公开(公告)号：US20160348086A1

公开(公告)日：2016-12-01

申请号：US15115670

申请日：2015-01-30

Applicant: EASEL BIOTECHNOLOGIES, LLC

Inventor： Yi-Xin Huo ,  Benjamin Schilling ,  Shahrooz Rabizadeh

IPC: C12N9/88 ,  C12P5/02 ,  C12N15/74 ,  C12N9/12 ,  C10L1/00 ,  C12P7/16

CPC classification number: C12N9/88 ,  C10L1/00 ,  C10L2200/0469 ,  C10L2290/26 ,  C12N9/1205 ,  C12N15/74 ,  C12P5/026 ,  C12P7/16 ,  C12P7/625 ,  C12Y207/01019 ,  C12Y401/02009 ,  Y02E50/10

Abstract: Genetically engineered cells and methods are presented that allow for the production of various value products from CO2. Contemplated cells have a CBB cycle that is genetically modified such that two molecules of CO2 fixed in the CBB cycle can be withdrawn from the modified CBB cycle as a single C2 compound. In contemplated aspects a CBB cycle includes an enzymatic activity that generates the single C2 compound from a compound of the CBB cycle, while further modifications to the CBB cycle will not introduce additional recombinant enzymatic activity/activities outside the already existing catalytic activities in the CBB cycle.

Abstract translation: 提出了基因工程细胞和方法，允许从二氧化碳生产各种价值产品。 考虑的细胞具有遗传修饰的CBB循环，使得在CBB循环中固定的两个分子的CO 2可以作为单一的C2化合物从经修饰的CBB循环中排出。 在预期的方面，CBB循环包括从CBB循环的化合物产生单一C2化合物的酶活性，而对CBB循环的进一步修饰将不会在CBB循环中已经存在的催化活性之外引入另外的重组酶活性/活性 。

公开(公告)号：US20160340599A1

公开(公告)日：2016-11-24

申请号：US15230389

申请日：2016-08-06

Applicant: Gui-zhong SONG

Inventor： Gui-zhong SONG

IPC: C10L1/18 ,  C10L1/22 ,  C10L1/30 ,  C10L1/16

CPC classification number: C10L1/18 ,  C10L1/00 ,  C10L1/10 ,  C10L1/16 ,  C10L1/1608 ,  C10L1/1802 ,  C10L1/1824 ,  C10L1/1852 ,  C10L1/1857 ,  C10L1/1905 ,  C10L1/22 ,  C10L1/232 ,  C10L1/2641 ,  C10L1/30 ,  C10L1/305 ,  C10L2200/024 ,  C10L2200/0469 ,  C10L2200/0484 ,  C10L2230/08 ,  C10L2230/10 ,  C10L2290/141 ,  C10L2290/24

Abstract: The industrial fuel comprises the following constituents by weight percent: 65%-70% of methanol, 10%-15% of sugar pressing waste liquid, 5%-8% of rosin water, 1%-3% of oxydol with 27.5% mass concentration, 1.5%-3% of xylene, 1%-3% of phytate, 1.5%-2% of benzotriazole, 3%-5% of acetone, 0.01%-0.05% of ferrocene, 0.1%-0.5% of lavender oil, and 1.5%-2% of rubber swelling inhibitor.

Abstract translation: 工业燃料包括以下重量百分比的组分：65％-70％的甲醇，10％-15％的糖压废液，5％-8％的松香水，1％-3％的氧化酚，27.5％的质量 浓度，1.5％-3％二甲苯，1％-3％植酸盐，1.5％-2％苯并三唑，3％-5％丙酮，0.01％-0.05％二茂铁，0.1％-0.5％薰衣草油 ，和1.5％-2％的橡胶膨胀抑制剂。

公开(公告)号：US20160046884A1

公开(公告)日：2016-02-18

申请号：US14879560

申请日：2015-10-09

Applicant: TOTAL RAFFINAGE MARKETING

Inventor： Nelly Dolmazon ,  Géraldine PAPIN ,  Frédéric TORT

IPC: C10L10/14 ,  C08G8/28 ,  C10L1/22

CPC classification number: C10L10/14 ,  C08G8/12 ,  C08G8/28 ,  C10L1/00 ,  C10L1/02 ,  C10L1/026 ,  C10L1/18 ,  C10L1/22 ,  C10L1/238 ,  C10L1/2387 ,  C10L2200/0259 ,  C10L2200/0476 ,  C10L2200/0484 ,  C10L2250/04

Abstract: Modified alkylphenol-aldehyde resins include one or more alkylamines, having preferably at least one primary amine type group as well as their use for improving the flow properties of motor fuels and hydrocarbon fuels, such as in particular jet fuel, gas oil, fuel oil domestic, heavy fuel oil.

Abstract translation: 改性的烷基酚醛树脂包括一种或多种烷基胺，优选至少一种伯胺类基团，以及它们用于改善机动燃料和烃类燃料的流动性的用途，特别是喷气燃料，瓦斯油，国内燃料油 ，重油。

公开(公告)号：US09051519B2

公开(公告)日：2015-06-09

申请号：US13827153

申请日：2013-03-14

Applicant: ELEVANCE RENEWABLE SCIENCES, INC.

Inventor： Linda A. Kunz ,  Tessa M. Pals ,  Steven A. Cohen ,  Melvin L. Luetkens, Jr. ,  Chander Balakrishnan ,  Robert B. Snyder

IPC: C07C1/00 ,  C07C6/02 ,  C07C5/05 ,  C10G3/00 ,  C11C3/12 ,  C10G29/20 ,  C10G45/00 ,  C10G45/58 ,  C10G50/00 ,  C10G65/04 ,  C10G69/12 ,  C11B3/00 ,  C10L1/02 ,  C10L1/08 ,  C11C3/00 ,  C11C3/10 ,  C07C6/04 ,  C07C1/213 ,  C07C5/03 ,  C07C7/13

CPC classification number: C11C3/126 ,  C07C1/213 ,  C07C5/03 ,  C07C5/05 ,  C07C6/04 ,  C07C7/13 ,  C07C2523/28 ,  C07C2523/42 ,  C07C2523/44 ,  C07C2523/46 ,  C07C2523/72 ,  C07C2523/745 ,  C07C2523/755 ,  C10G3/42 ,  C10G3/44 ,  C10G3/50 ,  C10G29/205 ,  C10G45/00 ,  C10G45/58 ,  C10G50/00 ,  C10G65/043 ,  C10G69/123 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1088 ,  C10G2300/30 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/20 ,  C10G2400/22 ,  C10L1/00 ,  C10L1/026 ,  C10L1/08 ,  C10L2200/0469 ,  C10L2200/0476 ,  C11B3/00 ,  C11C3/003 ,  C11C3/10 ,  C11C3/12 ,  C11C3/123 ,  Y02P20/582 ,  Y02P30/20 ,  C07C11/02 ,  C07C11/12 ,  C07C9/14 ,  C07C9/22 ,  C07C11/21

Abstract: Methods are provided for refining natural oil feedstocks and partially hydrogenating polyunsaturated olefins and polyunsaturated esters. 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 polyunsaturated olefins from the polyunsaturated esters in the metathesized product. In certain embodiments, the methods further comprise partially hydrogenating the polyunsaturated olefins in the presence of a hydrogenation catalyst, wherein at least a portion of the polyunsaturated olefins are converted to monounsaturated olefins. In other embodiments, the methods further comprise partially hydrogenating the polyunsaturated esters in the presence of a hydrogenation catalyst, wherein at least a portion of the polyunsaturated esters are converted to monounsaturated esters.

Abstract translation: 提供了用于澄清天然油原料和部分氢化多不饱和烯烃和多不饱和酯的方法。 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，所述方法还包括从所述多元不饱和酯中分离所述多不饱和烯烃。 在某些实施方案中，所述方法还包括在氢化催化剂存在下部分氢化多不饱和烯烃，其中至少一部分多不饱和烯烃转化为单不饱和烯烃。 在其它实施方案中，所述方法还包括在氢化催化剂存在下部分氢化多不饱和酯，其中至少一部分多不饱和酯转化为单不饱和酯。

公开(公告)号：US20150113866A1

公开(公告)日：2015-04-30

申请号：US14340860

申请日：2014-07-25

Applicant: SHELL OIL COMPANY

Inventor： Timothy Michael SHEA ,  Trevor James DAVIES ,  Michael Clifford MACKNAY ,  Hanane Belmokaddem BENNIS

IPC: C10L10/10

CPC classification number: C10L10/10 ,  C10L1/00 ,  C10L1/1824 ,  C10L1/223 ,  C10L2200/0259 ,  C10L2200/0407 ,  C10L2200/0415 ,  C10L2200/0423 ,  C10L2230/22 ,  C10L2270/023 ,  C10L2270/04

Abstract: High octane unleaded aviation fuel compositions having high aromatics content and a CHN content of at least 98 wt %, less than 2 wt % of oxygen content, an adjusted heat of combustion of at least 43.5 MJ/kg, a vapor pressure in the range of 38 to 49 kPa, freezing point is less than −58° C. is provided.

Abstract translation: 高辛烷值无铅航空燃料组合物，其芳烃含量高，CHN含量至少为98重量％，氧含量小于2重量％，调节后的燃烧热为43.5兆焦耳/公斤，蒸气压在 38至49kPa，凝固点小于-58℃。

公开(公告)号：US08979955B2

公开(公告)日：2015-03-17

申请号：US13029188

申请日：2011-02-17

Applicant: Foster A. Agblevor ,  Nii Ofei Mante

Inventor： Foster A. Agblevor ,  Nii Ofei Mante

IPC: C01B6/24 ,  C10J3/00 ,  C10B47/24 ,  C10B53/02 ,  C10C5/00 ,  C10L1/00 ,  C10G3/00 ,  B01J27/053 ,  B01J29/40

CPC classification number: C10B47/24 ,  B01J27/053 ,  B01J29/40 ,  C10B53/02 ,  C10C5/00 ,  C10G3/49 ,  C10G2300/1059 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/00 ,  Y02E50/14 ,  Y02E50/32 ,  Y02P30/20

Abstract: Methods for fractional catalytic pyrolysis which allow for conversion of biomass into a slate of desired products without the need for post-pyrolysis separation are described. The methods involve use of a fluid catalytic bed which is maintained at a suitable pyrolysis temperature. Biomass is added to the catalytic bed, preferably while entrained in a non-reactive gas such as nitrogen, causing the biomass to become pyrolyzed and forming the desired products in vapor and gas forms, allowing the desired products to be easily separated.

Abstract translation: 描述了允许将生物质转化成所需产物的石板而不需要后裂解分离的分级催化裂解方法。 该方法涉及使用保持在合适的热解温度的流化床催化床。 将生物质加入到催化床中，优选在夹带在非反应性气体例如氮气中，使生物质变成热解并形成蒸气和气体形式的所需产物，从而容易地分离所需的产物。

公开(公告)号：US20150073062A1

公开(公告)日：2015-03-12

申请号：US14273491

申请日：2014-05-08

Applicant: McAlister Technologies, LLC

Inventor： Roy Edward McAlister

IPC: C10J3/72 ,  B01J7/00 ,  C07C1/04 ,  C01B3/00 ,  C10L3/10

CPC classification number: C10J3/723 ,  B01J7/00 ,  B01J19/24 ,  C01B3/001 ,  C01B3/0015 ,  C01B2203/0283 ,  C07C1/04 ,  C10B53/02 ,  C10G2/30 ,  C10G2/32 ,  C10G2/34 ,  C10G2/50 ,  C10G3/40 ,  C10G2300/1011 ,  C10L1/00 ,  C10L3/10 ,  C12P3/00 ,  F17D1/02 ,  F17D1/04 ,  F17D1/08 ,  F17D1/12 ,  F17D3/12 ,  Y02E50/14 ,  Y02E50/32 ,  Y02E60/34 ,  Y02P20/129 ,  Y02P20/133 ,  Y02P30/20 ,  Y10T137/0318 ,  Y10T137/8593

Abstract: Techniques, systems and material are disclosed for thermochemical regeneration of biomass into renewable engineered fuel, storage of the renewable engineered fuel, respeciation of the renewable engineered fuel and transport. In one aspect, a method includes generating low density hydrogen fuel from biomass dissociation at a first location of a low elevation. The low density hydrogen fuel is self-transported in a pipeline to a second location at a higher elevation than the first location by traveling from the first location to the second location without adding energy of pressure. A high density hydrogen carrier is generated at the second location of higher elevation by reacting the low density hydrogen fuel with at least one of a carbon donor, a nitrogen donor and an oxygen donor harvested from industrial waste. The high density hydrogen carrier is delivered to a third location of a lower elevation than the second location while providing pressure or kinetic energy.

Abstract translation: 公开了用于将生物质热再生为可再生工程燃料的技术，系统和材料，可再生工程燃料的储存，可再生工程燃料的分配和运输。 一方面，一种方法包括在低仰角的第一位置从生物质解离产生低密度氢燃料。 通过从第一位置行进到第二位置，低密度氢燃料在管道中自运送到比第一位置更高的高度的第二位置，而不增加压力。 通过使低密度氢燃料与碳供体，氮供体和从工业废物中获得的氧供体中的至少一个反应，在高海拔的第二位置产生高密度氢载体。 高密度氢载体被输送到比第二位置低的第三位置，同时提供压力或动能。

公开(公告)号：US08888871B2

公开(公告)日：2014-11-18

申请号：US13339811

申请日：2011-12-29

Applicant: Maria Magdalena Ramirez Corredores ,  Vicente Sanchez Iglesias

Inventor： Maria Magdalena Ramirez Corredores ,  Vicente Sanchez Iglesias

IPC: C10L1/00 ,  C10G69/14 ,  C10G3/00 ,  C10L1/18 ,  C10G69/00 ,  C10L1/02 ,  C10G69/04 ,  C10L1/04 ,  C10G69/06 ,  C10B49/22

CPC classification number: C10L1/00 ,  C10B49/22 ,  C10B53/02 ,  C10G3/42 ,  C10G3/50 ,  C10G69/00 ,  C10G69/04 ,  C10G69/06 ,  C10G69/14 ,  C10G2300/302 ,  C10L1/02 ,  C10L1/04 ,  C10L1/1817 ,  C10L2200/0469 ,  C10L2290/543 ,  Y02E50/14 ,  Y02P30/20

Abstract: Renewable fuels are produced in commercial quantities and with enhanced efficiency by integrating a bio-oil production system with a conventional petroleum refinery so that the bio-oil is co-processed with a petroleum-derived stream in the refinery. The techniques used to integrate the bio-oil production system and conventional petroleum refineries are selected based on the quality of the bio-oil and the desired product slate from the refinery.

Abstract translation: 通过将生物油生产系统与传统的炼油厂相结合，可再生燃料以商业数量生产并提高效率，使生物油与炼油厂的石油衍生物流共同加工。 用于整合生物油生产系统和传统炼油厂的技术是根据生物油的质量和来自炼油厂的期望产品板岩来选择的。

公开(公告)号：US08658025B2

公开(公告)日：2014-02-25

申请号：US13038118

申请日：2011-03-01

Applicant: Michael Siskin ,  Glen E. Phillips ,  Simon R. Kelemen ,  Walter Weissman

Inventor： Michael Siskin ,  Glen E. Phillips ,  Simon R. Kelemen ,  Walter Weissman

IPC: C10L1/02

CPC classification number: C10B55/00 ,  C10B53/02 ,  C10B55/10 ,  C10B57/045 ,  C10B57/06 ,  C10G3/00 ,  C10G3/57 ,  C10G2300/1014 ,  C10G2300/1037 ,  C10G2300/708 ,  C10L1/00 ,  Y02E50/14 ,  Y02P20/145 ,  Y02P30/20

Abstract: Biomass is used as a co-feed for a heavy petroleum oil coking process to improve the operation of the coking process and to utilize biomaterial for the production of transportation fuels. The coking process may be a delayed coking process or a fluidized bed coking process and in each case, the presence of the biomass will decrease the coke drying time so reducing coke handling problems in the unit besides forming a superior coke product. In the case of a fluidized bed coking process using a gasifier for the coke, the addition of an alkali metal salt improves the operation of the gasifier.

Abstract translation: 生物质用作重石油炼焦过程的共同进料，以改善焦化过程的运行并利用生物材料生产运输燃料。 焦化方法可以是延迟焦化方法或流化床焦化方法，并且在每种情况下，生物质的存在将降低焦炭干燥时间，从而减少除了形成高级焦炭产物之外的单元中的焦炭处理问题。 在使用气化炉用于焦炭的流化床焦化方法的情况下，加入碱金属盐改善了气化器的操作。

公开(公告)号：US20130217906A1

公开(公告)日：2013-08-22

申请号：US13827153

申请日：2013-03-14

Applicant: ELEVANCE RENEWABLE SCIENCES, INC.

Inventor： Linda A. Kunz ,  Tessa M. Pals ,  Steven A. Cohen ,  Melvin L. Luetkens, JR. ,  Chander Balakrishnan ,  Robert B. Snyder

IPC: C10G3/00 ,  C11C3/12

CPC classification number: C11C3/126 ,  C07C1/213 ,  C07C5/03 ,  C07C5/05 ,  C07C6/04 ,  C07C7/13 ,  C07C2523/28 ,  C07C2523/42 ,  C07C2523/44 ,  C07C2523/46 ,  C07C2523/72 ,  C07C2523/745 ,  C07C2523/755 ,  C10G3/42 ,  C10G3/44 ,  C10G3/50 ,  C10G29/205 ,  C10G45/00 ,  C10G45/58 ,  C10G50/00 ,  C10G65/043 ,  C10G69/123 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1088 ,  C10G2300/30 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/20 ,  C10G2400/22 ,  C10L1/00 ,  C10L1/026 ,  C10L1/08 ,  C10L2200/0469 ,  C10L2200/0476 ,  C11B3/00 ,  C11C3/003 ,  C11C3/10 ,  C11C3/12 ,  C11C3/123 ,  Y02P20/582 ,  Y02P30/20 ,  C07C11/02 ,  C07C11/12 ,  C07C9/14 ,  C07C9/22 ,  C07C11/21

Abstract: Methods are provided for refining natural oil feedstocks and partially hydrogenating polyunsaturated olefins and polyunsaturated esters. 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 polyunsaturated olefins from the polyunsaturated esters in the metathesized product. In certain embodiments, the methods further comprise partially hydrogenating the polyunsaturated olefins in the presence of a hydrogenation catalyst, wherein at least a portion of the polyunsaturated olefins are converted to monounsaturated olefins. In other embodiments, the methods further comprise partially hydrogenating the polyunsaturated esters in the presence of a hydrogenation catalyst, wherein at least a portion of the polyunsaturated esters are converted to monounsaturated esters.

Abstract translation: 提供了用于澄清天然油原料和部分氢化多不饱和烯烃和多不饱和酯的方法。 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，所述方法还包括从所述多元不饱和酯中分离所述多不饱和烯烃。 在某些实施方案中，所述方法还包括在氢化催化剂存在下部分氢化多不饱和烯烃，其中至少一部分多不饱和烯烃转化为单不饱和烯烃。 在其它实施方案中，所述方法还包括在氢化催化剂存在下部分氢化多不饱和酯，其中至少一部分多不饱和酯转化为单不饱和酯。