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1. 发明授权

US4151070A Staged slurry hydroconversion process 失效
标题翻译：分级浆液加氢转化法
公开(公告)号：US4151070A
公开(公告)日：1979-04-24
申请号：US862341
申请日：1977-12-20
申请人： David E. Allan , William E. Lewis
发明人： David E. Allan , William E. Lewis
IPC分类号： C10G49/12 , C10G65/02 , C10G13/06 , C10G37/02
CPC分类号： C10G49/12 , C10G65/02
摘要： A staged hydrocarbon hydroconversion process is provided in which a portion of the product boiling up to an atmospheric pressure distillation cut point of about 1050.degree. F. is removed between the stages and in which the first stage is operated at lower severity than the second stage.
摘要翻译：提供了分阶段的烃加氢转化方法，其中沸腾至大约1050°F的大气压蒸馏馏分的产物的一部分在阶段之间被除去，其中第一阶段以比第二阶段更低的严重程度运行。

2. 发明授权

US4137149A Slurry hydrogen treating processes 失效
标题翻译：浆液氢处理工艺
公开(公告)号：US4137149A
公开(公告)日：1979-01-30
申请号：US810913
申请日：1977-06-29
申请人： David E. Allan , William E. Lewis , William J. Metrailer
发明人： David E. Allan , William E. Lewis , William J. Metrailer
IPC分类号： C10G47/26 , C10G49/22 , C10G13/18 , C10G23/10
CPC分类号： C10G47/26 , C10G49/22
摘要： The liquid product of a slurry hydrogen treating zone is separated into fractions in the same separation zone used to obtain the heavy hydrocarbonaceous oil fraction used as feed for the hydrogen treating zone. A separate portion of coarser solids is withdrawn from the hydrogen treating zone.
摘要翻译：将浆液氢处理区的液体产物在用于获得用作氢处理区的进料的重质烃油馏分的相同分离区中分离成馏分。从氢处理区抽出较粗的固体的单独部分。

3. 发明授权

US08822744B2 Multi-stage co-processing of biofeeds for manufacturing of diesel range hydrocarbons 有权
标题翻译：用于生产柴油范围烃类的生物饲料的多阶段协同处理
公开(公告)号：US08822744B2
公开(公告)日：2014-09-02
申请号：US12809294
申请日：2007-12-20
申请人： Tahmid I. Mizan , Zhiguo Hou , William E. Lewis
发明人： Tahmid I. Mizan , Zhiguo Hou , William E. Lewis
IPC分类号： C07C1/00 , C10G65/04
CPC分类号： C10G3/45 , C10G3/46 , C10G3/50 , C10G2300/1014 , C10G2300/1074 , C10G2300/202 , C10G2300/301 , C10G2300/4018 , C10G2300/4081 , C10G2400/04 , Y02P30/20
摘要： Processes are provided for producing a diesel fuel product having a sulfur content of 10 ppm by weight or less from feed sources that include up to 10% by weight of a biocomponent feedstock. The mineral hydrocarbon portions of the feed sources can be distillate or heavier feed sources.
摘要翻译：提供了用于生产含有至多10重量％生物组分原料的进料源含硫量为10重量ppm以下的柴油燃料产品的方法。进料源的矿物烃部分可以是馏出物或较重的进料源。

4. 发明授权

US08816141B2 Reducing hydrogen consumption in hydrotreating of biocomponent feeds 有权
标题翻译：降低生物组分加氢处理中的氢消耗
公开(公告)号：US08816141B2
公开(公告)日：2014-08-26
申请号：US12861173
申请日：2010-08-23
申请人： Kathryn Y. Cole , Patrick L. Hanks , William E. Lewis
发明人： Kathryn Y. Cole , Patrick L. Hanks , William E. Lewis
IPC分类号： C07C1/00
CPC分类号： C10G3/45 , C10G3/44 , C10G3/46 , C10G3/48 , C10G3/50 , C10G3/52 , C10G3/60 , C10G45/02 , C10G45/58 , C10G2300/1011 , C10G2300/1014 , C10G2300/1055 , C10G2300/4018 , C10G2300/4081 , C10G2300/42 , C10G2400/04 , C10L1/08 , Y02P30/20
摘要： Processes are provided for deoxygenation of a biocomponent feedstock with reduced hydrogen consumption. The biocomponent feedstock can be processed under relatively low hydrogen partial pressures and at a relatively low treat gas ratio compared to the hydrogen need of the feedstock. The relatively low pressure, relatively low treat gas ratio hydroprocessing can result in reduced production of water and carbon monoxide and in increased production of carbon dioxide compared to relatively higher pressure process conditions.
摘要翻译：为生物组分原料脱氧提供了减少氢消耗的方法。生物组分原料可以在相对低的氢分压下以相对较低的处理气体比例与原料的氢气需求相比进行处理。相对低压，相对较低的处理气体比例加氢处理可以导致水和一氧化碳的产生减少，并且与相对较高的压力过程条件相比，二氧化碳的产生增加。

5. 发明授权

US08785701B2 Co-processing of diesel biofeed and kerosene range hydrocarbons 有权
标题翻译：柴油生物饲料和煤油范围烃的协同加工
公开(公告)号：US08785701B2
公开(公告)日：2014-07-22
申请号：US12653480
申请日：2009-12-15
申请人： Kathryn Y. Cole , William E. Lewis
发明人： Kathryn Y. Cole , William E. Lewis
IPC分类号： C07C1/20 , C07C4/06 , C10G45/00
CPC分类号： C10G3/50 , C10G3/46 , C10G45/02 , C10G65/043 , C10G2300/1014 , C10G2300/1018 , C10G2300/1051 , C10G2300/202 , C10G2300/4006 , C10G2300/4018 , C10G2400/04 , C10G2400/08 , Y02E50/13 , Y02P30/20
摘要： Processes are provided for producing a diesel fuel product having a sulfur content of 10 ppm by weight or less from feed sources that include up to 50% by weight of a biocomponent feedstock. The biocomponent feedstock is co-processed with a heavy oil feed in a severe hydrotreating stage. The product from the severe hydrotreatment stage is fractionated to separate out a diesel boiling range fraction, which is then separately hydrotreated.
摘要翻译：提供了用于生产具有包含至多50重量％的生物组分原料的进料源的硫含量为10重量ppm以下的柴油燃料产品的方法。生物组分原料在重质加氢处理阶段与重油进料共处理。将来自严重加氢处理阶段的产物分馏以分离柴油沸程馏分，然后分别加氢处理。

6. 发明授权

US08632675B2 Co-processing of diesel biofeed and heavy oil 有权
标题翻译：柴油生物饲料和重油的协同加工
公开(公告)号：US08632675B2
公开(公告)日：2014-01-21
申请号：US12653459
申请日：2009-12-15
申请人： Kathryn Y. Cole , William E. Lewis
发明人： Kathryn Y. Cole , William E. Lewis
IPC分类号： C10G65/04 , C10G65/10 , C10G45/02
CPC分类号： C10G45/64 , C10G65/12 , C10G69/02 , C10G2300/1011 , C10G2300/202 , C10G2400/04 , C10G2400/10 , Y02P30/20
摘要： Processes are provided for producing a diesel fuel product having a sulfur content of 10 ppm by weight or less from feed sources that include up to 50% by weight of a biocomponent feedstock. The biocomponent feedstock is co-processed with a heavy oil feed in a severe hydrotreating stage. The product from the severe hydrotreatment stage is fractionated to separate out a diesel boiling range fraction, which is then separately hydrotreated.
摘要翻译：提供了用于生产具有包含至多50重量％的生物组分原料的进料源的硫含量为10重量ppm以下的柴油燃料产品的方法。生物组分原料在重质加氢处理阶段与重油进料共处理。将来自严重加氢处理阶段的产物分馏以分离柴油沸程馏分，然后分别加氢处理。

7. 发明申请

US20120000824A1 INTEGRATED GAS AND LIQUID PHASE PROCESSING OF BIOCOMPONENT FEEDSTOCKS 有权
标题翻译：生物活性物质的气相和液相加工
公开(公告)号：US20120000824A1
公开(公告)日：2012-01-05
申请号：US13168287
申请日：2011-06-24
申请人： Richard C. Dougherty , Michael A. Hayes , Benjamin S. Umansky , William E. Lewis
发明人： Richard C. Dougherty , Michael A. Hayes , Benjamin S. Umansky , William E. Lewis
IPC分类号： C10G45/00
CPC分类号： C10G65/04 , C10G3/50 , C10G3/60 , C10G2300/1014 , C10G2300/1018 , C10G2300/1037 , C10G2300/202 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2300/4081 , C10G2400/04 , Y02P30/20
摘要： A mineral feed can be hydrotreated in a trickle-bed reactor or other stage in a continuous gas-phase environment. The effluent from the hydrotreatment stage can be separated to remove gas-phase impurities. The remaining liquid effluent from the hydrotreating stage can then be introduced, in total or in part, into a second stage/reactor. A feed of biocomponent origin can also be introduced into the second stage/reactor. The second stage/reactor can be operated to perform deoxygenation of the mixture of biocomponent feed and hydrotreated liquid effluent in a continuous liquid phase environment.
摘要翻译：矿物饲料可以在连续气相环境中的滴流床反应器或其他阶段进行加氢处理。来自加氢处理阶段的流出物可以分离以除去气相杂质。然后可以将来自加氢处理阶段的剩余液体流出物全部或部分地引入第二阶段/反应器中。生物成分来源的饲料也可以引入第二阶段/反应器。可以操作第二阶段/反应器以在连续液相环境中对生物组分进料和加氢处理的液体流出物的混合物进行脱氧。

8. 发明申请

US20070278135A1 Hydrocracker post-treat catalyst for production of low sulfur fuels 有权
标题翻译：用于生产低硫燃料的加氢裂化器后处理催化剂
公开(公告)号：US20070278135A1
公开(公告)日：2007-12-06
申请号：US11446251
申请日：2006-06-02
申请人： William J. Tracy , Chuansheng Bai , Robert A. Bradway , William E. Lewis , Randolph J. Smiley
发明人： William J. Tracy , Chuansheng Bai , Robert A. Bradway , William E. Lewis , Randolph J. Smiley
IPC分类号： C10G65/00 , C10G69/00
CPC分类号： C10G65/12 , B01J23/883 , B01J23/8885 , B01J31/10 , C10G45/08
摘要： A hydrocracking process for converting a petroleum feedstock to higher gravity, lower sulfur products, especially ultra low sulfur road diesel fuel. The process may be operated as a single-stage or two-stage hydrocracking. In each case, a hydrocracking step is followed directly by a post-treat hydrodesulfurization zone using a bulk multimetallic catalyst comprised of at least one Group VIII non-noble metal and at least two Group VIB metals with a ratio of Group VIB metal to Group VIII non-noble metal is from about 10:1 to about 1:10. In the two-stage option with interstage ammonia removal, the initial hydrocracking step may be followed by hydrodesulfurization using the bulk multimetallic catalyst prior to the ammonia removal which is followed by the second hydrocracking step. A final hydrodesulfurization over the bulk multimetallic catalyst may follow. The hydrodesulfurization over the bulk multimetallic catalyst is carried out at a pressure of at least 25 barg and preferably at least 40 barg.
摘要翻译：用于将石油原料转化为更高重力，较低硫产物，特别是超低硫道路柴油的加氢裂化方法。该方法可以作为单级或两级加氢裂化操作。在每种情况下，加氢裂化步骤直接通过后处理加氢脱硫区，使用由至少一种VIII族非贵金属和至少两种VIB族金属与VIII族的VIB族金属组成的本体多金属催化剂非贵金属为约10:1至约1:10。在阶段氨除去的两阶段选择中，初始加氢裂化步骤之后可以在除氨之前使用大量多金属催化剂进行加氢脱硫，其后是第二加氢裂化步骤。可以遵循大量多金属催化剂的最终加氢脱硫。本体多金属催化剂上的加氢脱硫在至少25barg，优选至少40barg的压力下进行。

9. 发明授权

US4740295A Hydroconversion process using a sulfided molybdenum catalyst concentrate 失效
标题翻译：使用硫化钼催化剂浓缩物的加氢转化法
公开(公告)号：US4740295A
公开(公告)日：1988-04-26
申请号：US944444
申请日：1986-12-22
申请人： Roby Bearden, Jr. , Clyde L. Aldridge , Francis X. Mayer , James H. Taylor , William E. Lewis
发明人： Roby Bearden, Jr. , Clyde L. Aldridge , Francis X. Mayer , James H. Taylor , William E. Lewis
IPC分类号： B01J23/28 , B01J27/19 , B01J37/20 , C10G47/26 , C10G47/02 , C10G1/08
CPC分类号： C10G47/26 , B01J23/28 , B01J27/19 , B01J37/20
摘要： Hydroconversion processes utilizing a catalyst prepared from a catalyst precursor concentrate such as phosphomolybdic acid, is provided. The catalyst precursor concentrate is treated at relatively low pressures in a specified manner.
摘要翻译：提供了使用由催化剂前体浓缩物如磷钼酸制备的催化剂的加氢转化方法。催化剂前体浓缩物以指定的方式在相对低的压力下处理。

10. 发明授权

US4656840A Container for freezable liquid 失效
标题翻译：集装箱可冻结液体
公开(公告)号：US4656840A
公开(公告)日：1987-04-14
申请号：US802735
申请日：1985-11-29
申请人： James G. Loofbourrow , William E. Lewis , Robert J. Pelton
发明人： James G. Loofbourrow , William E. Lewis , Robert J. Pelton
IPC分类号： B65D21/024 , F25D3/08
CPC分类号： F25D3/08 , F25D2303/08221 , Y10T428/24008
摘要： A container filled with a freezable liquid for use in refrigerating or temporarily cooling purposes. The container of the invention is generally rectangular and has two plugs each on its face and one side. Opposite these plugs and in contra position to the plugs, on the back and other side of the container, are corresponding recesses. The recesses and plugs are formed in order that the plugs of one container fit into the recesses of a like container, thus allowing the containers to be fastened together. Thus, when filled with freezable liquid and frozen, two or more containers may be connected, at either their sides or face-to-back, to form blocks of frozen containers. In addition to the advantages of using containers filled with freezable liquid over using water-ice as a coolant, which advantages have been found in the prior art, use of blocks of the frozen containers of the present invention provides longer lasting cooling capability and the convenience of the cooling medium being adaptable to the size and shape of the cooling compartment.
摘要翻译：填充有用于制冷或临时冷却目的的可冷冻液体的容器。本发明的容器通常是矩形的，并且在其表面和一侧上具有两个插头。与这些插头相反并且与容器的背面和另一侧上的塞子相反的位置是相应的凹槽。形成凹部和塞子，使得一个容器的塞子装配到类似的容器的凹部中，从而允许容器紧固在一起。因此，当填充有可冷冻液体并冷冻时，两个或更多个容器可以在其两侧或面对面地连接以形成冷冻容器块。除了使用装有可冷冻液体的容器以使用水冰作为冷却剂的优点之外，在现有技术中已经发现了这些优点，因此本发明的冷冻容器块的使用提供了更持久的冷却能力和便利性的冷却介质适于冷却室的尺寸和形状。

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