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公开(公告)号:US11781162B2
公开(公告)日:2023-10-10
申请号:US17071821
申请日:2020-10-15
申请人: Genifuel Corporation
发明人: James R. Oyler
IPC分类号: C12P7/64 , C10L1/02 , C10L1/08 , C10G45/00 , C12M1/00 , C12P7/62 , C10G3/00 , C11B1/02 , C11B3/00 , C12P7/06 , C11C3/04 , C12P7/649 , C12P7/6409
CPC分类号: C12P7/649 , C10G3/00 , C10G3/50 , C10G45/00 , C10L1/02 , C10L1/026 , C10L1/08 , C11B1/025 , C11B3/003 , C11C3/04 , C12M21/02 , C12M21/12 , C12M23/58 , C12M43/02 , C12M47/06 , C12P7/065 , C12P7/62 , C12P7/64 , C12P7/6409 , C10G2300/1014 , C10L2200/0476 , C10L2270/026 , C10L2290/26 , C10L2290/544 , Y02E50/10 , Y02P20/10 , Y02P30/20
摘要: A process for production of biofuels from algae can include cultivating an oil-producing algae by promoting sequential photoautotrophic and heterotrophic growth. The method can further include producing oil by heterotrophic growth of algae wherein the heterotrophic algae growth is achieved by introducing a sugar feed to the oil-producing algae. An algal oil can be extracted from the oil-producing algae, and can be converted to form biodiesel.
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公开(公告)号:US20180320208A1
公开(公告)日:2018-11-08
申请号:US15740969
申请日:2016-07-04
发明人: Yuji Okita , Makoto Ito , Rie Hamaguchi , Hatsumi Goda , Seiya Mochinaga , Daisuke Honda
CPC分类号: C12P7/6427 , C10G3/00 , C12N15/09 , C12N15/52 , C12N15/79 , C12P1/00 , C12P7/64 , C12P7/6472 , C12P19/34 , C12R1/00 , C12R1/89
摘要: A Labyrinthulid microorganism capable of producing a PUFA only through the elongase-desaturase pathway. A Labyrinthulid microorganism which has no ability of producing a PUFA through the endogenous PUFA-PKS pathway or has the ability at an extremely weak level and which has an ability of producing a PUFA through the endogenous elongase-desaturase pathway. The Labyrinthulid microorganism is a microorganism belonging to the genus Parietichytrium or Parietichytrium.
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公开(公告)号:US20180251411A1
公开(公告)日:2018-09-06
申请号:US15972530
申请日:2018-05-07
发明人: Jeffrey John SCHEIBEL , Scott Leroy CRON , Stephen Anthony DEROSE , Ryan Michael WEST , Phillip Kyle VINSON , Thomas Earl WILLIAMS , Kevin Lee GARBER , Praveen Kumar DEPA
IPC分类号: C07C2/64 , C10G3/00 , C07C5/333 , C10G29/20 , C10G35/00 , C07C29/16 , C11D1/14 , C11D1/22 , C11D1/37 , C07C303/24 , C07C303/14 , C11D3/34 , C07C5/327 , C07C11/02 , C07C15/107 , C07C309/62 , C07C305/04 , C07C33/20
CPC分类号: C07C2/64 , C07C5/327 , C07C5/333 , C07C29/16 , C07C303/14 , C07C303/24 , C07C309/62 , C10G3/00 , C10G3/42 , C10G3/50 , C10G29/205 , C10G35/00 , C10G2300/1011 , C10G2300/1014 , C10G2300/1051 , C10G2400/30 , C11D1/146 , C11D1/22 , C11D1/37 , C11D3/34 , Y02P30/20 , C07C11/02 , C07C15/107 , C07C305/04 , C07C33/20
摘要: The present invention relates generally to methods for producing renewable detergent compounds. More specifically, the invention relates to methods for producing detergent intermediates, including bio-linear alkylbenzene (LAB), bio-alcohols, and long chain bio-paraffins, from natural oils.
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公开(公告)号:US20180161749A1
公开(公告)日:2018-06-14
申请号:US15879749
申请日:2018-01-25
申请人: XYLECO, INC.
发明人: Marshall MEDOFF
IPC分类号: B01J19/08 , H01M8/1007 , C12P19/02 , C12P5/02 , C08B1/00 , C10G3/00 , C10G11/00 , C10G15/10 , C10G47/00 , C12P7/02 , C10L1/02 , C10L1/04 , C12P7/04 , C12P7/10 , C12P7/14 , C12P7/16 , C12P5/00 , H01M8/1011 , H01M8/22 , H01M8/16 , C12P19/14
CPC分类号: B01J19/08 , B01J19/081 , B01J19/085 , B01J2219/08 , B01J2219/0879 , C08B1/00 , C10G3/00 , C10G11/00 , C10G15/10 , C10G47/00 , C10G2300/1011 , C10L1/02 , C10L1/04 , C10L2200/0469 , C10L2270/02 , C10L2270/04 , C10L2290/02 , C10L2290/06 , C10L2290/26 , C10L2290/34 , C10L2290/36 , C10L2290/543 , C12P5/00 , C12P5/02 , C12P5/023 , C12P7/02 , C12P7/04 , C12P7/10 , C12P7/14 , C12P7/16 , C12P19/02 , C12P19/14 , C12P2201/00 , C12P2203/00 , H01M8/1007 , H01M8/1013 , H01M8/16 , H01M8/22 , Y02E50/16 , Y02E50/343 , Y02P30/20 , Y02T50/678
摘要: Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful products, such as fuels. For example, systems can use feedstock materials, such as cellulosic and/or lignocellulosic materials and/or starchy materials, to produce ethanol and/or butanol, e.g., by fermentation.
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公开(公告)号:US20180086678A1
公开(公告)日:2018-03-29
申请号:US15684709
申请日:2017-08-23
IPC分类号: C07C1/32 , B01J29/40 , C07C4/06 , C07C2/06 , C07C1/22 , C07C7/04 , B01J29/85 , C01B39/02 , C07C1/20 , C07C1/26 , C10G3/00 , C07C11/02 , C07C11/06
CPC分类号: C07C1/322 , B01J29/40 , B01J29/85 , B01J2229/36 , B01J2229/37 , C01B39/026 , C07C1/20 , C07C1/22 , C07C1/26 , C07C2/06 , C07C4/06 , C07C7/04 , C07C2529/85 , C10G3/00 , C10G2300/202 , C10G2300/4081 , C10G2400/20 , Y02P20/52 , Y02P30/20 , Y02P30/42 , C07C11/02 , C07C11/06
摘要: The present invention is a phosphorous modified zeolite (A) made by a process comprising in that order: selecting a zeolite with low Si/Al ratio (advantageously lower than 30) among H+ or NH4+-form of MFI, MEL, FER, MOR, clinoptilolite, said zeolite having been made preferably without direct addition of organic template; steaming at a temperature ranging from 400 to 870° C. for 0.01-200h; leaching with an aqueous acid solution containing the source of P at conditions effective to remove a substantial part of Al from the zeolite and to introduce at least 0.3 wt % of P; separation of the solid from the liquid; an optional washing step or an optional drying step or an optional drying step followed by a washing step; a calcination step. The present invention also relates to a process (hereunder referred as “XTO process”) for making an olefin product from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock wherein said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock is contacted with the above catalyst (in the XTO reactor) under conditions effective to convert at least a portion of the oxygen-containing, halogenide-containing or sulphur-containing organic feedstock to olefin products (the XTO reactor effluent).The present invention also relates to a process (hereunder referred as “combined XTO and OCP process”) to make light olefins from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock comprising: contacting said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock in the XTO reactor with the above catalyst at conditions effective to convert at least a portion of the feedstock to form an XTO reactor effluent comprising light olefins and a heavy hydrocarbon fraction; separating said light olefins from said heavy hydrocarbon fraction; contacting said heavy hydrocarbon fraction in the OCP reactor at conditions effective to convert at least a portion of said heavy hydrocarbon fraction to light olefins.
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公开(公告)号:US09909072B2
公开(公告)日:2018-03-06
申请号:US14796335
申请日:2015-07-10
发明人: Chidambaram Mandan , Kshudiram Mantri , Supriya Apegaonkar , Ramesh Bhujade , Nagesh Sharma , Raksh Vir Jasra
IPC分类号: B01J27/24 , C10G3/00 , C10G1/00 , B01J37/03 , B01J21/04 , B01J21/06 , B01J23/46 , B01J23/882 , B01J23/883 , B01J27/16 , B01J29/04 , B01J37/02 , C10L9/08 , C10L1/32
CPC分类号: C10G3/00 , B01J21/04 , B01J21/066 , B01J23/464 , B01J23/882 , B01J23/883 , B01J27/16 , B01J29/041 , B01J29/045 , B01J37/0203 , B01J37/036 , C10G1/00 , C10G3/46 , C10G3/49 , C10G3/50 , C10L1/326 , C10L9/086 , Y02P30/20
摘要: The present disclosure relates to a process for the production of bio-oil which involves heating a mixture of a biomass slurry and a first catalyst composition at a temperature ranging from 200 to 350° C. and at a pressure ranging from 70 to 250 bars to obtain a mass containing crude bio oil, a residue and the catalyst; separating the crude bio oil from said mass to obtain a separated crude bio oil; extracting said separated crude bio oil with at least one solvent and evaporating said solvent to obtain a solvent free crude bio oil; subjecting said solvent free crude bio oil to reduction in the presence of a second catalyst composition and hydrogen source at temperature and pressure conditions similar to those employed for the conversion of bio mass into crude bio oil to obtain bio-oil. The second catalyst composition is the same as that of the first catalyst composition. The process also comprises a method step of recovering the first catalyst and reusing it either for preparing crude bio oil or bio oil or both.
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公开(公告)号:US09862655B2
公开(公告)日:2018-01-09
申请号:US14319017
申请日:2014-06-30
申请人: UOP LLC
IPC分类号: C07C5/03 , C07C2/04 , C07C2/06 , C07C2/08 , C07C2/12 , C10L1/16 , B01D3/00 , C10L1/04 , C07C1/24 , C10G50/00 , C10G69/12 , C10G3/00
CPC分类号: C07C5/03 , B01D3/009 , C07C1/24 , C07C2/12 , C07C2529/70 , C10G3/00 , C10G50/00 , C10G69/126 , C10G2400/08 , C10L1/04 , Y02P20/127 , C07C11/08 , C07C11/02 , C07C9/14
摘要: Methods and systems for producing jet-range hydrocarbons are disclosed herein. In an exemplary embodiment, a method for producing jet-range hydrocarbons includes the steps of combining a first stream including C4 olefinic hydrocarbons and a second stream including C5-C8 olefinic hydrocarbons to produce a third stream including C4-C8 hydrocarbons, oligomerizing the third stream including C4-C8 olefinic hydrocarbons to produce a fourth stream including C4-C20 olefinic hydrocarbons, and separating C5-C8 hydrocarbons from the fourth stream including C4-C20 olefinic hydrocarbons to produce the second stream including C5-C8 olefinic hydrocarbons and a fifth stream including C9-C20 olefinic hydrocarbons. The method further includes the step of hydrogenating the fifth stream including C9-C20 olefinic hydrocarbons to produce a sixth stream including C9-C20 paraffinic jet-range hydrocarbons.
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公开(公告)号:US20170362521A1
公开(公告)日:2017-12-21
申请号:US15693655
申请日:2017-09-01
发明人: Michael Scott
IPC分类号: C10L1/02 , C07C67/03 , C07C67/08 , C07C67/58 , C10G3/00 , C11B3/04 , C11B3/12 , C11B3/16 , C11C3/00 , C11C3/10 , C11B3/00 , C10G33/00 , B01D21/26 , B03D1/14
CPC分类号: C10L1/026 , B01D21/262 , B03D1/1431 , C07C67/03 , C07C67/08 , C07C67/58 , C10G3/00 , C10G3/40 , C10G33/00 , C10G2300/1003 , C10G2300/201 , C10G2400/04 , C10L2200/0446 , C10L2200/0476 , C10L2270/026 , C10L2270/04 , C10L2290/06 , C10L2290/18 , C10L2290/542 , C10L2290/543 , C10L2290/544 , C10L2290/547 , C11B3/001 , C11B3/006 , C11B3/008 , C11B3/04 , C11B3/12 , C11B3/16 , C11C3/003 , C11C3/10 , Y02E50/13 , Y02P30/20 , C07C69/24 , C07C69/52
摘要: There is described a process for producing biodiesel and related products from mixtures. There is also described a process for producing precursors and feedstock materials for producing biodiesel and related products. The processes use esterification and trans-esterification, separation and purification. Other process steps such as acidification and distillation can also be used.
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公开(公告)号:US09777234B1
公开(公告)日:2017-10-03
申请号:US15371301
申请日:2016-12-07
CPC分类号: C10L1/08 , C06B47/00 , C07C1/22 , C07C1/24 , C07C5/03 , C07C5/13 , C07C5/29 , C07C5/31 , C07C7/04 , C07C45/455 , C07C2103/74 , C07C2521/18 , C07C2523/42 , C07C2523/44 , C07C2527/126 , C07C2602/26 , C07C2602/28 , C07C2602/36 , C07C2603/08 , C07C2603/74 , C07C2603/78 , C07C2603/94 , C10G3/00 , C10L1/04 , C10L1/1608 , C10L10/12 , C10L2200/0469 , C10L2270/026 , C10L2270/04 , C10L2290/543 , C07C13/32 , C07C13/50 , C07C13/72 , C07C13/605 , C07C13/615 , C07C13/547 , C07C13/48 , C07C49/323
摘要: A method for converting cedarwood oil into high density fuels including, hydrogenating cedarwood oil in the presence of at least one hydrogenation catalyst to generate hydrogenated cedarwood oil, removing the hydrogenation catalyst from the hydrogenated cedarwood oil, purifying the hydrogenated cedarwood oil to produce a first high density fuel, isomerizing the first high density fuel in the presence of at least one acid catalyst catalyst to generate a hydrocarbon mixture including adamantanes, and distilling the adamantane mixture to produce a second alkyl-adamantane high density fuel.
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公开(公告)号:US20170218288A1
公开(公告)日:2017-08-03
申请号:US15514970
申请日:2015-10-01
发明人: Ville Vauhkonen , Jaakko Nousiainen
CPC分类号: C10L1/02 , C10G3/00 , C10G3/42 , C10G3/50 , C10G2300/1014 , C10G2300/301 , C10G2300/305 , C10L1/023 , Y02P30/20
摘要: The present invention relates to a gasoline composition comprising a) 70-86% by volume of ethanol, b) a hydrocarbon component comprising hydrocarbons derived from feedstock comprising tall oil material, where said hydrocarbon component has RON of 50-70 and it comprises 25-60 mass % of naphthenes.
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