公开(公告)号：US08404917B2

公开(公告)日：2013-03-26

申请号：US12392399

申请日：2009-02-25

申请人： Santi Kulprathipanja ,  Stephen W. Sohn

发明人： Santi Kulprathipanja ,  Stephen W. Sohn

IPC分类号： C07C7/12 ,  C07C7/13 ,  C10G25/08 ,  C10G25/12

CPC分类号： C10G25/03 ,  B01J20/18 ,  B01J20/186 ,  B01J2220/42 ,  C10G2300/104 ,  C10G2300/1044

摘要： A mixed matrix adsorbent is found for use in the removal of light alkanes from a gasoline stream. The mixed matrix comprises two adsorbents with one adsorbent having an LTA type structure and the other adsorbent having an MFI structure.

摘要翻译： 发现混合基质吸附剂用于从汽油流中除去轻质烷烃。 混合基质包含两个吸附剂，其中一个吸附剂具有LTA型结构，另一个吸附剂具有MFI结构。

公开(公告)号：US08394261B2

公开(公告)日：2013-03-12

申请号：US12933898

申请日：2008-10-31

申请人： Kyle E. Litz ,  Tracey M. Jordan ,  Mark N. Rossetti ,  Anthony J. Loughran ,  Jennifer L. Vreeland

发明人： Kyle E. Litz ,  Tracey M. Jordan ,  Mark N. Rossetti ,  Anthony J. Loughran ,  Jennifer L. Vreeland

IPC分类号： C10G25/00

CPC分类号： C10G27/10 ,  B01J31/165 ,  B01J31/2226 ,  B01J31/223 ,  B01J2531/46 ,  C07F7/28 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/1051 ,  C10G2300/1055 ,  C10G2300/202 ,  C10G2300/44

摘要： Catalysts amenable to oxidizing sulfur compounds and systems and methods of using these catalysts to effect the removal of sulfur from crude oil and crude oil distillates are disclosed. The catalyst is disposed with a titanyl moiety which serves to selectively coordinate sulfur compounds and affect their oxidation. The titanyl may be bound within a polymer or on the surface of a polymer or on the surface or in the pores of an inorganic support. The resulting oxidized sulfur compounds are readily separated from the initial crude oil or crude oil distillate streams by traditional separation techniques arrayed as described in the systems and methods disclosed.

公开(公告)号：US20130026066A1

公开(公告)日：2013-01-31

申请号：US13192062

申请日：2011-07-27

申请人： Cemal Ercan ,  Yuguo Wang ,  Mohammad R. Al-Dossary ,  Rashid M. Al-Othman

发明人： Cemal Ercan ,  Yuguo Wang ,  Mohammad R. Al-Dossary ,  Rashid M. Al-Othman

IPC分类号： C10G35/02

CPC分类号： C10G59/06 ,  C10G61/08 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/305 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2400/02

摘要： A process for refining naphtha that results in an improved octane value in a subsequent gasoline blend. Certain embodiments include separating a naphtha feed into light naphtha and heavy naphtha; separating the heavy naphtha into a paraffin stream and non-paraffin stream; introducing the light naphtha to a first isomerization unit, introducing the paraffin stream to a second isomerization unit; introducing the non-paraffin stream to a reforming unit and combining the resulting effluents to form a gasoline blend. The resulting gasoline blend has improved characteristics over gasoline blends that are made without introducing the paraffin stream to a second isomerization unit.

摘要翻译： 精炼石脑油的方法，其导致随后的汽油混合物中改善的辛烷值。 某些实施方案包括将石脑油进料分离成轻质石脑油和重质石脑油; 将重质石脑油分离成石蜡流和非石蜡流; 将轻石脑油引入第一异构化单元，将石蜡流引入第二异构化单元; 将非石蜡流引入重整单元并将所得的流出物组合以形成汽油混合物。 所得到的汽油共混物具有比在不将石蜡流引入第二异构化单元的情况下制备的汽油共混物更好的特性。

公开(公告)号：US20130006028A1

公开(公告)日：2013-01-03

申请号：US13503544

申请日：2010-10-29

申请人： Chaogang Xie ,  Yongcan Gao ,  Weimin Lu ,  Jun Long ,  Yan Cui ,  Jiushun Zhang ,  Yinan Yang ,  Jianguo Ma ,  Zheng Li ,  Nan Jiang

发明人： Chaogang Xie ,  Yongcan Gao ,  Weimin Lu ,  Jun Long ,  Yan Cui ,  Jiushun Zhang ,  Yinan Yang ,  Jianguo Ma ,  Zheng Li ,  Nan Jiang

IPC分类号： C07C1/20 ,  B01J8/24

CPC分类号： C10G51/06 ,  C10G11/18 ,  C10G11/20 ,  C10G51/026 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/104 ,  C10G2300/301 ,  C10G2300/4018 ,  C10G2300/4093 ,  C10G2300/708 ,  C10G2400/02 ,  C10G2400/20

摘要： The present invention discloses catalytic cracking apparatus and process, which are useful for catalytic cracking of heavy oils with a high heavy oil conversion, a high propylene yield and low dry gas and coke yields.

摘要翻译： 本发明公开了一种催化裂化装置和方法，其可用于具有高重油转化率，高丙烯产率和低干气体以及焦炭产率的重油的催化裂化。

公开(公告)号：US20120291340A1

公开(公告)日：2012-11-22

申请号：US13453880

申请日：2012-04-23

申请人： Andries Quirin Maria BOON ,  Johan Willem GOSSELINK ,  John William HARRIS ,  Andries Hendrik JANSSEN ,  Sander VAN PAASEN ,  Colin John SCHAVERIEN ,  Nicolaas Wilhelmus Joseph WAY

发明人： Andries Quirin Maria BOON ,  Johan Willem GOSSELINK ,  John William HARRIS ,  Andries Hendrik JANSSEN ,  Sander VAN PAASEN ,  Colin John SCHAVERIEN ,  Nicolaas Wilhelmus Joseph WAY

IPC分类号： C10L1/00 ,  B01J19/00

CPC分类号： C10G3/57 ,  B01J8/0055 ,  B01J8/1827 ,  B01J8/1872 ,  B01J8/388 ,  C10B49/22 ,  C10B53/02 ,  C10B57/06 ,  C10G1/08 ,  C10G3/50 ,  C10G11/18 ,  C10G2300/1011 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/1051 ,  C10G2300/1055 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/4006 ,  C10G2300/807 ,  C10L1/04 ,  Y02E50/14 ,  Y02E50/32 ,  Y02P30/20

摘要： A process or a system for converting a solid biomass material is provided, comprising contacting the solid biomass material with a catalytic cracking catalyst at a temperature of more than 400° C. in a riser reactor to produce one or more cracked products. The riser reactor contains: a riser reactor pipe, which riser reactor pipe has a diameter that increases in a downstream direction; and a bottom section connected to the riser reactor pipe, which bottom section has a larger diameter than the riser reactor pipe.

摘要翻译： 提供了一种用于转化固体生物质材料的方法或系统，包括在立管反应器中使固体生物质材料与催化裂化催化剂在大于400℃的温度下接触以产生一种或多种裂化产物。 提升管反应器包括：提升管反应器管，其提升管反应器管的直径在下游方向上增加; 以及连接到提升管反应器管的底部，该底部具有比提升管反应器管更大的直径。

公开(公告)号：US20120289752A1

公开(公告)日：2012-11-15

申请号：US13453869

申请日：2012-04-23

申请人： Johan Willem GOSSELINK ,  John William HARRIS ,  Andries Hendrik JANSSEN ,  Sander VAN PAASEN ,  Colin John SCHAVERIEN ,  Nicolaas Wilhelmus Joseph WAY ,  Andries Quirin Maria BOON

发明人： Johan Willem GOSSELINK ,  John William HARRIS ,  Andries Hendrik JANSSEN ,  Sander VAN PAASEN ,  Colin John SCHAVERIEN ,  Nicolaas Wilhelmus Joseph WAY ,  Andries Quirin Maria BOON

IPC分类号： C10G1/00 ,  C10L1/16

CPC分类号： C10G1/08 ,  C10B49/22 ,  C10B53/02 ,  C10B57/02 ,  C10B57/06 ,  C10G3/42 ,  C10G3/50 ,  C10G3/57 ,  C10G11/18 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/1051 ,  C10G2300/1055 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2400/20 ,  C10L1/04 ,  C10L9/083 ,  Y02E50/14 ,  Y02E50/15 ,  Y02E50/32 ,  Y02P20/145 ,  Y02P30/20

摘要： A process for converting a solid biomass material is provided. The solid biomass material and a fluid hydrocarbon feed is contacted with a catalytic cracking catalyst at a temperature of more than 400° C. in a catalytic cracking reactor to produce one or more cracked products which are then fractionated to produce one or more product fractions; then hydrodeoxygenated to produce one or more hydrodeoxygenated products.

摘要翻译： 提供了一种转化固体生物质材料的方法。 将固体生物质材料和流体烃进料在催化裂化反应器中在大于400℃的温度下与催化裂化催化剂接触以产生一种或多种裂化产物，然后将其分馏以产生一种或多种产物级分; 然后加氢脱氧以产生一种或多种加氢脱氧产物。

公开(公告)号：US20120203039A1

公开(公告)日：2012-08-09

申请号：US12931521

申请日：2011-02-03

申请人： Lawrence A. Smith, JR.

发明人： Lawrence A. Smith, JR.

IPC分类号： C10L1/16

CPC分类号： C10L1/04 ,  C10G9/36 ,  C10G45/08 ,  C10G45/38 ,  C10G69/06 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2300/301 ,  C10G2400/02

摘要： A single stage process for treating pyrolysis gasoline containing acetylene, diolefins, sulfur compounds and nitrogen compounds to react a sufficient amount of said acetylene and diolefins with hydrogen to produce saturated products and hydrogen sulfide to provide a pyrolysis gasoline product suitably for use as gasoline blending stock comprising: feeding pyrolysis gasoline and hydrogen at a mol ratio of hydrogen to pyrolysis gasoline of at least 0.5:1 and preferably in the range of 1:1 to 3:1 to a hydrodesulfurization zone containing a hydrodesulfurization catalyst such as cobalt/molybdenum under vapor phase conditions at a pressure in the range of 200 to 500 psig at a temperature in the range of 550° F. to 850° F. The operating temperature is at least above the dew point of the mixture of pyrolysis gasoline and hydrogen, preferably in a range 50 to 400° F. above said dew point.

摘要翻译： 用于处理含有乙炔，二烯烃，硫化合物和氮化合物的裂解汽油的单阶段方法，以使足够量的所述乙炔和二烯烃与氢反应以产生饱和产物和硫化氢，以提供适合用作汽油混合原料的热解汽油产物 包括：以高于摩尔比的氢气将热解汽油和氢气与至少0.5:1，优选在1:1至3:1范围内的热解汽油加入到含有加氢脱硫催化剂例如钴/钼的加氢脱硫区 在550°F至850°F范围内的温度下，在200至500psig范围内的压力下的相位条件。工作温度至少高于热解汽油和氢气的混合物的露点，优选在 在所述露点以上50至400°F的范围。

公开(公告)号：US20120187046A1

公开(公告)日：2012-07-26

申请号：US13010995

申请日：2011-01-21

申请人： Dylan J. Boday ,  Joseph Kuczynski ,  Robert E. Meyer, III ,  Timothy J. Tofil

发明人： Dylan J. Boday ,  Joseph Kuczynski ,  Robert E. Meyer, III ,  Timothy J. Tofil

IPC分类号： B01D71/02 ,  C08J9/26 ,  B01D47/02 ,  B01D39/00 ,  B01D53/22 ,  B01D61/14 ,  C08G77/00 ,  B05D5/00

CPC分类号： B01D71/70 ,  B01D39/1676 ,  B01D53/1456 ,  B01D53/228 ,  B01D61/00 ,  B01D67/0006 ,  B01D2257/304 ,  B01D2323/30 ,  C02F1/44 ,  C02F2101/101 ,  C02F2103/10 ,  C10G31/09 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/1055 ,  C10G2300/202 ,  Y10T156/10

摘要： Sulfur contaminants, such as elemental sulfur (S8), hydrogen sulfide and other sulfur components in fluids (e.g., air, natural gas, and other gases, as well as water and other liquids) are removed using a silicone-based chemical filter/bath. In one embodiment, a silicone-based chemical filter includes a membrane having a cross-linked silicone that is a reaction product of an olefin and a polyhydrosiloxane. For example, sulfur contaminants in air may be removed by passing the air through the membrane before the air enters a data center or other facility housing computer systems. In another embodiment, a silicone-based chemical bath includes a housing having an inlet port, an outlet port, and a chamber containing a silicone oil. For example, sulfur contaminants in air may be removed by passing the air through the silicone oil in the chamber before the air enters a data center or other facility housing computer systems.

摘要翻译： 诸如元素硫（S8），硫化氢和其他流体中的硫成分（如空气，天然气和其他气体，以及水和其他液体）中的硫污染物使用硅氧烷基化学过滤器/浴 。 在一个实施方案中，硅氧烷基化学过滤器包括具有作为烯烃和聚氢硅氧烷的反应产物的交联硅氧烷的膜。 例如，空气中的硫污染物可以在空气进入数据中心或容纳计算机系统的其他设备之前通过空气通过膜而被去除。 在另一个实施方案中，基于硅氧烷的化学浴包括具有入口端口，出口端口和包含硅油的室的壳体。 例如，空气中的硫污染物可以在空气进入数据中心或容纳计算机系统的其它设备之前通过空气通过腔室中的硅油来除去。

公开(公告)号：US08222473B1

公开(公告)日：2012-07-17

申请号：US13334844

申请日：2011-12-22

申请人： Cong-Yan Chen ,  Xiaoying Ouyang ,  Tracy M. Davis ,  Stacey I. Zones

发明人： Cong-Yan Chen ,  Xiaoying Ouyang ,  Tracy M. Davis ,  Stacey I. Zones

IPC分类号： C07C5/27

CPC分类号： C07C5/2775 ,  B01J29/74 ,  B01J29/90 ,  C07C2529/12 ,  C07C2529/22 ,  C07C2529/44 ,  C07C2529/74 ,  C10G45/62 ,  C10G45/64 ,  C10G2300/104 ,  C10G2300/305 ,  C10G2400/02 ,  Y02P20/584 ,  C07C9/16

摘要： A process for isomerizing light paraffins using a catalyst comprising an STI-type zeolite and at least one Group VIII metal. It has been found that the catalyst can selectively convert C6 paraffins into the more favorable higher octane C6 isomer, namely 2,3-dimethylbutane (RON=105), over the less favorable C6 isomer, namely octane 2,2-dimethylbutane (RON=94).

摘要翻译： 使用包含STI型沸石和至少一种VIII族金属的催化剂使轻链烷烃异构化的方法。 已经发现，催化剂可以选择性地将C6链烷烃转化成更有利的较高辛烷值的C6异构体，即2,3-二甲基丁烷（RON = 105），比较不利的C6异构体即辛烷值2,2-二甲基丁烷（RON = 94）。

公开(公告)号：US08128805B2

公开(公告)日：2012-03-06

申请号：US10257889

申请日：2001-04-18

申请人： Marius Vaarkamp

发明人： Marius Vaarkamp

IPC分类号： C10G45/10 ,  C10G47/14 ,  C07C5/02 ,  C07C5/22

CPC分类号： C10G49/08 ,  B01J21/12 ,  B01J29/06 ,  B01J29/084 ,  B01J29/80 ,  B01J37/0246 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/1051 ,  C10G2300/1055 ,  C10G2300/1059 ,  C10G2300/202 ,  C10G2400/04

摘要： A catalyst for the hydrogenation, hydroisomerisation, hydrocracking and/or hydrodesulfurisation, of hydrocarbon feedstocks, the catalyst consisting of a substantially binder free bead type support material obtained through a sol-gel method, and a catalytically active component selected from precious metals, the support comprising 5 to 50 wt. % of at least one molecular sieve material and 50 to 95 wt. % of silica-alumina.

摘要翻译： 用于烃原料的氢化，加氢异构化，加氢裂化和/或加氢脱硫的催化剂，由通过溶胶 - 凝胶法获得的基本上无粘结剂的珠型载体材料和选自贵金属的催化活性组分，所述载体 包含5至50wt。 ％的至少一种分子筛材料和50至95wt。 ％的二氧化硅 - 氧化铝。