含H 2的二氧化碳或二者的低BTU气体，并将再生催化剂再循环回裂化区，所述 催化剂在使用前在至少600℃的温度下蒸发。在优选的实施方案中，催化剂载体将包含二氧化硅和γ-氧化铝的混合物。