RU2011112940A - Композиции жидкого топлива на основе каталитически деоксигенированных и конденсированных оксигенированных углеводов - Google Patents

Композиции жидкого топлива на основе каталитически деоксигенированных и конденсированных оксигенированных углеводов Download PDF

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RU2011112940A
RU2011112940A RU2011112940/04A RU2011112940A RU2011112940A RU 2011112940 A RU2011112940 A RU 2011112940A RU 2011112940/04 A RU2011112940/04 A RU 2011112940/04A RU 2011112940 A RU2011112940 A RU 2011112940A RU 2011112940 A RU2011112940 A RU 2011112940A
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range
boiling point
water
oxygenated hydrocarbon
hydrocarbon
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RU2542990C2 (ru
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Джоанна Маргарет БОЛДРЕЙ (GB)
Джоанна Маргарет БОЛДРЕЙ
Пол Джордж БЛОММЕЛ (US)
Пол Джордж БЛОММЕЛ
Рэнди Дуглас КОРТРАЙТ (US)
Рэнди Дуглас КОРТРАЙТ
Ричард Джон ПРАЙС (GB)
Ричард Джон ПРАЙС
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Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL)
Шелл Интернэшнл Рисерч Маатсхаппий Б.В.
Вайрент Энерджи Системз, Инк. (US)
Вайрент Энерджи Системз, Инк.
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Abstract

1. Композиция жидкого топлива, содержащая фракцию перегонки компонента, содержащего, по меньшей мере, одно С4+ соединение, произведенное из растворимого в воде оксигенированного углеводорода, и полученного по способу, включающему: ! подачу воды и растворимого в воде оксигенированного углеводорода, содержащего C1+O1+ углеводород, в водной жидкой фазе и/или паровой фазе; ! подачу Н2; ! проведение каталитической реакции в жидкой и/или паровой фазе между оксигенированным углеводородом и Н2 в присутствии катализатора деоксигенирования при температуре деоксигенирования и давлении деоксигенирования для получения оксигената, содержащего в реакционном потоке C1+O1-3 углеводород; и ! проведение каталитической реакции в жидкой и/или паровой фазе для оксигената в присутствии катализатора конденсации при температуре конденсации и давлении конденсации для получения С4+ соединения, ! где С4+ соединение включает представителя, выбираемого из группы, состоящей из С4+ спирта, С4+ кетона, С4+ алкана, С4+ алкена, С5+ циклоалкана, С5+ циклоалкена, арила, конденсированного арила и их смеси; ! где композицию жидкого топлива выбирают из: ! композиции бензина, характеризующейся температурой начала кипения в диапазоне от 15°С до 70°С (IP123), температурой конца кипения, равной, самое большее, 230°С, (IP123), значением исследовательского октанового числа (ИОЧ) в диапазоне от 85 до 110 (ASTM D2699) и значением моторного октанового числа (МОЧ) в диапазоне от 75 до 100 (ASTM D2700); ! композиции дизельного топлива, характеризующейся температурой начала кипения в диапазоне от 130°С до 230°С (IP123), температурой конца кипения, равной, самое большее, 410°С, (IP123) и цетановым числом в диапа�

Claims (10)

1. Композиция жидкого топлива, содержащая фракцию перегонки компонента, содержащего, по меньшей мере, одно С4+ соединение, произведенное из растворимого в воде оксигенированного углеводорода, и полученного по способу, включающему:
подачу воды и растворимого в воде оксигенированного углеводорода, содержащего C1+O1+ углеводород, в водной жидкой фазе и/или паровой фазе;
подачу Н2;
проведение каталитической реакции в жидкой и/или паровой фазе между оксигенированным углеводородом и Н2 в присутствии катализатора деоксигенирования при температуре деоксигенирования и давлении деоксигенирования для получения оксигената, содержащего в реакционном потоке C1+O1-3 углеводород; и
проведение каталитической реакции в жидкой и/или паровой фазе для оксигената в присутствии катализатора конденсации при температуре конденсации и давлении конденсации для получения С4+ соединения,
где С4+ соединение включает представителя, выбираемого из группы, состоящей из С4+ спирта, С4+ кетона, С4+ алкана, С4+ алкена, С5+ циклоалкана, С5+ циклоалкена, арила, конденсированного арила и их смеси;
где композицию жидкого топлива выбирают из:
композиции бензина, характеризующейся температурой начала кипения в диапазоне от 15°С до 70°С (IP123), температурой конца кипения, равной, самое большее, 230°С, (IP123), значением исследовательского октанового числа (ИОЧ) в диапазоне от 85 до 110 (ASTM D2699) и значением моторного октанового числа (МОЧ) в диапазоне от 75 до 100 (ASTM D2700);
композиции дизельного топлива, характеризующейся температурой начала кипения в диапазоне от 130°С до 230°С (IP123), температурой конца кипения, равной, самое большее, 410°С, (IP123) и цетановым числом в диапазоне от 35 до 120 (ASTM D613); и
композиции керосина, характеризующейся температурой начала кипения в диапазоне от 80 до 150°С, температурой конца кипения в диапазоне от 200 до 320°С и вязкостью при - 20°С в диапазоне от 0,8 до 10 мм2/с (ASTM D445).
2. Композиция жидкого топлива по п.1, где компонент, содержащий, по меньшей мере, одно С4+ соединение, произведенное из растворимого в воде оксигенированного углеводорода, имеет возраст, меньший, чем 100 лет, согласно вычислению по концентрации углерода-14 в компоненте.
3. Композиция жидкого топлива по п.1 или 2, где композиция жидкого топлива дополнительно содержит одну или несколько топливных присадок.
4. Композиция бензина, содержащая компонент, содержащий, по меньшей мере, одно С4+ соединение, производимое из растворимого в воде оксигенированного углеводорода, и характеризующийся температурой конца кипения в диапазоне от 150 до 220°С, плотностью при 15°С в диапазоне от 700 до 890 кг/м3, уровнем содержания серы, равным, самое большее, 5 мг/кг, уровнем содержания кислорода, равным, самое большее, 3,5 мас.%, значением ИОЧ в диапазоне от 80 до 110 и значением МОЧ в диапазоне от 70 до 100, где упомянутая композиция бензина характеризуется температурой начала кипения в диапазоне от 15°С до 70°С (IP123), температурой конца кипения, равной, самое большее, 220°С, (IP123), значением ИОЧ в диапазоне от 85 до 110 (ASTM D2699) и значением МОЧ в диапазоне от 75 до 100 (ASTM D2700).
5. Композиция дизельного топлива, содержащая компонент, содержащий, по меньшей мере, одно С4+ соединение, производимое из растворимого в воде оксигенированного углеводорода, и характеризующийся значением Т95 в диапазоне от 220 до 380°С, температурой вспышки в диапазоне от 30 до 70°С, плотностью при 15°С в диапазоне от 700 до 900 кг/м3, уровнем содержания серы, равным, самое большее, 5 мг/кг, уровнем содержания кислорода, равным, самое большее, 10 мас.%, и вязкостью при 40°С в диапазоне от 0,5 до 6 сСт, где упомянутая композиция дизельного топлива характеризуется температурой начала кипения в диапазоне от 130°С до 230°С (IP123), температурой конца кипения, равной, самое большее, 410°С, (IP123) и цетановым числом в диапазоне от 35 до 120 (ASTM D613).
6. Композиция керосина, содержащая компонент, содержащий, по меньшей мере, одно С4+ соединение, производимое из растворимого в воде оксигенированного углеводорода, и характеризующийся температурой начала кипения в диапазоне от 120 до 215°С, температурой конца кипения в диапазоне от 220 до 320°С, плотностью при 15°С в диапазоне от 700 до 890 кг/м3, уровнем содержания серы, равным, самое большее, 0,1 мас.%, уровнем содержания совокупной ароматики, равным, самое большее, 30 об.%, температурой замерзания, равной - 40°С и менее, максимальной высотой некоптящего пламени, равной, по меньшей мере, 18 мм, вязкостью при - 20°С в диапазоне от 1 до 10 сСт и удельным энергосодержанием в диапазоне от 40 до 47 МДж/кг, где упомянутая композиция керосина характеризуется температурой начала кипения в диапазоне от 80 до 150°С, температурой конца кипения в диапазоне от 200 до 320°С и вязкостью при - 20°С в диапазоне от 0,8 до 10 мм2/сек (ASTM D445).
7. Способ получения композиции жидкого топлива по п.1, включающий перемешивание:
(a) фракции перегонки компонента, содержащего, по меньшей мере, одно С4+ соединение, произведенное из растворимого в воде оксигенированного углеводорода, полученного по способу, включающему:
подачу воды и растворимого в воде оксигенированного углеводорода, содержащего С1+О1+ углеводород, в водной жидкой фазе и/или паровой фазе;
подачу Н2;
проведение каталитической реакции в жидкой и/или паровой фазе между оксигенированным углеводородом и H2 в присутствии катализатора деоксигенирования при температуре деоксигенирования и давлении деоксигенирования для получения оксигената, содержащего в реакционном потоке C1+O1-3 углеводород; и
проведение каталитической реакции в жидкой и/или паровой фазе для оксигената в присутствии катализатора конденсации при температуре конденсации и давлении конденсации для получения С4+ соединения,
где С4+ соединение включает представителя, выбираемого из группы, состоящей из С4+ спирта, С4+ кетона, С4+ алкана, С4+ алкена, С5+ циклоалкана, С5+ циклоалкена, арила, конденсированного арила и их смеси, и
(b) по меньшей мере, одного компонента топлива.
8. Способ получения композиции бензина по п.4, включающий перемешивание:
(a) компонента, содержащего, по меньшей мере, одно С4+ соединение, производимое из растворимого в воде оксигенированного углеводорода, и характеризующегося температурой конца кипения в диапазоне от 150 до 250°С, плотностью при 15°С в диапазоне от 700 до 890 кг/м3, уровнем содержания серы, равным, самое большее, 5 мг/кг, уровнем содержания кислорода, равным, самое большее, 3,5 мас.%, значением ИОЧ в диапазоне от 80 до 110 и значением МОЧ в диапазоне от 70 до 100, и
(b) по меньшей мере, одного компонента топлива.
9. Способ получения композиции дизельного топлива по п.5, включающий перемешивание:
(a) компонента, содержащего, по меньшей мере, одно С4+ соединение, производимое из растворимого в воде оксигенированного углеводорода, и характеризующегося значением Т95 в диапазоне от 220 до 380°С, температурой вспышки в диапазоне от 30 до 70°С, плотностью при 15°С в диапазоне от 700 до 900 кг/м3, уровнем содержания серы, равным, самое большее, 5 мг/кг, уровнем содержания кислорода, равным, самое большее, 10 мас.%, и вязкостью при 40°С в диапазоне от 0,5 до 6 сСт, и
(b) по меньшей мере, одного компонента топлива.
10. Способ получения композиции керосина по п.6, включающий перемешивание:
(a) компонента, содержащего, по меньшей мере, одно С4+ соединение, производимое из растворимого в воде оксигенированного углеводорода, и характеризующегося температурой начала кипения в диапазоне от 120 до 215°С, температурой конца кипения в диапазоне от 220 до 340°С, плотностью при 15°С в диапазоне от 700 до 890 кг/м3, уровнем содержания серы, равным, самое большее, 0,1% (масс.), уровнем содержания совокупной ароматики, равным, самое большее, 30 об.%, температурой замерзания, равной - 40°С и менее, максимальной высотой некоптящего пламени, равной, по меньшей мере, 18 мм, вязкостью при - 20°С в диапазоне от 1 до 10 сСт и удельным энергосодержанием в диапазоне от 40 до 47 МДж/кг, и
(b) по меньшей мере, одного компонента топлива.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2616620C2 (ru) * 2011-05-23 2017-04-18 Вайрент, Инк. Производство химических веществ и топлив из биомассы

Families Citing this family (143)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005097684A2 (en) * 2004-04-02 2005-10-20 Skill Associates, Inc. Biomass converters and processes
RU2472840C2 (ru) * 2007-03-08 2013-01-20 Вайрент, Инк. Синтез жидкого топлива и химических реактивов из кислородсодержащих углеводородов
SE531491C2 (sv) * 2007-03-29 2009-04-28 Reac Fuel Ab Bränsle framställt från biomassa
US10590571B2 (en) * 2007-12-28 2020-03-17 Albany International Corp. Ultra-resilient pad
US8697924B2 (en) * 2008-09-05 2014-04-15 Shell Oil Company Liquid fuel compositions
JP5368074B2 (ja) * 2008-12-11 2013-12-18 昭和シェル石油株式会社 ガソリンエンジン用燃料組成物
JP5368072B2 (ja) * 2008-12-11 2013-12-18 昭和シェル石油株式会社 ガソリンエンジン用燃料組成物
JP5368073B2 (ja) * 2008-12-11 2013-12-18 昭和シェル石油株式会社 ガソリンエンジン用燃料組成物の製造方法及びその製造方法に使用する自動車エンジン用燃料基材
WO2010080733A1 (en) 2009-01-09 2010-07-15 Cool Planet Biofuels, Llc System and method for atmospheric carbon sequestration
US9909067B2 (en) 2009-01-21 2018-03-06 Cool Planet Energy Systems, Inc. Staged biomass fractionator
CA2749982C (en) * 2009-01-21 2017-11-14 Cool Planet Biofuels, Inc. System and method for biomass fractioning
US9162212B2 (en) 2009-03-09 2015-10-20 Wayne State University Supported catalyst systems and method of making biodiesel products using such catalysts
KR101761728B1 (ko) 2009-09-30 2017-07-26 떼에스오뜨로와 이엔쎄. 살균 방법 및 장치
ES2362248B1 (es) * 2009-12-11 2012-05-10 Universidad Politecnica De Valencia Producción de combustibles l�?quidos (sylvan-liquid fuels) a partir de 2 -metilfurano.
US9303226B2 (en) 2009-12-31 2016-04-05 Shell Oil Company Direct aqueous phase reforming of bio-based feedstocks
US9447347B2 (en) 2009-12-31 2016-09-20 Shell Oil Company Biofuels via hydrogenolysis-condensation
WO2011143392A1 (en) 2010-05-12 2011-11-17 Shell Oil Company Process including hydrogenolysis of biomass followed by dehydrogenation and aldol condensation for producing alkanes
BR112012028663A2 (pt) 2010-05-12 2016-08-16 Shell Int Research método, e, sistema
US8366907B2 (en) * 2010-08-02 2013-02-05 Battelle Memorial Institute Deoxygenation of fatty acids for preparation of hydrocarbons
WO2014046982A1 (en) * 2012-09-24 2014-03-27 Xf Technologies Inc. Fuels and fuel additives comprising ester derivatives of 5-methyl-2-furoic acid
US9062264B2 (en) * 2010-10-29 2015-06-23 Kior, Inc. Production of renewable bio-gasoline
US9447350B2 (en) 2010-10-29 2016-09-20 Inaeris Technologies, Llc Production of renewable bio-distillate
US8377152B2 (en) * 2010-10-29 2013-02-19 Kior, Inc. Production of renewable bio-distillate
US9382489B2 (en) 2010-10-29 2016-07-05 Inaeris Technologies, Llc Renewable heating fuel oil
US9315739B2 (en) 2011-08-18 2016-04-19 Kior, Llc Process for upgrading biomass derived products
US8143464B2 (en) 2011-03-24 2012-03-27 Cool Planet Biofuels, Inc. Method for making renewable fuels
US8951476B2 (en) 2011-03-24 2015-02-10 Cool Planet Energy Systems, Inc. System for making renewable fuels
US8137628B2 (en) * 2011-03-24 2012-03-20 Cool Planet Biofuels, Inc. System for making renewable fuels
US8431757B2 (en) 2011-03-24 2013-04-30 Cool Planet Biofuels, Inc. Method for making renewable fuels
BR112013026982A2 (pt) 2011-04-21 2017-01-10 Shell Internationale Rsearch Mij B V composição de combustível líquido, processos para preparar uma composição de combustível líquido e para operar um motor, e, uso da composição de combustível líquido
US8367881B2 (en) 2011-05-09 2013-02-05 Cool Planet Biofuels, Inc. Method for biomass fractioning by enhancing biomass thermal conductivity
US8173044B1 (en) 2011-05-09 2012-05-08 Cool Planet Biofuels, Inc. Process for biomass conversion to synthesis gas
MX2013013555A (es) 2011-05-27 2014-02-27 Bp Corp North America Inc Metodo para convertir mezcla de fermentacion en combustible.
US20120304531A1 (en) 2011-05-30 2012-12-06 Shell Oil Company Liquid fuel compositions
US10696603B2 (en) 2011-06-06 2020-06-30 Carbon Technology Holdings, LLC Mineral solubilizing microorganism infused biochars
US10173937B2 (en) 2011-06-06 2019-01-08 Cool Planet Energy Systems, Inc. Biochar as a microbial carrier
US9493379B2 (en) 2011-07-25 2016-11-15 Cool Planet Energy Systems, Inc. Method for the bioactivation of biochar for use as a soil amendment
US9809502B2 (en) 2011-06-06 2017-11-07 Cool Planet Energy Systems, Inc. Enhanced Biochar
US10252951B2 (en) 2011-06-06 2019-04-09 Cool Planet Energy Systems, Inc. Biochars and biochar treatment processes
US12054440B2 (en) 2011-06-06 2024-08-06 Carbon Technology Holdings, LLC Method for application of biochar in turf grass and landscaping environments
US9980912B2 (en) 2014-10-01 2018-05-29 Cool Planet Energy Systems, Inc. Biochars for use with animals
US8568493B2 (en) 2011-07-25 2013-10-29 Cool Planet Energy Systems, Inc. Method for producing negative carbon fuel
US8317891B1 (en) 2011-06-06 2012-11-27 Cool Planet Biofuels, Inc. Method for enhancing soil growth using bio-char
US10118870B2 (en) 2011-06-06 2018-11-06 Cool Planet Energy Systems, Inc. Additive infused biochar
US10322389B2 (en) 2014-10-01 2019-06-18 Cool Planet Energy Systems, Inc. Biochar aggregate particles
US10550044B2 (en) 2011-06-06 2020-02-04 Cool Planet Energy Systems, Inc. Biochar coated seeds
US11279662B2 (en) 2011-06-06 2022-03-22 Carbon Technology Holdings, LLC Method for application of biochar in turf grass and landscaping environments
US9216916B2 (en) 2013-10-25 2015-12-22 Cool Planet Energy Systems, Inc. System and method for purifying process water produced from biomass conversion to fuels
US10640429B2 (en) 2011-06-06 2020-05-05 Cool Planet Energy System, Inc. Methods for application of biochar
US10059634B2 (en) 2011-06-06 2018-08-28 Cool Planet Energy Systems, Inc. Biochar suspended solution
US9493380B2 (en) 2011-06-06 2016-11-15 Cool Planet Energy Systems, Inc. Method for enhancing soil growth using bio-char
US11214528B2 (en) 2011-06-06 2022-01-04 Carbon Technology Holdings, LLC Treated biochar for use in water treatment systems
US10392313B2 (en) 2011-06-06 2019-08-27 Cool Planet Energy Systems, Inc. Method for application of biochar in turf grass and landscaping environments
US10233129B2 (en) 2011-06-06 2019-03-19 Cool Planet Energy Systems, Inc. Methods for application of biochar
WO2012177348A1 (en) * 2011-06-21 2012-12-27 W. R. Grace & Co.-Conn. Catalytic purification of fatty acid alkyl esters used in fuels
US20130015099A1 (en) 2011-07-14 2013-01-17 Cool Planet Biofuels, Inc. Liquid fuel composition
US9260666B2 (en) 2011-07-25 2016-02-16 Cool Planet Energy Systems, Inc. Method for reducing the carbon footprint of a conversion process
US10427069B2 (en) 2011-08-18 2019-10-01 Inaeris Technologies, Llc Process for upgrading biomass derived products using liquid-liquid extraction
WO2013034950A1 (en) 2011-09-08 2013-03-14 Société Anonyme Des Eaux Minerales D'evian Method for producing a bio-pet polymer
FI20110300A0 (fi) * 2011-09-11 2011-09-11 Neste Oil Oyj Bensiinikoostumukset ja menetelmä niiden valmistamiseksi
US20130151167A1 (en) * 2011-12-08 2013-06-13 Marathon Petroleum Company Lp Method To Determine The DRA In A Hydrocarbon Fuel
CN103998398A (zh) 2011-12-15 2014-08-20 陶氏环球技术有限责任公司 使用基于卤素的催化剂对聚醚多元醇和它们的衍生物进行脱羟基化
BR112014014206A2 (pt) 2011-12-15 2017-06-13 Dow Global Technologies Llc processo para preparar uma olefina
WO2013090074A1 (en) 2011-12-15 2013-06-20 Dow Global Technologies Llc Non-reductive dehydroxylation of vicinal compounds to olefins using a halogen-based catalyst
WO2013090071A1 (en) 2011-12-15 2013-06-20 Dow Global Technologies Llc Reductive dehydroxylation of vicinal polyols to olefins using an iodine-based catalyst having enhanced solubility
EP2791087B1 (en) 2011-12-15 2016-05-18 Dow Global Technologies LLC Iodine-based catalyst for reductive dehydroxylation of vicinal polyols to olefins
US9005380B2 (en) * 2012-03-23 2015-04-14 Johann Haltermann Limited High performance liquid rocket propellant
AU2013262762B2 (en) 2012-05-17 2015-08-20 Shell Internationale Research Maatschappij B.V. Methods and systems for processing biomass material
DE102012208417A1 (de) * 2012-05-21 2013-11-21 INGEN GTL Ltd. Verfahren zur Herstellung eines isoparaffinischen Kohlenwasserstoffgemisches
CN102757310B (zh) * 2012-07-04 2015-04-29 易高环保能源研究院有限公司 催化转化纤维素制异丙醇的方法
US9302250B2 (en) * 2012-11-15 2016-04-05 Phillips 66 Company Catalysts for renewable hydrogen production from oxygenated feedstocks
WO2014096250A1 (en) 2012-12-21 2014-06-26 Shell Internationale Research Maatschappij B.V. Liquid fuel compositions comprising organic sunscreen compounds
RU2502790C1 (ru) * 2013-01-14 2013-12-27 Игорь Николаевич Куликов Способ получения и состав присадки к жидкому топливу
WO2014133012A1 (ja) * 2013-03-01 2014-09-04 東燃ゼネラル石油株式会社 燃料油
CN105143406B (zh) * 2013-03-14 2018-01-23 维仁特公司 从二氧化合物和多氧化合物产生芳香族化合物
FI126331B (en) 2013-04-02 2016-10-14 Upm Kymmene Corp Renewable hydrocarbon composition
FI126330B (en) * 2013-04-02 2016-10-14 Upm Kymmene Corp Renewable hydrocarbon composition
EP2989073B1 (en) * 2013-04-26 2020-06-03 The Regents of the University of California Methods to produce fuels
WO2014190124A1 (en) * 2013-05-22 2014-11-27 Virent, Inc. Hydrogenation of carboxylic acids to increase yield of aromatics
US9873836B2 (en) * 2013-05-22 2018-01-23 Virent, Inc. Process for converting biomass to aromatic hydrocarbons
CN104560102B (zh) * 2013-10-29 2016-05-18 中国石油化工股份有限公司 一种提高生物油品质的方法
US8815963B1 (en) 2013-11-04 2014-08-26 Auxilium Green, LLC Catalyst composition formulated for synthesis of alcohols and method of preparing the same
CN103721702B (zh) * 2013-11-26 2015-06-10 河北隆海生物能源科技有限公司 一种生产生物柴油用的催化剂的制备方法
WO2015091458A1 (en) 2013-12-16 2015-06-25 Shell Internationale Research Maatschappij B.V. Liquid fuel compositions
US20150259619A1 (en) * 2014-03-11 2015-09-17 Swift Fuels, Llc Motor fuel formulation
CN106414377A (zh) * 2014-03-24 2017-02-15 加利福尼亚大学董事会 制备环状和非环状酮的方法
DK3143101T3 (da) 2014-05-12 2021-05-03 Katholieke Univ Leuven K U Leuven R&D Katalytisk fremgangsmåde med tofaset opløsningsmiddel til direkte fremstilling af let naphtha ud fra carbohydratholdigt råmateriale
EP2949733A1 (en) 2014-05-28 2015-12-02 Shell Internationale Research Maatschappij B.V. Gasoline compositions comprising oxanilide uv filter compounds
EP3172184A1 (en) 2014-07-25 2017-05-31 SABIC Global Technologies B.V. Synthesis of diacetone alcohol and mesityl oxide
WO2016044452A1 (en) * 2014-09-17 2016-03-24 Crc Industries, Inc. Systems for the reduction of intake valve deposits and methods
US10472297B2 (en) 2014-10-01 2019-11-12 Cool Planet Energy System, Inc. Biochars for use in composting
US10870608B1 (en) 2014-10-01 2020-12-22 Carbon Technology Holdings, LLC Biochar encased in a biodegradable material
US11426350B1 (en) 2014-10-01 2022-08-30 Carbon Technology Holdings, LLC Reducing the environmental impact of farming using biochar
US11053171B2 (en) 2014-10-01 2021-07-06 Carbon Technology Holdings, LLC Biochars for use with animals
EP3200915A4 (en) 2014-10-01 2018-06-20 Cool Planet Energy Systems, Inc. Biochars and biochar treatment processes
US11097241B2 (en) 2014-10-01 2021-08-24 Talipot Cool Extract (Ip), Llc Biochars, biochar extracts and biochar extracts having soluble signaling compounds and method for capturing material extracted from biochar
CN104368346B (zh) * 2014-10-20 2016-08-24 中科合成油淮南催化剂有限公司 用于糠醛气相加氢制备2-甲基呋喃的催化剂及其制备方法
CN107107047B (zh) 2014-10-29 2020-05-22 加利福尼亚大学董事会 用胺催化剂制备燃料、汽油添加剂和润滑剂的方法
WO2016069797A1 (en) 2014-10-29 2016-05-06 The Regents Of The University Of California Methods for producing fuels, gasoline additives, and lubricants using amine catalysts
JP6855375B2 (ja) 2014-11-12 2021-04-07 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイＳｈｅｌｌ Ｉｎｔｅｒｎａｔｉｏｎａｌｅ Ｒｅｓｅａｒｃｈ Ｍａａｔｓｃｈａｐｐｉｊ Ｂｅｓｌｏｔｅｎ Ｖｅｎｎｏｏｔｓｈａｐ 燃料組成物
US20160186081A1 (en) * 2014-12-30 2016-06-30 Chih-Jung Chao Environmental protection liquid fuel generator
JP6807850B2 (ja) 2015-02-27 2021-01-06 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイＳｈｅｌｌ Ｉｎｔｅｒｎａｔｉｏｎａｌｅ Ｒｅｓｅａｒｃｈ Ｍａａｔｓｃｈａｐｐｉｊ Ｂｅｓｌｏｔｅｎ Ｖｅｎｎｏｏｔｓｈａｐ 潤滑組成物の使用
CN104698027A (zh) * 2015-03-26 2015-06-10 广东石油化工学院 用于获得渣油高温焦化反应过程中间相物质的试验装置
WO2017209778A2 (en) 2015-08-13 2017-12-07 Virent, Inc. Production of alternative gasoline fuels
CA2995149C (en) 2015-08-13 2023-10-17 Shell Internationale Research Maatschappij B.V. Fuel formulation
CN105132003B (zh) * 2015-08-27 2017-04-12 中国科学院青岛生物能源与过程研究所 一种生物基航空燃料的制备方法
US10808195B2 (en) 2015-09-22 2020-10-20 Shell Oil Company Fuel compositions
US10596558B2 (en) * 2015-11-20 2020-03-24 Reliance Industries Limited Naphtha reforming catalyst and processes thereof
US11959033B2 (en) 2015-11-30 2024-04-16 Shell Usa, Inc. Fuel composition
US11028221B2 (en) 2015-12-11 2021-06-08 SOCIETE ANONYME DES EAUX MINERALES D'EVIAN et en abrégé “S.A.E.M.E” PET polymer with an anti-crystallization comonomer that can be bio-sourced
MX2018007383A (es) 2015-12-21 2018-08-15 Shell Int Research Metodos para proporcionar combustibles liquidos de propulsion a base de queroseno de mayor calidad.
EP3492561A4 (en) * 2016-07-26 2020-02-26 Idemitsu Kosan Co., Ltd. GASOLINE COMPOSITION AND PRODUCTION METHOD THEREFOR
EP3541906A1 (en) * 2016-11-15 2019-09-25 Exxonmobil Research And Engineering Company Fuel compositions for controlling combustion in engines
ES2850500T3 (es) * 2016-11-16 2021-08-30 Archer Daniels Midland Co Procedimiento para producir 1,2-propanodiol a partir de glicerol
RU2678457C2 (ru) * 2017-01-18 2019-01-29 Общество с ограниченной ответственностью "НаноТехЦентр" Применение композиции, включающей минеральное моторное масло или индустриальное масло, суспензию наноматериала (УНМ) и поверхностно-активное вещество (ПАВ) для маркировки нефтепродукта, и способ идентификации продукта
EP3697873B1 (en) 2017-10-18 2021-05-26 Shell Internationale Research Maatschappij B.V. Method for reducing low speed pre-ignition
WO2019084657A1 (en) * 2017-11-06 2019-05-09 The Saskatchewan Research Council Process for the production of hydrocarbon biofuels
CN109897659B (zh) * 2017-12-11 2021-02-05 中国科学院大连化学物理研究所 一种液体燃料的制备方法
MX2020006266A (es) 2017-12-15 2021-01-20 Talipot Cool Extract Ip Llc Biocarbones y extractos de biocarbón que tienen compuestos de señalización solubles y método de captura de material extracto de biocarbón.
US11578275B2 (en) * 2018-01-10 2023-02-14 Steeper Energy Aps Process for upgrading oxygen containing renewable oil
US11306039B1 (en) * 2018-06-05 2022-04-19 Triad National Security, Llc System and method for making fuels
US11499107B2 (en) 2018-07-02 2022-11-15 Shell Usa, Inc. Liquid fuel compositions
CN113710778B (zh) 2019-04-01 2023-05-23 国际壳牌研究有限公司 用于减少低速提前点火的方法
CN113924353A (zh) * 2019-06-20 2022-01-11 国际壳牌研究有限公司 汽油燃料成分
WO2020260607A1 (en) 2019-06-28 2020-12-30 Shell Internationale Research Maatschappij B.V. Process for producing triptane and/or triptene
WO2021078753A1 (en) 2019-10-22 2021-04-29 Shell Internationale Research Maatschappij B.V. Method for reducing intake valve deposits
RU2734918C1 (ru) * 2019-12-30 2020-10-26 Акционерное общество "Всероссийский научно-исследовательский институт по переработке нефти" (АО "ВНИИ НП") Альтернативное автомобильное топливо для бензиновых двигателей, содержащее производное фурфурола
WO2021138367A1 (en) * 2020-01-02 2021-07-08 Clearrefining Technologies, Llc System and method for making a kerosene fuel product
WO2022094560A1 (en) 2020-10-29 2022-05-05 Marathon Petroleum Company Lp Systems and methods for separating water and removing solids from pre-treated and unfiltered feedstock
KR102561034B1 (ko) * 2021-03-17 2023-07-31 한국과학기술연구원 바이오매스의 액상 개질용 세리아 기반 불균일계 합금 촉매, 그 제조방법, 및 이를 이용하는 고순도 수소 생산 방법
WO2022228989A1 (en) 2021-04-26 2022-11-03 Shell Internationale Research Maatschappij B.V. Fuel compositions
CN117222725A (zh) 2021-04-26 2023-12-12 国际壳牌研究有限公司 燃料组合物
CN117769589A (zh) 2021-08-12 2024-03-26 国际壳牌研究有限公司 汽油燃料组合物
EP4408957A1 (en) 2021-09-29 2024-08-07 Shell Internationale Research Maatschappij B.V. Fuel compositions
US11613715B1 (en) * 2021-10-12 2023-03-28 Marathon Petroleum Company Lp Systems and methods of converting renewable feedstocks into intermediate hydrocarbon blend stocks and transportation fuels
KR102668911B1 (ko) * 2021-12-07 2024-05-28 한국과학기술연구원 니켈-철-티타니아 촉매, 이의 제조방법 및 이를 이용한 수첨탈산소 반응 방법
US11891579B2 (en) * 2022-04-18 2024-02-06 Greyrock Technology, Llc Process for the synthesis of high-value, low carbon chemical products
US11981872B2 (en) * 2022-06-20 2024-05-14 ExxonMobil Technology and Engineering Company Systems and methods for renewable fuels
WO2024017743A1 (en) 2022-07-20 2024-01-25 Shell Internationale Research Maatschappij B.V. Fuel compositions
US20240132791A1 (en) 2022-09-30 2024-04-25 Afton Chemical Corporation Fuel composition
US11939283B1 (en) * 2022-09-30 2024-03-26 Uop Llc Process for the hydrogenation of olefins
WO2024068384A1 (en) 2022-09-30 2024-04-04 Shell Internationale Research Maatschappij B.V. Fuel composition
WO2024083782A1 (en) 2022-10-21 2024-04-25 Shell Internationale Research Maatschappij B.V. Fuel compositions

Family Cites Families (108)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4013734A (en) 1973-12-14 1977-03-22 Exxon Research And Engineering Company Novel catalyst and its use for steam hydroconversion and dealkylation processes
US4223001A (en) 1978-06-20 1980-09-16 Allied Chemical Corporation Production of hydrogen from carbon monoxide and water
US4382150A (en) 1982-01-19 1983-05-03 Uop Inc. Method for hydrogenating aqueous solutions of carbohydrates
US4487980A (en) 1982-01-19 1984-12-11 Uop Inc. Method for hydrogenating aqueous solutions of carbohydrates
US4380679A (en) 1982-04-12 1983-04-19 Uop Inc. Hydrogenation of saccharides
US4380680A (en) 1982-05-21 1983-04-19 Uop Inc. Method for hydrogenating aqueous solutions of carbohydrates
US4541836A (en) 1982-12-09 1985-09-17 Union Carbide Corporation Fuel compositions
US4456779A (en) 1983-04-26 1984-06-26 Mobil Oil Corporation Catalytic conversion of olefins to higher hydrocarbons
US4503274A (en) 1983-08-08 1985-03-05 Uop Inc. Ruthenium hydrogenation catalyst with increased activity
US4554260A (en) 1984-07-13 1985-11-19 Exxon Research & Engineering Co. Two stage process for improving the catalyst life of zeolites in the synthesis of lower olefins from alcohols and their ether derivatives
AU576030B2 (en) 1984-12-31 1988-08-11 Mobil Oil Corporation Process for producing high boiling jet fuel
US4543435A (en) 1985-01-17 1985-09-24 Mobil Oil Corporation Multistage process for converting oxygenates to liquid hydrocarbons with ethene recycle
US5019135A (en) 1987-10-13 1991-05-28 Battelle Memorial Institute Method for the catalytic conversion of lignocellulosic materials
US5001292A (en) 1987-12-08 1991-03-19 Mobil Oil Corporation Ether and hydrocarbon production
US4885421A (en) 1987-12-08 1989-12-05 Harandi Mohsen N Multistage reactor system for production of fuels
US4919896A (en) 1987-12-28 1990-04-24 Mobil Oil Corporation Multistage catalytic reactor system for production of heavy hydrocarbons
US4828812A (en) 1987-12-29 1989-05-09 Mobil Oil Corporation Titanosilicates of enhanced ion exchange capacity and their preparation
US5180868A (en) * 1988-06-20 1993-01-19 Battelle Memorial Institute Method of upgrading oils containing hydroxyaromatic hydrocarbon compounds to highly aromatic gasoline
US4935568A (en) 1988-12-05 1990-06-19 Mobil Oil Corporation Multistage process for oxygenate conversion to hydrocarbons
US5130101A (en) 1989-04-28 1992-07-14 Mobil Oil Corporation Reactor system for conversion of alcohols to ether-rich gasoline
US5238898A (en) 1989-12-29 1993-08-24 Mobil Oil Corp. Catalyst and process for upgrading methane to higher hydrocarbons
US5105044A (en) 1989-12-29 1992-04-14 Mobil Oil Corp. Catalyst and process for upgrading methane to higher hydrocarbons
US5177279A (en) 1990-10-23 1993-01-05 Mobil Oil Corporation Integrated process for converting methanol to gasoline and distillates
US5139002A (en) 1990-10-30 1992-08-18 Hydrogen Consultants, Inc. Special purpose blends of hydrogen and natural gas
US5344849A (en) 1990-10-31 1994-09-06 Canada Chemical Corporation Catalytic process for the production of hydrocarbons
US5095159A (en) 1990-11-21 1992-03-10 Mobil Oil Corporation Ether and hydrocarbon production
US5096159A (en) * 1991-01-18 1992-03-17 Advantage Lift Systems, Inc. Automotive lift system
ES2118968T3 (es) 1992-06-05 1998-10-01 Battelle Memorial Institute Metodo para la conversion catalitica de materiales organicos en un producto gaseoso.
WO1995030825A1 (en) 1994-05-04 1995-11-16 University Of Central Florida Hydrogen-natural gas motor fuel
US5666923A (en) 1994-05-04 1997-09-16 University Of Central Florida Hydrogen enriched natural gas as a motor fuel with variable air fuel ratio and fuel mixture ratio control
CA2149685C (en) * 1994-06-30 1999-09-14 Jacques Monnier Conversion of depitched tall oil to diesel fuel additive
JP2671944B2 (ja) 1994-08-25 1997-11-05 工業技術院長 セルロース系バイオマスからの水素の製造方法
US5578647A (en) 1994-12-20 1996-11-26 Board Of Regents, The University Of Texas System Method of producing off-gas having a selected ratio of carbon monoxide to hydrogen
US5787863A (en) 1996-01-23 1998-08-04 Caterpillar Inc. Fuel system having priming actuating fluid accumulator
US5697987A (en) * 1996-05-10 1997-12-16 The Trustees Of Princeton University Alternative fuel
US5861137A (en) 1996-10-30 1999-01-19 Edlund; David J. Steam reformer with internal hydrogen purification
US7462207B2 (en) 1996-11-18 2008-12-09 Bp Oil International Limited Fuel composition
US5977013A (en) 1996-12-19 1999-11-02 Battelle Memorial Institute Catalyst and method for aqueous phase reactions
DE19725006C2 (de) 1997-06-13 1999-04-29 Dbb Fuel Cell Engines Gmbh Methanolreformierungsreaktor und Behandlungsverfahren für einen Katalysator hierfür
DE19725009C1 (de) 1997-06-13 1999-03-04 Dbb Fuel Cell Engines Gmbh Verfahren zur Behandlung eines Methanolreformierungskatalysators
US5959167A (en) * 1997-08-25 1999-09-28 The University Of Utah Research Foundation Process for conversion of lignin to reformulated hydrocarbon gasoline
EP0978314A4 (en) 1997-10-07 2002-03-13 Nippon Kokan Kk CATALYST FOR THE PRODUCTION OF HYDROGEN OR SYNTHESIS GAS AND METHOD FOR THE PRODUCTION THEREOF
DE69925052T2 (de) 1998-01-21 2006-03-02 Haldor Topsoe A/S Verfahren zur Herstellung von wasserstoffreichem Gas
JPH11217343A (ja) 1998-01-30 1999-08-10 Sangi Co Ltd 化学工業原料及びハイオク燃料の合成法
US6054041A (en) 1998-05-06 2000-04-25 Exxon Research And Engineering Co. Three stage cocurrent liquid and vapor hydroprocessing
GR1003235B (el) 1998-05-22 1999-10-13 Διεργασια παραγωγης υδρογονου και ηλεκτρικης ενεργειας απο αναμορφωση βιο-αιθανολης, με χρηση κυψελιδων καυσιμου και με μηδενικη εκπομπη ρυπων
AU740872B2 (en) 1998-06-09 2001-11-15 Idemitsu Kosan Co. Ltd Catalyst and process for reforming hydrocarbon
US6479428B1 (en) 1998-07-27 2002-11-12 Battelle Memorial Institute Long life hydrocarbon conversion catalyst and method of making
US6440895B1 (en) 1998-07-27 2002-08-27 Battelle Memorial Institute Catalyst, method of making, and reactions using the catalyst
US6172272B1 (en) 1998-08-21 2001-01-09 The University Of Utah Process for conversion of lignin to reformulated, partially oxygenated gasoline
US6353143B1 (en) * 1998-11-13 2002-03-05 Pennzoil-Quaker State Company Fuel composition for gasoline powered vehicle and method
US6207132B1 (en) 1998-12-04 2001-03-27 Chinese Petroleum Corporation Process for producing high purity hydrogen
US7273957B2 (en) 1999-05-04 2007-09-25 Catalytic Distillation Technologies Process for the production of gasoline stocks
EP1063011B1 (de) 1999-05-22 2001-12-12 OMG AG & Co. KG Verwendung eines Katalysators für die Dampfreformierung von Methanol
US20020020107A1 (en) * 1999-07-02 2002-02-21 Bailey Brent K. Low molecular weight compression ignition fuel
US6372680B1 (en) 1999-07-27 2002-04-16 Phillips Petroleum Company Catalyst system for converting oxygenated hydrocarbons to aromatics
US6969506B2 (en) 1999-08-17 2005-11-29 Battelle Memorial Institute Methods of conducting simultaneous exothermic and endothermic reactions
US6570043B2 (en) 1999-09-03 2003-05-27 Battelle Memorial Institute Converting sugars to sugar alcohols by aqueous phase catalytic hydrogenation
US6235797B1 (en) 1999-09-03 2001-05-22 Battelle Memorial Institute Ruthenium on rutile catalyst, catalytic system, and method for aqueous phase hydrogenations
US6761745B2 (en) * 2000-01-24 2004-07-13 Angelica Hull Method of reducing the vapor pressure of ethanol-containing motor fuels for spark ignition combustion engines
US6291725B1 (en) 2000-03-03 2001-09-18 Board Of Trustees Operating Michigan State University Catalysts and process for hydrogenolysis of sugar alcohols to polyols
US6397790B1 (en) 2000-04-03 2002-06-04 R. Kirk Collier, Jr. Octane enhanced natural gas for internal combustion engine
US6508209B1 (en) 2000-04-03 2003-01-21 R. Kirk Collier, Jr. Reformed natural gas for powering an internal combustion engine
US7029506B2 (en) * 2000-04-14 2006-04-18 Jordan Frederick L Organic cetane improver
CN1487911A (zh) 2000-12-23 2004-04-07 �������¹ɷ����޹�˾ 通过氢化羰基化合物生产醇的方法
US6765101B1 (en) 2001-05-01 2004-07-20 Union Carbide Chemicals & Plastics Technology Corporation Synthesis of lower alkylene oxides and lower alkylene glycols from lower alkanes and/or lower alkenes
DE10128203A1 (de) 2001-06-11 2002-12-12 Basf Ag Verfahren zur Herstellung von Sorbit
US6670300B2 (en) 2001-06-18 2003-12-30 Battelle Memorial Institute Textured catalysts, methods of making textured catalysts, and methods of catalyzing reactions conducted in hydrothermal conditions
US6607707B2 (en) 2001-08-15 2003-08-19 Ovonic Battery Company, Inc. Production of hydrogen from hydrocarbons and oxygenated hydrocarbons
US20030115792A1 (en) 2001-10-05 2003-06-26 Shabtai Joseph S Process for converting lignins into a high octane blending component
US20030100807A1 (en) * 2001-10-05 2003-05-29 Shabtai Joseph S Process for converting lignins into a high octane additive
US6841085B2 (en) 2001-10-23 2005-01-11 Battelle Memorial Institute Hydrogenolysis of 6-carbon sugars and other organic compounds
US6479713B1 (en) 2001-10-23 2002-11-12 Battelle Memorial Institute Hydrogenolysis of 5-carbon sugars, sugar alcohols, and other methods and compositions for reactions involving hydrogen
NZ533175A (en) 2001-11-29 2006-03-31 Wisconsin Alumni Res Found Low-temperature hydrogen production from oxygenated hydrocarbons
US6699457B2 (en) 2001-11-29 2004-03-02 Wisconsin Alumni Research Foundation Low-temperature hydrogen production from oxygenated hydrocarbons
US6953873B2 (en) 2002-05-10 2005-10-11 Wisconsin Alumni Research Foundation Low-temperature hydrocarbon production from oxygenated hydrocarbons
US6739125B1 (en) 2002-11-13 2004-05-25 Collier Technologies, Inc. Internal combustion engine with SCR and integrated ammonia production
JP4150579B2 (ja) * 2002-12-03 2008-09-17 昭和シェル石油株式会社 灯油組成物
US7199250B2 (en) 2002-12-20 2007-04-03 Battelle Memorial Institute Process for producing cyclic compounds
US6982328B2 (en) 2003-03-03 2006-01-03 Archer Daniels Midland Company Methods of producing compounds from plant material
US20050203195A1 (en) 2003-08-05 2005-09-15 Yong Wang Tailored Fischer-Tropsch synthesis product distribution
FR2867464B1 (fr) 2004-03-10 2006-06-09 Inst Francais Du Petrole Procede de production d'hydrogene a tres haute purete a partir d'alcools comportant au moins deux atomes de carbone
WO2005121020A2 (en) 2004-06-03 2005-12-22 Rogers Charles J Low temperature methods for hydrogen production
US20060013759A1 (en) 2004-07-13 2006-01-19 Conocophillips Company Systems and methods for hydrogen production
WO2006119357A2 (en) 2005-05-02 2006-11-09 University Of Utah Research Foundation Processes for catalytic conversion of lignin to liquid bio-fuels
US7288685B2 (en) 2005-05-19 2007-10-30 Uop Llc Production of olefins from biorenewable feedstocks
US7814091B2 (en) * 2005-09-27 2010-10-12 Oracle International Corporation Multi-tiered query processing techniques for minus and intersect operators
US8053614B2 (en) * 2005-12-12 2011-11-08 Neste Oil Oyj Base oil
FI20055665L (fi) * 2005-12-12 2007-06-13 Neste Oil Oyj Prosessi haarautuneen hiilivetykomponentin valmistamiseksi
KR101102878B1 (ko) * 2005-12-12 2012-01-10 네스테 오일 오와이제이 분지형 탄화수소 성분의 제조방법
US7678950B2 (en) 2005-12-16 2010-03-16 Conocophillips Company Process for converting carbohydrates to hydrocarbons
US8231857B2 (en) * 2005-12-21 2012-07-31 Virent, Inc. Catalysts and methods for reforming oxygenated compounds
US7615652B2 (en) 2006-01-26 2009-11-10 Battelle Memorial Institute Two-stage dehydration of sugars
US7649099B2 (en) 2006-01-26 2010-01-19 Battelle Memorial Institute Method of forming a dianhydrosugar alcohol
RU2454391C2 (ru) * 2006-05-08 2012-06-27 Вайрент, Инк. Способы и системы для получения многоатомных спиртов
US7880049B2 (en) * 2006-06-06 2011-02-01 Wisconsin Alumni Research Foundation Production of liquid alkanes in the jet fuel range (C8-C15) from biomass-derived carbohydrates
JP2008088140A (ja) * 2006-10-05 2008-04-17 Sangi Co Ltd 化学工業原料及び燃料組成物の合成方法
EP2698416B1 (en) 2007-03-08 2020-07-08 Virent, Inc. Synthesis of Liquid Fuels from Oxygenated Hydrocarbons
RU2472840C2 (ru) 2007-03-08 2013-01-20 Вайрент, Инк. Синтез жидкого топлива и химических реактивов из кислородсодержащих углеводородов
US7425657B1 (en) * 2007-06-06 2008-09-16 Battelle Memorial Institute Palladium catalyzed hydrogenation of bio-oils and organic compounds
FI121308B (fi) * 2007-06-11 2010-09-30 Neste Oil Oyj Prosessi haaroittuneiden hiilivetyjen valmistamiseksi
US8143469B2 (en) * 2007-06-11 2012-03-27 Neste Oil Oyj Process for producing branched hydrocarbons
US8048290B2 (en) * 2007-06-11 2011-11-01 Neste Oil Oyj Process for producing branched hydrocarbons
KR20100052465A (ko) * 2007-06-29 2010-05-19 에너지 & 인바이런멘탈 리서치 센터 파운데이션 독립적으로 제조된 혼합원료로부터 제조된 항공기용 케로센
CN101952398B (zh) * 2007-12-03 2014-05-21 格沃股份有限公司 可再生组合物
US8075642B2 (en) * 2008-04-14 2011-12-13 Wisconsin Alumni Research Foundation Single-reactor process for producing liquid-phase organic compounds from biomass
JP2012501338A (ja) 2008-08-27 2012-01-19 ヴァイレント エナジー システムズ インク． バイオマスからの液体燃料の合成
US8697924B2 (en) 2008-09-05 2014-04-15 Shell Oil Company Liquid fuel compositions

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2616620C2 (ru) * 2011-05-23 2017-04-18 Вайрент, Инк. Производство химических веществ и топлив из биомассы

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