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1. 发明申请

WO2008081101A3 METHOD FOR CONVERTING LOADS FROM RENEWABLE SOURCES INTO GOOD-QUALITY DIESEL FUEL BASES 审中-公开
标题翻译：将可再生能源中的负荷转化为优质柴油燃料的方法
公开(公告)号：WO2008081101A3
公开(公告)日：2008-11-13
申请号：PCT/FR2007001977
申请日：2007-11-30
申请人： INST FRANCAIS DU PETROLE
发明人： DUPASSIEUX NATHALIE , CHAPUS THIERRY
IPC分类号： C10G3/00 , C10G45/08 , C10G45/62 , C10G65/04
CPC分类号： C10G3/46 , C10G3/48 , C10G3/50 , C10G3/54 , C10G45/08 , C10G45/62 , C10G65/043 , C10G2300/1011 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/4025 , C10G2400/04 , Y02P30/20
摘要： The invention to a method for processing loads from renewable sources in order to produce excellent quality diesel fuel bases. The loads used may consist of raw vegetal oils or vegetal oils previously submitted to a pre-refining step, of animal fats, or mixtures of such loads. The invention also relates to a method for obtaining diesel-bases high yields from such loads.
摘要翻译：本发明涉及一种处理来自可再生资源的负载以产生优质柴油燃料基地的方法。所使用的负载可能包括以前进行预精炼步骤的生植物油或植物油，动物脂肪或这些负载的混合物。本发明还涉及一种从这种负载获得高产量柴油机的方法。

2. 发明申请

WO2009037400A2 ?HYDROCONVERSION METHOD IN A BUBBLING BED WITH BIORENEWABLE CHARGES FOR THE PRODUCTION OF FUEL STOCKS 审中-公开
标题翻译：？用于生产燃料库的可生物发电的燃烧床中的氢转移方法
公开(公告)号：WO2009037400A2
公开(公告)日：2009-03-26
申请号：PCT/FR2008001065
申请日：2008-07-18
申请人： INST FRANCAIS DU PETROLE , DAUDIN ANTOINE , DUPASSIEUX NATHALIE , CHAPUS THIERRY , QUIGNARD ALAIN
发明人： DAUDIN ANTOINE , DUPASSIEUX NATHALIE , CHAPUS THIERRY , QUIGNARD ALAIN
IPC分类号： C10G49/04 , B01J8/22 , B01J21/04 , B01J23/883 , C10G3/00 , C10G49/12 , C10L1/02 , C11B3/12
CPC分类号： C10G49/04 , C10G3/46 , C10G3/48 , C10G3/50 , C10G3/56 , C10G49/12 , C10G2300/1014 , C10G2300/1018 , C10G2300/301 , C10G2300/4018 , C10G2400/06 , C10G2400/08 , Y02P30/20
摘要： The invention relates to a method for hydrotreatment and/or hydroconversion of a biorenewable charge containing triglyceride and/or fatty acid structures the fatty chains of which have between 8 and 25 carbon atoms said method comprising the following steps: a) hydrotreatment and/or hydroconversion of said biorenewable charge in a bubbling bed reactor in the presence of a granular catalyst with at least one metal or metal compound having a hydrogenation or deshydrogenation function on an amorphous support to give a first stream, b) introduction of the stream produced in a) to a distillation zone from which a gas fraction and at least one distillate cut the final boiling point of which is less than 4000C are obtained.
摘要翻译：本发明涉及一种用于加氢处理和/或加氢转化含有甘油三酯和/或脂肪酸结构的生物可逆电荷的方法，其脂肪链具有8至25个碳原子，所述方法包括以下步骤：a）加氢处理和/或加氢转化在具有至少一种在无定形载体上具有氢化或脱氢功能的金属或金属化合物的颗粒催化剂存在下，在鼓泡床反应器中产生所述生物可再生电荷以产生第一流，b）引入在a）到达蒸馏区，从该蒸馏区获得气馏分和至少一个切出其最终沸点小于4000℃的馏出物。

3. 发明专利

BRPI0903654A2 未知
公开(公告)号：BRPI0903654A2
公开(公告)日：2011-09-06
申请号：BRPI0903654
申请日：2009-06-19
申请人： INST FRANCAIS DU PETROLE
发明人： GUILLON EMMANUELLE , BOUCHY CHRISTOPHE , DUPASSIEUX NATHALIE , DAUDIN ANTOINE , CHAPUS THIERRY
IPC分类号： C10G3/00 , B01J29/072 , C10G45/08 , C10G45/64
摘要： Treating feedstock from renewable vegetable/animal source involves (a) subjecting feedstock to hydrotreatment in presence of fixed-bed catalyst and hydrogen mixed with feedstock such that hydrogen/feedstock ratio is 150-750 Nm 3>hydrogen/m 3>feedstock, (b) separation of hydrogen, other gases and hydrocarbon-containing base, (c) hydroisomerization of base in presence of selective catalyst, the stage (c) is carried out in presence of hydrogen mixed with the feedstock such that the hydrogen/feedstock ratio is 70-1000 Nm 3>/m 3>feedstock, (d) separation of diesel fuel base. Treating a feedstock from a renewable vegetable or animal source involves (a) subjecting the feedstock to hydrotreatment in presence of fixed-bed catalyst containing hydro-dehydrogenizing function and an amorphous support, at 200-450[deg] C., at a pressure of 1-10 MPa, at hourly space velocity of 0.1-10 -> 1>and in presence of hydrogen mixed with the feedstock such that the hydrogen/feedstock ratio is 150 and 750 Nm 3>hydrogen/m 3>feedstock to produce an effluent, (b) separation, from the effluent from stage (a), of the hydrogen, other gases and at least one hydrocarbon-containing base, (c) hydroisomerization of at least part of the hydrocarbon-containing base from stage (b) in presence of fixed-bed hydroisomerization selective catalyst, the catalyst comprising at least one group VIII metal and/or at least one VIB group metal and at least one mono-dimensional 10 MR zeolite molecular sieve, the stage (c) is carried out at 150-500[deg] C, at pressure of 1-10 MPa, at an hourly space velocity of 0.1-10 h -> 1>and in presence of hydrogen mixed with the feedstock such that the hydrogen/feedstock ratio is 70-1000 Nm 3>/m 3>feedstock to produce an effluent, (d) separation, from the effluent from stage (c), of the hydrogen, other gases and at least one diesel fuel base. An independent claim is included for method (M2) involving providing an effluent from a hydrotreatment of a renewable animal or vegetable source and subjecting the effluent to a hydroisomerization stage with at least one hydroisomerization catalyst comprising at least one group VIII and/or group VI metal and at least one mono-dimensional 10 MR zeolite molecular sieve (S1).

4. 发明专利

FR2910483B1 PROCEDE DE CONVERSION DE CHARGES ISSUES DE SOURCES RENOUVELABLES EN BASES CARBURANTS GAZOLES DE BONNE QUALITE. 未知
公开(公告)号：FR2910483B1
公开(公告)日：2010-07-30
申请号：FR0611398
申请日：2006-12-21
申请人： INST FRANCAIS DU PETROLE
发明人： DUPASSIEUX NATHALIE , CHAPUS THIERRY
IPC分类号： C10G3/00 , C10G45/08 , C10G45/62 , C10G45/64

5. 发明专利

GB2405361A Gas processing method using a filtered glycol solution 未知
公开(公告)号：GB2405361A
公开(公告)日：2005-03-02
申请号：GB0416551
申请日：2004-07-26
申请人： INST FRANCAIS DU PETROLE
发明人： BAUDOT ARNAUD , DUPASSIEUX NATHALIE , MONTES SOPHIE
IPC分类号： B01D53/14 , B01D53/28 , B01D53/96 , B01D61/00 , B01D61/14 , B01D61/58 , C07C29/76 , C10L3/10
摘要： A liquid effluent comprising glycol, water and salts is dehydrated 14 and at least part of the liquid effluent is filtered through a nanofilter membrane 10 having a pore size ranging between 5 - 100 Angstrom. A pressure difference is applied between the two faces of the membrane and the effluent is preferably expanded 8 prior to being filtered. The liquid effluent is separated from a hydrocarbon feed (especially natural gas), wherein glycol is mixed with the natural gas during transportation by a circulation line in order to prevent hydrate formation. The recovered glycol may be recycled and re-used as a hydrate inhibitor.

6. 发明专利

GB2405361B Gas processing method using a filtered glycol solution 未知
公开(公告)号：GB2405361B
公开(公告)日：2007-03-28
申请号：GB0416551
申请日：2004-07-26
申请人： INST FRANCAIS DU PETROLE
发明人： BAUDOT ARNAUD , DUPASSIEUX NATHALIE , MONTES SOPHIE
IPC分类号： B01D61/00 , B01D53/14 , B01D53/28 , B01D53/96 , B01D61/14 , B01D61/58 , C07C29/76 , C10L3/10
摘要： The invention relates to a method and to a plant for processing a gas by means of a glycol solution wherein a feed comprising a gas, a glycol, water and salts is subjected to a first stage ( 5 ) of separating the gas from a liquid effluent and said liquid effluent is subjected to a dehydration stage ( 14 ) to recover a dehydrated liquid effluent, characterized in that the salts contained in the liquid effluent, dehydrated or not, are eliminated in a membrane separation stage ( 10 ) by means of a driving force generated by mechanical pressure difference on either side of a membrane of pore size ranging between 5 and 100 Angstrom. The invention also relates to the use of the method and of the plant for regeneration of a liquid compound of the glycol family used for hydrate formation prevention when using a natural gas.

7. 发明专利

NO20043218L 未知
公开(公告)号：NO20043218L
公开(公告)日：2005-01-31
申请号：NO20043218
申请日：2004-07-29
申请人： INST FRANCAIS DU PETROLE
发明人： BAUDOT ARNAUD , DUPASSIEUX NATHALIE , MONTES SOPHIE
IPC分类号： B01D53/14 , B01D53/28 , B01D53/96 , B01D61/00 , B01D61/14 , B01D61/58 , C07C29/76 , C10L3/10
摘要： The invention relates to a method and to a plant for processing a gas by means of a glycol solution wherein a feed comprising a gas, a glycol, water and salts is subjected to a first stage ( 5 ) of separating the gas from a liquid effluent and said liquid effluent is subjected to a dehydration stage ( 14 ) to recover a dehydrated liquid effluent, characterized in that the salts contained in the liquid effluent, dehydrated or not, are eliminated in a membrane separation stage ( 10 ) by means of a driving force generated by mechanical pressure difference on either side of a membrane of pore size ranging between 5 and 100 Angstrom. The invention also relates to the use of the method and of the plant for regeneration of a liquid compound of the glycol family used for hydrate formation prevention when using a natural gas.

8. 发明专利

NO20043218A 未知
公开(公告)号：NO20043218A
公开(公告)日：2005-01-31
申请号：NO20043218
申请日：2004-07-29
申请人： INST FRANCAIS DU PETROLE
发明人： BAUDOT ARNAUD , DUPASSIEUX NATHALIE , MONTES SOPHIE
IPC分类号： B01D53/14 , B01D53/28 , B01D53/96 , B01D61/00 , B01D61/14 , B01D61/58 , C07C29/76 , C10L3/10
CPC分类号： B01D61/147 , B01D61/145 , C07C29/76 , C10L3/10 , C07C31/20

9. 发明专利

FR2949475B1 PROCEDE DE CONVERSION DE CHARGES ISSUES DE SOURCES RENOUVELABLES EN CO-TRAITEMENT AVEC UNE CHARGE PETROLIERE METTANT EN OEUVRE UN CATALYSEUR A BASE DE MOLYBDENE 未知
公开(公告)号：FR2949475B1
公开(公告)日：2012-04-20
申请号：FR0904160
申请日：2009-09-02
申请人： INST FRANCAIS DU PETROLE
发明人： DUPASSIEUX NATHALIE , DAUDIN ANTOINE , CHAPUS THIERRY
IPC分类号： C10G65/08 , C10G45/04 , C10G45/50 , C10G45/58 , C10G49/04

10. 发明专利

AR076079A1 PROCESO PARA LA HIDROGENACION CONTINUA DE MATERIAS PRIMAS QUE CONTIENEN TRIGLICERIDOS 未知
公开(公告)号：AR076079A1
公开(公告)日：2011-05-18
申请号：ARP100100649
申请日：2010-03-04
申请人： INST FRANCAIS DU PETROLE
发明人： DUPASSIEUX NATHALIE , ESCHENROEDER FRANK , ABE DETLEF , LABAN DAVID , SCHUETTER HARTMUT , BOURNAY LAURENT , CHAPUS THIERRY
IPC分类号： C10G3/00 , C10G45/02
摘要： Un proceso para la hidrogenacion continua de materias primas que contienen triglicéridos en un sistema de reactor de lecho fijo de varios lechos catalizadores dispuestos en serie y que comprende un catalizador de hidrogenacion. La alimentacion de materia prima, el gas que contiene hidrogeno y el agente diluyente se pasan juntos a través de los lechos catalizadores a condiciones de hidrogenacion. Tanto el flujo de alimentacion de materia prima como así también el flujo de gas que contiene hidrogeno están divididos en un numero igual de diferentes flujos parciales. Cada uno de estos se pasa a un lecho catalizador de manera tal que la relacion en peso del agente diluyente a alimentacion de materia prima es esencialmente igual a la entrada de todos los lechos catalizadores y no excede de 4:1. El proceso que se reivindica preferentemente se lleva a cabo a bajas temperaturas y permite el uso de unidades existentes debido a la baja relacion de reciclado. Además, se usa un exceso suficiente de hidrogeno de modo tal que no haya una pérdida de producto valioso a través de las reacciones de decarboxilacion.

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