公开(公告)号：US09790439B2

公开(公告)日：2017-10-17

申请号：US13699328

申请日：2011-05-23

Applicant: Jaakko Nousiainen ,  Pekka Knuuttila ,  Arto Rissanen

Inventor： Jaakko Nousiainen ,  Pekka Knuuttila ,  Arto Rissanen

IPC: C10L1/02 ,  B01J8/00 ,  C10G45/60 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08 ,  C10G3/00

CPC classification number: C10G45/60 ,  C10G3/46 ,  C10G3/48 ,  C10G3/49 ,  C10G3/50 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1022 ,  C10G2300/202 ,  C10G2300/4018 ,  C10G2300/4081 ,  C10G2300/802 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08 ,  Y02E50/13 ,  Y02P30/20 ,  Y02T50/678

Abstract: The present invention relates to a process for producing mixture of fuel components, which process comprises providing a feed of biological origin; subjecting said feed of biological origin and a hydrogen gas feed to a single step of hydroprocessing in the presence of a catalyst system comprising dewaxing catalyst to form a mixture of fuel components. The present invention relates also to an apparatus for producing a mixture of fuel components from a feed of biological origin. The invention relates also to the use of the fuel components.

公开(公告)号：US09783751B2

公开(公告)日：2017-10-10

申请号：US14389817

申请日：2013-04-05

Applicant: IGTL TECHNOLOGY LTD

Inventor： Richard John Hyman

IPC: C10G2/00 ,  C10L1/04 ,  C10G35/04 ,  C10G45/58 ,  C10L1/06 ,  C10L1/08

CPC classification number: C10L1/04 ,  C10G2/332 ,  C10G2/343 ,  C10G35/04 ,  C10G45/58 ,  C10G2300/4081 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/20 ,  C10L1/06 ,  C10L1/08 ,  C10L2200/0438 ,  C10L2200/0446 ,  C10L2200/0492 ,  C10L2270/023 ,  C10L2270/026

Abstract: The invention relates to a process for the conversion of hydrogen and one or more oxides of carbon to hydrocarbons, which process comprises: contacting hydrogen and one or more oxides of carbon with a catalyst in a reaction zone; removing from the reaction zone an outlet stream comprising unreacted hydrogen, unreacted one or more oxides of carbon and one or more hydrocarbons and feeding the outlet stream to a separation zone in which the outlet stream is divided into at least three fractions, in which; a first fraction predominantly comprises unreacted hydrogen, unreacted one or more oxides of carbon and hydrocarbons having from 1 to 4 carbon atoms; a second fraction predominantly comprises hydrocarbons having 5 to 9 carbon atoms, at least a portion of which hydrocarbons having from 5 to 9 carbon atoms are olefinic; and a third fraction predominantly comprises hydrocarbons having 10 or more carbon atoms; characterized in that at least a portion of the second fraction is recycled to the reaction zone.

公开(公告)号：US09783474B2

公开(公告)日：2017-10-10

申请号：US15032218

申请日：2014-10-27

Applicant: PURDUE RESEARCH FOUNDATION

Inventor： William Nicholas Delgass ,  Rakesh Agrawal ,  Fabio Henrique Ribeiro ,  Basudeb Saha ,  Sara Lynn Yohe ,  Mahdi M Abu-Omar ,  Trenton Parsell ,  Paul James Dietrich ,  Ian Michael Klein

IPC: C07C41/18 ,  C10L1/02 ,  B01J23/60 ,  D21C9/00 ,  C08H7/00 ,  C08H8/00 ,  D21C3/22 ,  C07C41/01 ,  C07G1/00 ,  C07D307/48 ,  C07D307/50 ,  B01J21/18 ,  B01J23/652 ,  C07C1/22 ,  C07D307/46 ,  C10L1/04

CPC classification number: C07C41/18 ,  B01J21/18 ,  B01J21/185 ,  B01J23/60 ,  B01J23/6525 ,  C07C1/22 ,  C07C41/01 ,  C07C2521/18 ,  C07C2523/60 ,  C07C2523/64 ,  C07D307/46 ,  C07D307/48 ,  C07D307/50 ,  C07G1/00 ,  C08H6/00 ,  C08H8/00 ,  C10L1/02 ,  C10L1/04 ,  C10L2200/0469 ,  D21C3/222 ,  D21C9/00 ,  C07C43/23

Abstract: Described herein are processes for one-step delignification and hydrodeoxygenation of lignin fraction a biomass feedstock. The lignin feedstock is derived from by-products of paper production and biorefineries. Additionally described is a process for converting biomass-derived oxygenates to lower oxygen-content compounds and/or hydrocarbons in the liquid or vapor phase in a reactor system containing hydrogen and a catalyst comprised of a hydrogenation function and/or an oxophilic function and/or an acid function. Finally, also described herein is a process for converting biomass-derived oxygenates to lower oxygen-content compounds and/or hydrocarbons in the liquid or vapor phase in a reactor system containing hydrogen and a catalyst comprised of a hydrogenation function and/or an oxophilic function and/or an acid function.

公开(公告)号：US20170283341A1

公开(公告)日：2017-10-05

申请号：US15621663

申请日：2017-06-13

Applicant: DYNO NOBEL INC.

Inventor： Jordan Arthur ,  Scott Hunsaker ,  Verlene Lovell ,  Lee F. McKenzie

IPC: C06B31/28

CPC classification number: C06B31/28 ,  C06B31/08 ,  C06B47/145 ,  C10L1/04 ,  C10L1/328

Abstract: Explosive compositions are disclosed herein. The compositions include a diesel fuel and a vacuum gas oil. Some compositions disclosed herein include an emulsion that includes an oxidizer in a discontinuous phase and a blend of diesel fuel and vacuum gas oil in a continuous phase. Methods of manufacturing explosive compositions are also disclosed herein.

公开(公告)号：US09771531B2

公开(公告)日：2017-09-26

申请号：US14952060

申请日：2015-11-25

Applicant: Sundrop Fuels, Inc.

Inventor： Renus C. Kelfkens ,  Wayne W. Simmons ,  Douglas S. Jack ,  Jerrod Wayne Hohman ,  Sidney P. White

IPC: C10G3/00 ,  C10G2/00 ,  C10J3/46 ,  C10G45/44 ,  C10K1/08 ,  C10K1/32 ,  C10K3/02 ,  C10G45/00 ,  C10L1/04 ,  C10K3/00 ,  C10J3/84 ,  C10J3/50 ,  C01B3/38 ,  C10J3/48

CPC classification number: C10J3/466 ,  C01B3/38 ,  C01B2203/0233 ,  C01B2203/062 ,  C01B2203/1241 ,  C10G2/32 ,  C10G2/34 ,  C10G3/00 ,  C10G45/00 ,  C10G45/44 ,  C10G2300/1011 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10J3/485 ,  C10J3/506 ,  C10J3/84 ,  C10J2300/0916 ,  C10J2300/0976 ,  C10J2300/1659 ,  C10J2300/1807 ,  C10J2300/1853 ,  C10K1/08 ,  C10K1/32 ,  C10K3/008 ,  C10K3/023 ,  C10L1/04 ,  C10L2200/0492 ,  C10L2270/023 ,  C10L2270/026 ,  C10L2270/04 ,  C10L2290/04 ,  C10L2290/06 ,  C10L2290/10 ,  C10L2290/42 ,  C10L2290/541 ,  C10L2290/542 ,  C10L2290/543 ,  C10L2290/548 ,  Y02E50/32 ,  Y02P20/145 ,  Y02P20/582 ,  Y02P30/20

Abstract: An integrated plant to generate chemical grade syngas from a steam biomass reforming in a multiple stage bio reforming reactor for use with either a high temperature or low temperature Fischer-Tropsch synthesis process to produce fuel from biomass is discussed. The first stage has a reactor to cause a chemical devolatilization of a biomass feedstock from the biomass feedstock supply lines into its constituent gases of CO, H2, CO2, CH4, tars, chars, and other components into a raw syngas mixture. A second stage performs further reforming of the raw syngas from the first stage into the chemical grade syngas by further applying heat and pressure to chemically crack at least the tars, reform the CH4, or a combination of both, into their corresponding syngas molecules. The second stage feeds the chemical grade syngas derived from the biomass feedstock to the downstream Fischer-Tropsch train to produce the fuel from the biomass. One or more recycle loops supply tail gas or FT product back into the plant.

公开(公告)号：US09764997B1

公开(公告)日：2017-09-19

申请号：US15099214

申请日：2016-04-14

Applicant: The United States of America as represented by the Secretary of the Navy

Inventor： Benjamin G Harvey

IPC: C07C5/03 ,  C07C2/42 ,  C07C5/327 ,  C10L1/04 ,  C07C2/40 ,  C07C1/24 ,  C07C1/30 ,  C07C1/04

CPC classification number: C07C5/03 ,  C07C1/0485 ,  C07C1/24 ,  C07C1/30 ,  C07C2/403 ,  C07C2/42 ,  C07C2/46 ,  C07C5/327 ,  C07C5/42 ,  C07C2523/755 ,  C07C2601/18 ,  C07C2603/90 ,  C10G2/32 ,  C10G3/00 ,  C10G9/00 ,  C10G45/00 ,  C10G50/00 ,  C10G57/02 ,  C10G69/126 ,  C10G2300/308 ,  C10G2400/08 ,  C10L1/04 ,  C10L2270/04 ,  C10L2290/24 ,  C10L2290/42 ,  Y02P30/20 ,  C07C13/263 ,  C07C13/64

Abstract: A method for making hydrogenated cyclooctatetraene dimers including cyclo-dimerizing butadiene to form 1,5-cyclooctadiene in the presence of at least one first catalyst, dehydrogenating 1,5-cyclooctadiene to 1,3,5,7-cyclooctatetraene, dimerizing 1,3,5,7-cyclooctatetraene to a C16 multicyclic hydrocarbon cyclooctatetraene dimer, and hydrogenating multicyclic hydrocarbon cyclooctatetraene dimer to form hydrogenated cyclooctatetraene dimers.

公开(公告)号：US09732282B2

公开(公告)日：2017-08-15

申请号：US15269736

申请日：2016-09-19

Applicant: Elevance Renewable Sciences, Inc.

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

IPC: C07C1/00 ,  C07C6/00 ,  C07C5/22 ,  C10G3/00 ,  C10G45/00 ,  C10G45/58 ,  C10G50/00 ,  C10G65/04 ,  C11B3/00 ,  C10L1/02 ,  C10L1/08 ,  C11C3/00 ,  C07C67/03 ,  C07C67/54 ,  C07C6/04 ,  C07C51/09 ,  C07C2/86 ,  C11C1/08 ,  C10G69/02 ,  C10L1/04

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.

公开(公告)号：US20170226028A1

公开(公告)日：2017-08-10

申请号：US15519419

申请日：2015-10-14

Applicant: Gevo, Inc.

Inventor： Jonathan O. SMITH ,  Nicholas MCGUIRE ,  Leo E. MANZER ,  Madeline SJODIN ,  Paul STARKEY ,  Caroline SALAZAR

IPC: C07C1/24 ,  C07C2/52 ,  C08F236/08 ,  C10L1/04 ,  C07C45/00 ,  C07C67/03 ,  C07C51/16 ,  C07C2/06 ,  C07C45/51

CPC classification number: C07C1/24 ,  B01J23/02 ,  B01J23/06 ,  B01J23/10 ,  B01J37/0018 ,  B01J37/03 ,  B01J37/082 ,  C07C1/20 ,  C07C2/06 ,  C07C2/52 ,  C07C45/00 ,  C07C45/512 ,  C07C51/16 ,  C07C67/03 ,  C07C2521/02 ,  C07C2521/04 ,  C07C2521/06 ,  C07C2523/06 ,  C07C2523/34 ,  C08F236/08 ,  C10L1/04 ,  C10L2200/04 ,  C10L2270/04 ,  Y02P20/132 ,  Y02P20/52 ,  C07C11/09 ,  C07C11/06 ,  C07C49/08

Abstract: This application relates to the production of functionalized lower hydrocarbons and more particularly to the process of converting ethanol to functionalized lower hydrocarbons. In particular embodiments, the ethanol to functionalized lower hydrocarbon conversion is catalyzed by a ZnxZryAvQsMnwOz mixed oxide catalyst or a bifunctional heterogeneous catalyst. In particular embodiments, the ethanol to be converted is present at molar concentrations in the reactor feed equal to or exceeding 14%.

公开(公告)号：US20170191007A1

公开(公告)日：2017-07-06

申请号：US15313650

申请日：2015-05-26

Applicant: SHELL OIL COMPANY

Inventor： Johannes Bernardus Wilhelmus MORSINK ,  Johannes TURFBOER ,  Rendert Jan WIERSMA ,  Ferry WINTER

IPC: C11D7/24 ,  C10G47/00 ,  C11D11/00 ,  C10G2/00

CPC classification number: C11D7/24 ,  C10G2/332 ,  C10G47/00 ,  C10G2300/1022 ,  C10G2300/301 ,  C10G2300/302 ,  C10L1/04 ,  C11D3/43 ,  C11D7/5027 ,  C11D11/0017 ,  C11D11/0029 ,  C23G5/024 ,  D06L1/02

Abstract: The present invention provides a Fischer-Tropsch gasoil fraction having an initial boiling point of at least 165° C. and a final boiling point of at most 220° C. In another aspect the present invention provides a cleaning composition and the use of a Fischer-Tropsch gasoil fraction according to the invention.

公开(公告)号：US20170158503A1

公开(公告)日：2017-06-08

申请号：US15327345

申请日：2015-07-22

Applicant: Iogen Corporation

Inventor： Patrick J. Foody ,  Brian Foody

IPC: C01B3/48 ,  C10G2/00 ,  C12P7/10 ,  C10L3/08 ,  C10L1/02 ,  C01B3/50 ,  C10L1/04

CPC classification number: C12P7/14 ,  C01B3/38 ,  C01B3/48 ,  C01B3/50 ,  C01B32/50 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/025 ,  C01B2203/0283 ,  C01B2203/0405 ,  C01B2203/043 ,  C01B2203/0475 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/0872 ,  C01B2203/1241 ,  C01B2203/148 ,  C07C29/1518 ,  C10G2/50 ,  C10G2400/02 ,  C10L1/02 ,  C10L1/023 ,  C10L1/04 ,  C10L1/06 ,  C10L3/00 ,  C10L3/08 ,  C10L2290/10 ,  C10L2290/26 ,  C10L2290/42 ,  C10L2290/542 ,  C10L2290/543 ,  C10L2290/545 ,  C12F3/10 ,  C12P5/023 ,  C12P7/06 ,  C12P7/065 ,  C12P7/10 ,  C12P7/54 ,  Y02E50/16 ,  Y02E50/17 ,  Y02E50/343 ,  Y02P20/128 ,  Y02P20/145 ,  Y02P30/10 ,  C07C31/04 ,  C07C31/08

Abstract: The present disclosure provides a process for forming a biogenic carbon-based fuel or a fuel intermediate from biogenic carbon dioxide and hydrogen. The hydrogen is sourced from a process that produces hydrogen and fossil carbon dioxide from a fossil-fuel hydrocarbon and separates the fossil carbon dioxide from the hydrogen. The process may further comprise carrying out or arranging for one or more parties to carry out at least one step that contributes to a reduction in the GHG emissions of the biogenic carbon-based fuel, or a fuel made from the fuel intermediate, of at least 20% relative to a gasoline baseline. In various embodiments this includes (a) introducing the fossil carbon dioxide underground, and/or (b) using a biogenic carbon-based product selected from a chemical and energy product produced from the non-fossil organic material to displace the use or production of a corresponding fossil-based product.