公开(公告)号：US20110201701A1

公开(公告)日：2011-08-18

申请号：US13023510

申请日：2011-02-08

Applicant: Stephen H. Lucas ,  Peter G. Tiverios ,  James R. Jones, JR.

Inventor： Stephen H. Lucas ,  Peter G. Tiverios ,  James R. Jones, JR.

IPC: C07C27/00 ,  B01J8/00

CPC classification number: C10L1/04 ,  B01J19/0006 ,  C07C29/1518 ,  C10G2/32 ,  C10G2/34 ,  C10G47/00 ,  C10J3/26 ,  C10J3/466 ,  C10J3/485 ,  C10J3/721 ,  C10J3/82 ,  C10J2300/0903 ,  C10J2300/0906 ,  C10J2300/0946 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/1628 ,  C10J2300/1634 ,  C10J2300/1643 ,  C10J2300/1659 ,  C10J2300/1665 ,  C10J2300/1671 ,  C10J2300/1675 ,  C10J2300/1815 ,  C10J2300/1853 ,  C10K1/004 ,  C10K1/005 ,  C10K1/101 ,  C10K1/16 ,  C10K3/001 ,  C10K3/04 ,  C10L1/08 ,  C10L2200/0469 ,  C10L2200/0492 ,  C10L2270/023 ,  C10L2270/026 ,  C10L2270/04 ,  C10L2290/04 ,  C10L2290/10 ,  C10L2290/42 ,  C10L2290/54 ,  C10L2290/543 ,  Y02E20/16 ,  Y02E50/18 ,  Y02E50/32 ,  Y02E50/343 ,  Y02P20/129 ,  Y02P20/133 ,  Y02P30/10 ,  C07C31/04 ,  C07C31/08

Abstract: Facilities and processes for generating ethanol from municipal solid waste (MSW) in an economical way via generating a syngas, passing the syngas through a catalytic synthesis reactor, separating fuel grade ethanol, extracting energy at particular strategic points, and recycling undesired byproducts.

Abstract translation: 通过生成合成气，将合成气通过催化合成反应器，分离燃料级乙醇，在特定战略点提取能量，以及回收不期望的副产物，以经济的方式从城市固体废物（MSW）生成乙醇的设施和方法。

公开(公告)号：US07999143B2

公开(公告)日：2011-08-16

申请号：US12193161

申请日：2008-08-18

Applicant: Terry L. Marker ,  Peter Kokayeff ,  Giovanni Faraci ,  Franco Baldiraghi

Inventor： Terry L. Marker ,  Peter Kokayeff ,  Giovanni Faraci ,  Franco Baldiraghi

IPC: C07C4/00 ,  C07C5/13

CPC classification number: C10L1/08 ,  C01B3/16 ,  C01B3/50 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/0455 ,  C01B2203/0475 ,  C01B2203/0485 ,  C01B2203/148 ,  C10G3/46 ,  C10G3/52 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1037 ,  C10G2300/4081 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/28 ,  Y02E50/13 ,  Y02P30/20

Abstract: A process has been developed for producing diesel boiling range fuel from renewable feedstocks such as plant and animal fats and oils. The process involves treating a renewable feedstock by hydrogenating and deoxygenating to provide a hydrocarbon fraction useful as a diesel boiling range fuel. Water is added to the deoxygenation reaction to drive carbon monoxide and water to react to form hydrogen and carbon dioxide. The hydrogen is then consumed by the reactions. If desired, the hydrocarbon fraction can be isomerized to improve cold flow properties.

Abstract translation: 已经开发了用于从可再生原料如植物和动物脂肪和油生产柴油沸点燃料的方法。 该方法包括通过氢化和脱氧处理可再生原料以提供可用作柴油沸程燃料的烃馏分。 将水加入脱氧反应中以驱使一氧化碳和水反应形成氢气和二氧化碳。 然后氢被反应消耗。 如果需要，烃馏分可以被异构化以改善冷流动性能。

公开(公告)号：US07982079B2

公开(公告)日：2011-07-19

申请号：US12208390

申请日：2008-09-11

Applicant: Terry L. Marker ,  Graham D. Ellis ,  Christopher D. Gosling

Inventor： Terry L. Marker ,  Graham D. Ellis ,  Christopher D. Gosling

IPC: C07C4/00

CPC classification number: C10L1/08 ,  C10G3/46 ,  C10G3/52 ,  C10G45/58 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1037 ,  C10G2300/4081 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/28 ,  C11C3/00 ,  C11C3/12 ,  Y02E50/13 ,  Y02P30/20

Abstract: An integrated process has been developed for producing diesel boiling range fuel from renewable feedstocks such as plant and animal fats and oils and using a byproduct naphtha as a denaturant for ethanol. The process involves treating a renewable feedstock by hydrogenating and deoxygenating i.e. decarboxylating, decarbonylating, and/or hydrodeoxygenating to provide a hydrocarbon fraction useful as a diesel fuel or diesel boiling range fuel blending component. If desired, the hydrocarbon fraction can be isomerized to improve cold flow properties. A byproduct naphtha stream from the diesel boiling range fuel production process is used as the denaturant in an alcohol denaturing process for the generation of denaturized ethanol.

Abstract translation: 已经开发了用于从诸如植物和动物脂肪和油的可再生原料生产柴油沸点燃料并且使用副产物石脑油作为乙醇变性剂的综合方法。 该方法包括通过氢化和脱氧处理可再生原料，即脱羧，脱羰和/或加氢脱氧以提供可用作柴油燃料或柴油沸程燃料调配组分的烃馏分。 如果需要，烃馏分可以被异构化以改善冷流动性能。 在用于产生变性乙醇的醇变性过程中，使用来自柴油沸程燃料生产方法的副产物石脑油流作为变性剂。

公开(公告)号：US20110136217A1

公开(公告)日：2011-06-09

申请号：US13026780

申请日：2011-02-14

Applicant: James R. Oyler

Inventor： James R. Oyler

IPC: C12M1/02

CPC classification number: C12P7/649 ,  C10G3/00 ,  C10G3/50 ,  C10G45/00 ,  C10G2300/1014 ,  C10L1/02 ,  C10L1/026 ,  C10L1/08 ,  C10L2200/0476 ,  C10L2270/026 ,  C10L2290/26 ,  C10L2290/544 ,  C11B1/025 ,  C11B3/003 ,  C11C3/04 ,  C12M21/02 ,  C12M21/12 ,  C12M23/58 ,  C12M43/02 ,  C12M47/06 ,  C12P7/065 ,  C12P7/62 ,  C12P7/64 ,  C12P7/6409 ,  Y02E50/13 ,  Y02E50/16 ,  Y02E50/17 ,  Y02P20/125 ,  Y02P30/20

Abstract: A process for production of biofuels from biomass can include depolymerizing a biomass to form a feed. The feed can be formed by autotrophically growing algal biomass and extracting the feed therefrom. The algal feed can be converted to an algal oil by introducing the algal feed to an oil-producing algae under growth conditions sufficient to encourage formation of algal oil within the oil-producing algae. The algal oil can be extracted from the oil-producing algae and can further be converted to biodiesel.

公开(公告)号：US07955820B1

公开(公告)日：2011-06-07

申请号：US12833821

申请日：2010-07-09

Applicant: Nikos Basil Reppas ,  Christian Perry Ridley

Inventor： Nikos Basil Reppas ,  Christian Perry Ridley

IPC: C12P1/00

CPC classification number: C10L1/04 ,  C10L1/02 ,  C10L1/08 ,  C10L2200/0469 ,  C10L2270/026 ,  C12N9/001 ,  C12P5/02 ,  C12P7/04 ,  Y10T436/21 ,  Y10T436/23

Abstract: The present disclosure identifies methods and compositions for modifying photoautotrophic organisms as hosts, such that the organisms efficiently convert carbon dioxide and light into n-alkanes, and in particular the use of such organisms for the commercial production of n-alkanes and related molecules.

Abstract translation: 本公开内容确定用于将光自养生物修饰为宿主的方法和组合物，使得生物有效地将二氧化碳和光转化成正烷烃，特别是使用这种生物来商业生产正烷烃和相关分子。

公开(公告)号：US20110124931A1

公开(公告)日：2011-05-26

申请号：US12939808

申请日：2010-11-04

Applicant: Jianhua YAO ,  Devadas PANJALA ,  Edward L. SUGHRUE, II ,  Eric W. VETTERS ,  Bruce RANDOLPH

Inventor： Jianhua YAO ,  Devadas PANJALA ,  Edward L. SUGHRUE, II ,  Eric W. VETTERS ,  Bruce RANDOLPH

IPC: C10L1/16

CPC classification number: C10M105/38 ,  C10G3/00 ,  C10G3/46 ,  C10G3/49 ,  C10G2300/1011 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2400/04 ,  C10L1/08 ,  C10L1/191 ,  C10L2200/0446 ,  C10L2290/06 ,  C10L2290/56 ,  C10M2207/401 ,  C10N2230/12 ,  Y02P30/20

Abstract: It has been discovered that the residence time of oils/fats in metal apparatus, particularly in the upstream of a hydrotreating unit, for example, a heat exchanger and/or a storage/feed tank, can impact significantly on corrosiveness of oils/fats in combination with and without conventional hydrocarbons. In addition, it is also found that the presence of hydrogen in the metal apparatus can also inhibit the corrosion rate of oils/fats.

Abstract translation: 已经发现，油/脂肪在金属装置中的停留时间，特别是在加氢处理装置的上游，例如热交换器和/或储存/进料罐中的停留时间可以显着地影响油/脂肪的腐蚀性 与和不使用常规碳氢化合物的组合。 此外，还发现金属装置中氢的存在也可以抑制油/脂肪的腐蚀速率。

公开(公告)号：US20110113679A1

公开(公告)日：2011-05-19

申请号：US12901829

申请日：2010-10-11

Applicant: Steven A. Cohen ,  Melvin L. Luetkens, JR. ,  Chander Balakrishnan ,  Robert Snyder

Inventor： Steven A. Cohen ,  Melvin L. Luetkens, JR. ,  Chander Balakrishnan ,  Robert Snyder

IPC: C10L1/19 ,  C07C5/02

CPC classification number: C10G3/42 ,  C07C2/862 ,  C07C6/04 ,  C07C51/09 ,  C07C67/03 ,  C07C67/54 ,  C07C2531/14 ,  C07C2531/24 ,  C10G45/00 ,  C10G45/58 ,  C10G50/00 ,  C10G65/043 ,  C10G69/02 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1092 ,  C10G2300/1096 ,  C10G2300/202 ,  C10G2300/30 ,  C10G2300/301 ,  C10G2300/307 ,  C10G2300/308 ,  C10G2300/44 ,  C10G2400/00 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/20 ,  C10G2400/22 ,  C10L1/026 ,  C10L1/04 ,  C10L1/08 ,  C10L2200/0469 ,  C11B3/00 ,  C11C1/08 ,  C11C3/003 ,  Y02E50/13 ,  Y02P30/20 ,  Y02T50/678 ,  C07C69/533 ,  C07C57/03 ,  C07C57/12 ,  C07C11/02

Abstract: Methods are provided for refining natural oil feedstocks. The methods comprise reacting the feedstock in the presence of a metathesis catalyst under conditions sufficient to form a metathesized product comprising olefins and esters. In certain embodiments, the methods further comprise separating the olefins from the esters in the metathesized product. In certain embodiments, the methods further comprise hydrogenating the olefins under conditions sufficient to form a fuel composition. In certain embodiments, the methods further comprise transesterifying the esters in the presence of an alcohol to form a transesterified product.

Abstract translation: 提供了用于精炼天然油原料的方法。 所述方法包括在复分解催化剂存在下，在足以形成包含烯烃和酯的复分解产物的条件下使原料反应。 在某些实施方案中，所述方法还包括将烯烃与复分解产物中的酯分离。 在某些实施方案中，所述方法还包括在足以形成燃料组合物的条件下氢化所述烯烃。 在某些实施方案中，所述方法还包括在醇存在下酯交酯化以形成酯交换产物。

公开(公告)号：US20110073523A1

公开(公告)日：2011-03-31

申请号：US12888780

申请日：2010-09-23

Applicant: Shouye CUI ,  Youhao XU ,  Zhihai HU ,  Jianhong GONG ,  Chaogang XIE ,  Yun CHEN ,  Zhigang ZHANG ,  Jianwei DONG

Inventor： Shouye CUI ,  Youhao XU ,  Zhihai HU ,  Jianhong GONG ,  Chaogang XIE ,  Yun CHEN ,  Zhigang ZHANG ,  Jianwei DONG

IPC: C10G69/04

CPC classification number: C10G11/18 ,  C10G11/05 ,  C10G55/06 ,  C10G69/04 ,  C10L1/08

Abstract: The present invention relates to a catalytic conversion process for producing more diesel and propylene, comprising contacting the feedstock oil with a catalyst having a relatively homogeneous activity in a reactor, wherein the reaction temperature, weight hourly space velocity and weight ratio of the catalyst/feedstock oil are sufficient to obtain a reaction product containing from 12 to 60% by weight of a fluid catalytic cracking gas oil relative to the weight of the feedstock oil; the fluid catalytic cracking gas oil is fed into the fluid catalytic cracking gas oil treatment device for further processing. Catalytic cracking, hydrogenation, solvent extraction, hydrocracking and process for producing more diesel are organically combined together, and hydrocarbons such as alkanes, alkyl side chains in the feedstocks for catalysis are selectively cracked and isomerized. Meanwhile, aromatics in the feedstocks, which enter into the diesel fraction, are minimized, and the retention of other components in the diesel fraction by the production of aromatics via the reaction such as aromatization and the like is avoided. While the feedstocks are converted into high cetane number diesel and propylene, the yields of dry gas and coke are significantly reduced, and the breaking tendency and consumption of the catalyst are decreased.

Abstract translation: 本发明涉及用于生产更多柴油和丙烯的催化转化方法，包括使原料油与反应器中具有相对均匀的活性的催化剂接触，其中反应温度，重量时空速和催化剂/原料的重量比 油足以获得相对于原料油的重量，含有12至60重量％流化催化裂化瓦斯油的反应产物; 将流化催化裂化瓦斯油送入流化催化裂化瓦斯油处理装置进行进一步处理。 催化裂化，氢化，溶剂萃取，加氢裂化和生产更多柴油的方法有机地结合在一起，烃类如烷烃，用于催化原料的烷基侧链被选择性裂化和异构化。 同时，进入柴油馏分的原料中的芳族化合物被最小化，并且避免了通过诸如芳构化等反应产生芳族化合物而将柴油馏分中其它组分的保留。 当原料转化为高十六烷值的柴油和丙烯时，干气和焦炭的产率显着降低，催化剂的破坏趋势和消耗降低。

公开(公告)号：US20110054230A1

公开(公告)日：2011-03-03

申请号：US12861173

申请日：2010-08-23

Applicant: Kathryn Y. Cole ,  Patrick L. Hanks ,  William E. Lewis

Inventor： Kathryn Y. Cole ,  Patrick L. Hanks ,  William E. Lewis

IPC: C07C1/207

CPC classification number: 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

Abstract: 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.

Abstract translation: 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。

公开(公告)号：US20110011721A1

公开(公告)日：2011-01-20

申请号：US12838175

申请日：2010-07-16

Applicant: Gary E. Champagne

Inventor： Gary E. Champagne

IPC: C10B57/12 ,  B01J29/06 ,  B01D5/00

CPC classification number: C10G1/02 ,  B01J29/06 ,  B01J2229/42 ,  C10B47/44 ,  C10B53/02 ,  C10G1/086 ,  C10G3/49 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4087 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/20 ,  C10L1/023 ,  C10L1/026 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08 ,  C10L3/00 ,  Y02E50/13 ,  Y02E50/14 ,  Y02E50/32 ,  Y02P20/145 ,  Y02P30/20 ,  Y02T50/678

Abstract: A biofuel production method, catalyst and system. The method may include combining a feedstock comprising a carbonaceous material with a consumable catalyst to produce a feedstock/catalyst mixture, and subjecting the feedstock/catalyst mixture to a vacuum pyrolytic gasification and liquefaction process to produce one or more biofuels. The catalyst includes effective amounts of various catalyst constituents, which may include some or all of kaolin, zeolite, amorphous silica, alumina aluminum phosphate and rare earth elements. The system may include apparatus for heating the feedstock/catalyst mixture under selected temperature and vacuum pressure conditions to produce a gaseous effluent comprising one or more hydrocarbon fractions, and additional distillation and condensation apparatus to produce one or more liquid and gaseous fuels.

Abstract translation: 生物燃料生产方法，催化剂和体系。 该方法可以包括将包含碳质材料的原料与可消耗催化剂组合以产生原料/催化剂混合物，以及使原料/催化剂混合物经受真空热解气化和液化过程以产生一种或多种生物燃料。 催化剂包括有效量的各种催化剂组分，其可以包括高岭土，沸石，无定形二氧化硅，氧化铝铝磷酸盐和稀土元素中的一些或全部。 该系统可以包括用于在选择的温度和真空压力条件下加热原料/催化剂混合物以产生包含一种或多种烃馏分的气态流出物以及另外的蒸馏和冷凝装置以产生一种或多种液体和气体燃料的装置。