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11. 发明专利

CA3101415A1 PROCEDE DE TRAITEMENT DE LA BIOMASSE PAR CO-BROYAGE AVEC UNE SECONDE CHARGE DE BIOMASSE 未知
公开(公告)号：CA3101415A1
公开(公告)日：2019-12-26
申请号：CA3101415
申请日：2019-06-12
申请人： IFP ENERGIES NOW , AXENS , COMMISSARIAT ENERGIE ATOMIQUE , TOTAL RAFFINAGE CHIMIE , THYSSENKRUPP IND SOLUTIONS AG , AVRIL , BIONEXT
发明人： PLENNEVAUX THOMAS , GAZARIAN JEREMY , BOURNAY LAURENT , ULLRICH NORBERT , HECQUET MICHAEL
IPC分类号： C10L5/36 , B02C21/00 , C10J3/00 , C10L5/44 , C10L9/08
摘要： La présente invention a pour objet un procédé de traitement d'une charge comprenant de la biomasse, ledit procédé comprenant au moins les étapes suivantes : a) Une étape de séchage de ladite charge à une température comprise entre 20 et 180°C, pendant une durée comprise entre 5 et 180 minutes, b) Une étape de torréfaction de la charge séchée issue de l'étape a) pour produire au moins un effluent solide biomasse torréfiée, et c) Une étape de co-broyage de l'effluent solide biomasse torréfiée issu de l'étape b) en présence d'une seconde charge de biomasse pour obtenir une poudre.

12. 发明专利

ES2927344T3 Procedimiento de tratamiento de la biomasa por co-trituración con una segunda carga de biomasa 未知
公开(公告)号：ES2927344T3
公开(公告)日：2022-11-04
申请号：ES19729301
申请日：2019-06-12
申请人： IFP ENERGIES NOW , AXENS , COMMISSARIAT ENERGIE ATOMIQUE , TOTALENERGIES ONETECH , THYSSENKRUPP IND SOLUTIONS AG , AVRIL , BIONEXT
发明人： PLENNEVAUX THOMAS , GAZARIAN JEREMY , BOURNAY LAURENT , ULLRICH NORBERT , HECQUET MICHAEL
IPC分类号： C10L5/36 , B02C21/00 , C10B49/02 , C10B53/02 , C10B57/14 , C10J3/00 , C10J3/62 , C10L5/44 , C10L9/08
摘要： La presente invención se refiere a un método para procesar una materia prima que contiene biomasa, comprendiendo dicho método al menos los siguientes pasos: a) una etapa de secado de dicha materia prima a una temperatura entre 20 y 180 °C durante una duración de entre 5 y 180 minutos , b) un paso de torrefacción de la materia prima seca proveniente del paso a) para producir al menos un efluente de biomasa sólida torrefactada, y c) un paso de co-molienda del efluente de biomasa sólida torrefactada del paso b) en presencia de un segundo materia prima de biomasa para obtener un polvo. (Traducción automática con Google Translate, sin valor legal)

13. 发明专利

FR3082850B1 PROCEDE DE TRAITEMENT DE LA BIOMASSE PAR CO-BROYAGE AVEC UNE SECONDE CHARGE DE BIOMASSE 未知
公开(公告)号：FR3082850B1
公开(公告)日：2021-01-08
申请号：FR1855487
申请日：2018-06-21
申请人： COMMISSARIAT ENERGIE ATOMIQUE , IFP ENERGIES NOW , AXENS , TOTAL RAFFINAGE CHIMIE , THYSSENKRUPP IND SOLUTIONS AG , AVRIL , BIONEXT
发明人： PLENNEVAUX THOMAS , GAZARIAN JEREMY , BOURNAY LAURENT , ULLRICH NORBERT , HECQUET MICHAEL
IPC分类号： C10B53/02 , B02C23/06 , C10B57/10
摘要： La présente invention a pour objet un procédé de traitement d'une charge comprenant de la biomasse, ledit procédé comprenant au moins les étapes suivantes : a) Une étape de séchage de ladite charge à une température comprise entre 20 et 180°C, pendant une durée comprise entre 5 et 180minutes, b) Une étape de torréfaction de la charge séchée issue de l'étape a) pour produire au moins un effluent solide biomasse torréfiée, et c) Une étape de co-broyage de l'effluent solide biomasse torréfiée issu de l'étape b) en présence d'une seconde charge de biomasse pour obtenir une poudre.

17. 发明申请

WO2010046590A3 PROCESS FOR OBTAINING BIOKEROSENE 审中-公开
标题翻译：获得生物酮的方法
公开(公告)号：WO2010046590A3
公开(公告)日：2010-06-17
申请号：PCT/FR2009051998
申请日：2009-10-20
申请人： TOTAL RAFFINAGE MARKETING , MAYEUR VINCENT , HECQUET MICHAEL , DEMOMENT PASCALE
发明人： MAYEUR VINCENT , HECQUET MICHAEL , DEMOMENT PASCALE
IPC分类号： C10G3/00 , C09D7/47 , C10G47/00 , C10G49/00 , C10G65/04 , C10G65/12 , C10L1/02
CPC分类号： C10L1/04 , C10G3/50 , C10G45/02 , C10G47/00 , C10G65/04 , C10G65/10 , C10G65/12 , C10G2300/1003 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/1055 , C10G2300/107 , C10G2300/1074 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10G2300/4081 , C10G2400/08 , C10G2400/18 , C10L1/06 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要： The invention relates to a process comprising the steps consisting in: - carrying out a hydrotreatment or a hydrocracking operated under a pressure of 20 to 120 bar and at a temperature between 250 and 500°C, preferably between 350 and 400°C, on a hydrocarbon-based feedstock comprising or consisting of a feedstock of petroleum origin, a feedstock of biological origin comprising or constituted by plant oils and/or animal fats, at least 5% by weight of the fatty acids of which have a chain length less than or equal to 14 carbon atoms relative to the total weight of the triglycerides, preferably at least 20% by weight, or even at least 50% by weight - carrying out a fractionation so as to recover a kerosene fraction, said fraction preferably having a boiling point below 300°C, and more preferably still a boiling point below 240°C.
摘要翻译：本发明涉及一种方法，其包括以下步骤： - 在20至120巴的压力下和在250至500℃之间，优选350至400℃的温度下进行加氢处理或加氢裂化，包含或由石油来源的原料组成的基于烃的原料，包含植物油和/或动物脂肪的生物来源的原料，至少5重量％的脂肪酸具有小于或等于相对于甘油三酯的总重量相当于14个碳原子，优选至少20重量％，或甚至至少50重量％，进行分馏以回收煤油馏分，所述馏分优选具有沸点低于300℃，更优选仍低于240℃的沸点。

18. 发明专利

FR2937647A1 PROCEDE D'OBTENTION DE BIOKEROSENE 未知
公开(公告)号：FR2937647A1
公开(公告)日：2010-04-30
申请号：FR0805911
申请日：2008-10-24
申请人： TOTAL RAFFINAGE MARKETING
发明人： MAYEUR VINCENT , HECQUET MICHAEL , DEMOMENT PASCALE
IPC分类号： C10G49/22 , A01N27/00 , C09D7/47 , C10G3/00 , C10L1/04 , C11D7/50
摘要： L'invention concerne un procédé comprenant les étapes consistant à : - effectuer un hydrotraitement ou un hydrocraquage opéré sous une pression de 20 à 120 bars et à une température comprise entre 250 et 500°C, préférentiellement entre 350 et 400°C, sur une charge hydrocarbonée comprenant ou consistant en une charge d'origine pétrolière, une charge d'origine biologique comprenant ou constituée par des huiles végétales et/ou des graisses animales dont au moins 5 % en poids des acides gras ont une longueur de chaîne inférieure ou égale à 14 atomes de carbone par rapport au poids total des triglycérides, préférentiellement au moins 20 % en poids, voire au moins 50 % en poids - effectuer un fractionnement de manière à récupérer une fraction kérosène, ladite fraction ayant préférentiellement un point d'ébullition inférieur à 300°C, et encore plus préférentiellement un point d'ébullition inférieur à 240°C.

19. 发明专利

ZA200901290B METHOD FOR THE HYDRO-PROCESSING OF A GAS OIL FEEDSTOCK AND CORRESPONDING HYDRO-REFINING UNIT 未知
公开(公告)号：ZA200901290B
公开(公告)日：2010-02-24
申请号：ZA200901290
申请日：2009-02-23
申请人： TOTAL RAFFINAGE MARKETING
发明人： MAYEUR VINCENT , VERGEL CESAR , MORVAN GIDAS , MARIETTE LAURENT , HECQUET MICHAEL
IPC分类号： C10G20060101
摘要： The process for catalytic hydrotreatment of gas oil feedstock and biological origin of vegetable oil- and animal fat feedstock (less than 15 wt.%) in a unit with fixed bed, comprises injecting the oil feedstock in a first reactor, injecting a part of the biological feedstock in the first reactor and other part in a second reactor, injecting a liquid effluent withdrawn from the first reactor in the second reactor, and effecting a supplementary treatment of carbon monoxide present in the gas recycled from the hydrotreatment of the total feedstock. The process for catalytic hydrotreatment of gas oil feedstock and biological origin of vegetable oil- and animal fat feedstock (less than 15 wt.%) in a unit with fixed bed, comprises injecting the oil feedstock in a first reactor, injecting a part of the biological feedstock in the first reactor and other part in a second reactor, injecting a liquid effluent withdrawn from the first reactor in the second reactor, effecting a supplementary treatment of carbon monoxide present in the gas recycled from the hydrotreatment of the total feedstock, and controlling the exothermicity of the biological feedstock hydrotreatment using a thermal regulation system. The gas oil feedstock is a gas fraction originating from distillation of crude oil and/or synthetic crude obtained from the treatment of bituminous schists, other heavy crude oils or effluent of Fischer Tropsch process, and originating from catalytic and/or thermal cracking (fluid catalytic cracking, coking, visbreaking). The catalytic injection zone of the biological feedstock comprises a first catalytic bed trap with metals. A quantity of hydrogen (120-450 Normoliters per liters of gas oil feedstock, and 200-1000 Normoliters per liters of biological feedstock) is introduced in the first and second catalytic zone respectively. The gas oil feedstock and biological feedstock are treated in the first and second catalytic zone at a temperature of 340-400[deg] C and 280-350[deg] C and at a pressure of 30-70 bars respectively. Spatial speed of the oil feedstock and biological feedstock in the first and second zone is 0.6-3 and 1-5 respectively. The biological feedstock crosses a catalytic bed having a catalyst in the hydrotreatment unit. Water is injected at a level of the biological feedstock treatment zone. The carbon monoxide is treated by a conversion unit using a reaction of carbon monoxide shift. A pressure swing adsorption unit is arranged for separating methane, ethane and propane, and the separated compounds are used in steam methane reformer. Carbon dioxide and hydrogen sulfide present in the recylce gas is treated or separated before re-injecting the gas in the hydrotreatment unit. The thermal regulation system has a liquid at a level of the biological feedstock treatment zone, and recuperates the heat of the effluent in the first reactor thus lowering the effluent temperature before injecting it to the second reactor. The hydrotreatment unit operates in a manner such that no liquid effluent recycles at the top of the reactor. Independent claims are included for: (1) a catalytic hydrotreatment unit; and (2) a hydroforming unit.

20. 发明专利

BRPI0716191A2 未知
公开(公告)号：BRPI0716191A2
公开(公告)日：2013-11-12
申请号：BRPI0716191
申请日：2007-12-11
申请人： TOTAL RAFFINAGE MARKETING
发明人： MAYEUR VINCENT , VERGEL CESAR , MORVAN GILDAS , MARIETTE LAURENT , HECQUET MICHAEL
IPC分类号： C10G3/00 , C10G45/02 , C10G49/00 , C10G65/04
摘要： The process for catalytic hydrotreatment of gas oil feedstock and biological origin of vegetable oil- and animal fat feedstock (less than 15 wt.%) in a unit with fixed bed, comprises injecting the oil feedstock in a first reactor, injecting a part of the biological feedstock in the first reactor and other part in a second reactor, injecting a liquid effluent withdrawn from the first reactor in the second reactor, and effecting a supplementary treatment of carbon monoxide present in the gas recycled from the hydrotreatment of the total feedstock. The process for catalytic hydrotreatment of gas oil feedstock and biological origin of vegetable oil- and animal fat feedstock (less than 15 wt.%) in a unit with fixed bed, comprises injecting the oil feedstock in a first reactor, injecting a part of the biological feedstock in the first reactor and other part in a second reactor, injecting a liquid effluent withdrawn from the first reactor in the second reactor, effecting a supplementary treatment of carbon monoxide present in the gas recycled from the hydrotreatment of the total feedstock, and controlling the exothermicity of the biological feedstock hydrotreatment using a thermal regulation system. The gas oil feedstock is a gas fraction originating from distillation of crude oil and/or synthetic crude obtained from the treatment of bituminous schists, other heavy crude oils or effluent of Fischer Tropsch process, and originating from catalytic and/or thermal cracking (fluid catalytic cracking, coking, visbreaking). The catalytic injection zone of the biological feedstock comprises a first catalytic bed trap with metals. A quantity of hydrogen (120-450 Normoliters per liters of gas oil feedstock, and 200-1000 Normoliters per liters of biological feedstock) is introduced in the first and second catalytic zone respectively. The gas oil feedstock and biological feedstock are treated in the first and second catalytic zone at a temperature of 340-400[deg] C and 280-350[deg] C and at a pressure of 30-70 bars respectively. Spatial speed of the oil feedstock and biological feedstock in the first and second zone is 0.6-3 and 1-5 respectively. The biological feedstock crosses a catalytic bed having a catalyst in the hydrotreatment unit. Water is injected at a level of the biological feedstock treatment zone. The carbon monoxide is treated by a conversion unit using a reaction of carbon monoxide shift. A pressure swing adsorption unit is arranged for separating methane, ethane and propane, and the separated compounds are used in steam methane reformer. Carbon dioxide and hydrogen sulfide present in the recylce gas is treated or separated before re-injecting the gas in the hydrotreatment unit. The thermal regulation system has a liquid at a level of the biological feedstock treatment zone, and recuperates the heat of the effluent in the first reactor thus lowering the effluent temperature before injecting it to the second reactor. The hydrotreatment unit operates in a manner such that no liquid effluent recycles at the top of the reactor. Independent claims are included for: (1) a catalytic hydrotreatment unit; and (2) a hydroforming unit.

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