公开(公告)号：US20110014665A1

公开(公告)日：2011-01-20

申请号：US12772170

申请日：2010-04-30

Applicant: Donald E. Trimbur ,  Chung-Soon Im ,  Harrison F. Dillon ,  Anthony G. Day ,  Scott Franklin ,  Anna Coragliotti

Inventor： Donald E. Trimbur ,  Chung-Soon Im ,  Harrison F. Dillon ,  Anthony G. Day ,  Scott Franklin ,  Anna Coragliotti

IPC: C12P7/64 ,  C12N1/13

CPC classification number: C10L1/026 ,  C07H21/04 ,  C10L1/06 ,  C10L2200/0484 ,  C10L2270/026 ,  C10L2270/04 ,  C11C3/00 ,  C12N1/12 ,  C12N1/32 ,  C12N9/0006 ,  C12N9/0008 ,  C12N9/1205 ,  C12N9/14 ,  C12N9/16 ,  C12N9/20 ,  C12N9/2408 ,  C12N9/2431 ,  C12N9/88 ,  C12N15/79 ,  C12P5/02 ,  C12P7/6409 ,  C12P7/6436 ,  C12P7/6445 ,  C12P7/6463 ,  C12P7/649 ,  C12P21/06 ,  C12Y302/01026 ,  Y02E50/10 ,  Y02E50/13 ,  Y02E50/343 ,  Y02P20/52 ,  Y02T50/678

Abstract: The invention provides methods of cultivating oil-bearing microbes using cellulosic material. Also provided are microorganisms containing one or more exogenous genes that facilitate the use of cellulosic materials as a feedstock. Also provided are microorganisms and methods for manufacturing non-alcohol-based fuels and fuel feedstocks through a process of converting cellulosic materials into oils.

Abstract translation: 本发明提供使用纤维素材料培养含油微生物的方法。 还提供了含有一种或多种促进使用纤维素材料作为原料的外源基因的微生物。 还提供了通过将纤维素材料转化为油的方法来制造非醇类燃料和燃料原料的微生物和方法。

公开(公告)号：US20110000128A1

公开(公告)日：2011-01-06

申请号：US12682511

申请日：2009-03-04

Applicant: Rudolf W. Gunnerman ,  Peter W. Gunnerman

Inventor： Rudolf W. Gunnerman ,  Peter W. Gunnerman

IPC: C10L1/12 ,  C10L1/10

CPC classification number: B01J35/06 ,  B01J23/30 ,  B01J23/745 ,  B01J23/75 ,  B01J23/755 ,  B01J23/888 ,  B01J23/8892 ,  C10G2/332 ,  C10G2/341 ,  C10G29/02 ,  C10G29/205 ,  C10G49/007 ,  C10G49/04 ,  C10G50/00 ,  C10G2300/1025 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/1051 ,  C10G2300/1055 ,  C10G2300/1059 ,  C10G2300/4006 ,  C10G2300/70 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08

Abstract: Biogases such as natural gas and other gases capable of being biologically derived by digestion of organic matter are converted to a clean-burning hydrocarbon liquid fuel in a process wherein a biogas is fed to a reaction vessel where the biogas contacts a liquid petroleum fraction and a transition metal catalyst immersed in the liquid, vaporized product gas is drawn from a vapor space above the liquid level, condensed, and fed to a product vessel where condensate is separated from uncondensed gas and drawn off as the liquid product fuel. Uncondensed gas can be recycled to the reaction vessel.

Abstract translation: 生物气体如天然气和能够通过有机物消化生物衍生的其它气体在其中将生物气体进料到反应容器中的过程中转化为清洁燃烧的烃液体燃料，其中生物气体接触液体石油馏分和 浸没在液体中的过渡金属催化剂，蒸发的产物气体从液面上方的蒸气空间中抽出，冷凝，并进料到产物容器中，其中冷凝物与未冷凝的气体分离并作为液体产物燃料排出。 未冷凝的气体可以再循环到反应容器中。

公开(公告)号：US20100299991A1

公开(公告)日：2010-12-02

申请号：US12676745

申请日：2008-09-05

Applicant: Gerardus Johannes Maria Gruter

Inventor： Gerardus Johannes Maria Gruter

IPC: C10L1/185 ,  C07D307/58

CPC classification number: C07D307/46 ,  C10L1/023 ,  C10L1/026 ,  C10L1/06 ,  C10L1/08 ,  C10L1/1857 ,  C10L10/02 ,  C10L10/12 ,  Y02E50/13 ,  Y02P20/127

Abstract: The current invention provides a method for the manufacture of an ether of 5-hydroxymethylfurfural by reacting a hexose-containing starting material with an olefin in the presence of an acid catalyst

Abstract translation: 本发明提供了一种通过使含己糖的原料与烯烃在酸催化剂存在下反应制备5-羟甲基糠醛醚的方法

公开(公告)号：US07837860B1

公开(公告)日：2010-11-23

申请号：US11299855

申请日：2005-12-12

Applicant: Richard K. Hoehn ,  Srinivasa G. Varadarajan ,  Douglas W. Kocher-Cowan

Inventor： Richard K. Hoehn ,  Srinivasa G. Varadarajan ,  Douglas W. Kocher-Cowan

IPC: C10G44/00 ,  C10G44/02

CPC classification number: C10G47/12 ,  C10G45/06 ,  C10G47/14 ,  C10G47/18 ,  C10G47/20 ,  C10G65/12 ,  C10G65/14 ,  C10G2300/1096 ,  C10G2300/305 ,  C10G2300/4056 ,  C10G2400/02 ,  C10L1/06

Abstract: A process for the production of low sulfur diesel and high octane naphtha. Separate high pressure vapor liquid separators serve to maintain and isolate the high octane naphtha produced in the hydrocracking zone thereby maximizing the value of the hydrocarbon streams produced.

Abstract translation: 一种生产低硫柴油和高辛烷值的石脑油的方法。 单独的高压蒸汽液体分离器用于维持和分离在加氢裂化区产生的高辛烷值石脑油，从而使产生的烃流的值最大化。

公开(公告)号：US07820867B2

公开(公告)日：2010-10-26

申请号：US12063021

申请日：2006-08-16

Applicant: Finn Joensen ,  Bodil Voss ,  Jesper Nerlov

Inventor： Finn Joensen ,  Bodil Voss ,  Jesper Nerlov

IPC: C07C1/00 ,  C07C27/00

CPC classification number: C07C29/151 ,  C10G3/00 ,  C10G3/49 ,  C10G2300/1022 ,  C10G2300/4081 ,  C10G2400/02 ,  C10L1/06 ,  Y02P30/20 ,  C07C31/04

Abstract: Process for converting oxygenate compounds to hydrocarbons comprising the steps: (a) introducing a feed stream of synthesis gas to a synthesis section for the production of easily convertible oxygenates, (b) passing the effluent stream from said synthesis section containing easily convertible oxygenates to a gasoline synthesis section, (c) passing the effluent of said gasoline synthesis section to a separator and withdrawing from said separator hydrocarbons boiling in the gasoline boiling range, (d) admixing a recycle stream from the separator containing unconverted synthesis gas volatile hydrocarbons with the feed stream of synthesis gas of step (a), (e) introducing a feed containing difficulty convertible oxygenates to the synthesis section of step (a).

Abstract translation: 将含氧化合物转化为烃的方法，包括以下步骤：（a）将合成气的进料流引入合成段，以生产容易转化的含氧化合物，（b）将含有易转化含氧化合物的合成段的流出物流送至 汽油合成段，（c）将所述汽油合成段的流出物通入分离器并从汽油沸程沸腾的所述分离器中取出，（d）将含有未转化的合成气挥发性烃的分离器的再循环流与进料混合 步骤（a）的合成气流，（e）将含有难以转化的含氧化合物的进料引入步骤（a）的合成部分。

公开(公告)号：US20100170826A1

公开(公告)日：2010-07-08

申请号：US12278961

申请日：2008-03-14

Applicant: Lisa Friedman ,  Mathew Rude

Inventor： Lisa Friedman ,  Mathew Rude

IPC: C10L1/04 ,  C10G11/05 ,  C10G11/02 ,  C12P1/00

CPC classification number: C12N9/1025 ,  C10G11/00 ,  C10G11/05 ,  C10G11/18 ,  C10G2300/1011 ,  C10G2300/301 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/00 ,  C10L1/023 ,  C10L1/026 ,  C10L1/06 ,  C10L1/08 ,  C12N9/1029 ,  C12P7/649 ,  Y02E50/13 ,  Y02P30/20

Abstract: Described herein are methods for cracking a biocrude, particularly catalytically cracking a biocrude that primarily includes olefmic hydrocarbons. Also described herein are compositions and methods of producing such compositions that are useful as fuels or fuel production feedstock.

Abstract translation: 本文描述了用于裂化生物粗体，特别是催化裂化主要包括烯烃的生物粗料的方法。 本文还描述了可用作燃料或燃料生产原料的组合物的组合物和方法。

公开(公告)号：US20100144907A1

公开(公告)日：2010-06-10

申请号：US12316209

申请日：2008-12-10

Applicant: Charles L. Kibby ,  Allen W. Burton, JR. ,  Alfred Hass ,  Simon Holz

Inventor： Charles L. Kibby ,  Allen W. Burton, JR. ,  Alfred Hass ,  Simon Holz

IPC: C07C1/00

CPC classification number: B01J35/0006 ,  B01J23/26 ,  B01J29/87 ,  B01J35/1019 ,  B01J37/031 ,  B01J37/18 ,  C01B39/082 ,  C10G2/33 ,  C10G2/334 ,  C10L1/06

Abstract: A process is described for converting synthesis gas containing carbon monoxide and hydrogen to hydrocarbons via methanol as an intermediate, by contacting the synthesis gas with a catalyst system containing a mixture of gallium silicate zeolite catalyst and a methanol catalyst. The process results in reduced amounts of undesirable low carbon number hydrocarbons, e.g., C4 and lower, undesirable high carbon number hydrocarbons, e.g., C10 and higher, and aromatic hydrocarbons. The process provides higher yields of useful, high octane hydrocarbons boiling in the gasoline range.

Abstract translation: 描述了通过使合成气与含有硅酸镓沸石催化剂和甲醇催化剂的混合物的催化剂体系接触来将含有一氧化碳和氢的合成气转化为甲醇作为中间体的方法。 该方法导致不期望的低碳数烃的量减少，例如C4和更低的不期望的高碳数烃，例如C10和更高级的芳族烃。 该方法提供了在汽油范围内沸腾的有用的高辛烷值的较高产率。

公开(公告)号：US20100121120A1

公开(公告)日：2010-05-13

申请号：US12607809

申请日：2009-10-28

Applicant: Bruce B. Randolph ,  Bruce Welch ,  Roland Schmidt ,  Edward L. Sughrue, II

Inventor： Bruce B. Randolph ,  Bruce Welch ,  Roland Schmidt ,  Edward L. Sughrue, II

IPC: C07C2/00 ,  C07C11/02

CPC classification number: C10G35/04 ,  C10G29/205 ,  C10G50/00 ,  C10L1/06

Abstract: A process for upgrading hydrocarbons comprising removal of C5 hydrocarbons from a feedstock, metathesizing said C5 hydrocarbons to C6+ and C4− hydrocarbons, and upgrading said C4− hydrocarbons is disclosed.

Abstract translation: 公开了一种用于升级烃的方法，包括从原料中除去C5烃，将所述C5烃分解为C6 +和C4-烃，并升级所述C4-烃。

公开(公告)号：US07671245B2

公开(公告)日：2010-03-02

申请号：US12431769

申请日：2009-04-29

Applicant: Jason A. Ryder

Inventor： Jason A. Ryder

IPC: C10L1/16

CPC classification number: C10L1/04 ,  C10L1/06 ,  C10L1/08 ,  C10L1/1608 ,  C10L1/1616 ,  Y10S208/95

Abstract: Provided herein are, among other things, jet fuel compositions and methods of making and using the same. In some embodiments, the fuel compositions comprise at least a fuel component readily and efficiently produced, at least in part, from a microorganism. In certain embodiments, the fuel compositions provided herein comprise a high concentration of at least a bioengineered fuel component. In further embodiments, the fuel compositions provided herein comprise amorphane.

Abstract translation: 喷雾燃料组合物及其制备和使用方法尤其如此。 在一些实施方案中，燃料组合物至少部分地由微生物包含至少一种燃料成分，并且至少部分地有效地产生。 在某些实施方案中，本文提供的燃料组合物包含高浓度的至少一种生物工程燃料组分。 在另外的实施方案中，本文提供的燃料组合物包括不可见的。

公开(公告)号：US20100030003A1

公开(公告)日：2010-02-04

申请号：US12448216

申请日：2007-12-11

Applicant: Jean-Marie Basset ,  Francois Stoffelbach ,  Mostafa Taoufik ,  Jean Thivolle-Cazat

Inventor： Jean-Marie Basset ,  Francois Stoffelbach ,  Mostafa Taoufik ,  Jean Thivolle-Cazat

IPC: C07C6/00

CPC classification number: C10L1/06 ,  B01J21/04 ,  B01J31/121 ,  B01J37/0209 ,  B01J2531/66 ,  C07C6/04 ,  C07C2521/04 ,  C07C2531/12 ,  C07C11/107

Abstract: The present invention relates to a process for manufacturing neohexene, comprising contacting isobutene with a supported catalyst comprising a tungsten compound chosen from tungsten hydrides, organometallic tungsten compounds and organometallic tungsten hydrides, and a support comprising an oxide of aluminium, so as to form a reaction mixture comprising neohexene, and preferably separating neohexene from the reaction mixture, so as to isolate it. The contacting leads to the direct production of neohexene, in particular in a single (reaction) stage and with a high molar selectivity for neohexene. The contacting can be performed at a temperature of 50 to 600° C., under a total absolute pressure of 0.01 to 100 MPa.

Abstract translation: 本发明涉及一种制备新己烯的方法，包括使异丁烯与包含选自氢化钨，有机金属钨化合物和有机金属氢化钨的钨化合物的负载催化剂和包含铝氧化物的载体接触，以形成反应 包含新己烯的混合物，优选从反应混合物中分离新己烯，以便将其分离。 接触导致新己烯的直接生产，特别是在单一（反应）阶段和对新己烯的高摩尔选择性。 接触可以在50〜600℃的温度下，在0.01〜100MPa的绝对压力下进行。