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1. 发明申请

US20050169825A1 Method of collecting carbon dioxide contained in fumes 审中-公开
标题翻译：收集烟雾中二氧化碳的方法
公开(公告)号：US20050169825A1
公开(公告)日：2005-08-04
申请号：US11014788
申请日：2004-12-20
申请人： Renaud Cadours , Pierre-Louis Carrette , Pascal Mougin , Paul Broutin , Pierre Boucot
发明人： Renaud Cadours , Pierre-Louis Carrette , Pascal Mougin , Paul Broutin , Pierre Boucot
IPC分类号： B01D53/62 , B01D53/14 , C01B32/50
CPC分类号： B01D53/1425 , B01D53/1475 , Y02C10/04 , Y02C10/06
摘要： The fumes flowing in through line 1 are contacted in column C1 with a solvent, at low vapour pressure, absorbing the carbon dioxide. The solvent laden with carbon dioxide is regenerated by distillation in column C2. In order to improve the regeneration operation, a gas is injected through line 11 into column C2 so that this gas carries along the carbon dioxide contained in the solvent. The carbon dioxide-rich gaseous effluent obtained at the top of column C2 can be liquefied by compression and cooling, then stored in surge tank R, which allows its transportation and possibly underground sequestration.
摘要翻译：通过管线1流动的烟气在塔C 1中与溶剂在低蒸气压下接触，吸收二氧化碳。用二氧化碳负载的溶剂通过柱C 2中的蒸馏再生。为了改善再生操作，将气体通过管线11注入塔C 2，使得该气体沿着溶剂中所含的二氧化碳携带。在塔C 2顶部获得的富含二氧化碳的气态流出液可以通过压缩和冷却液化，然后储存在缓冲罐R中，这允许其运输和可能的地下封存。

2. 发明申请

US20060104877A1 Method of deacidizing a gas with a fractional regeneration absorbent solution 有权
$Method of deacidizing a gas with a fractional regeneration absorbent solution$
标题翻译：使用分级再生吸收剂溶液使气体脱酸的方法
公开(公告)号：US20060104877A1
公开(公告)日：2006-05-18
申请号：US11264040
申请日：2005-11-02
申请人： Renaud Cadours , Pierre-Louis Carrette , Pierre Boucot , Pascal Mougin
发明人： Renaud Cadours , Pierre-Louis Carrette , Pierre Boucot , Pascal Mougin
IPC分类号： B01D53/40
CPC分类号： C10L3/10 , B01D53/48 , B01D53/62 , B01D53/75 , Y02C10/04 , Y02C10/06
摘要： The gaseous effluent flowing in through line 1 is contacted in absorption zone ZA with the liquid absorbent solution flowing in through line 9. The gaseous effluent depleted in acid compounds is discharged through line 2. The absorbent solution laden with acid compounds is discharged through line 3. The absorbent solution once laden with acid compounds comprises two phases: a first phase poor in acid compounds and a second phase rich in acid compounds. The two phases are separated in zone ZS. The first phase is recycled through lines 5 and 9 to absorption zone ZA. The second phase is fed through line 4 into regeneration zone ZR. In zone ZR, the acid compounds are separated from the absorbent solution. The acid compounds are discharged through line 7. The regenerated absorbent solution is recycled through lines 6 and 9 to zone ZA.
摘要翻译：通过管线1流动的气态流出物在吸收区ZA中与液体吸收剂溶液通过管线9流动。通过管线2排出贫酸化合物的气态流出物。载有酸性化合物的吸收剂溶液通过管线3排出一旦载有酸性化合物的吸收剂溶液包含两相：第一相酸性化合物不良，第二相富含酸化合物。两相在区域ZS中分离。第一阶段通过管线5和9再循环到吸收区ZA。第二相通过管线4进入再生区ZR。在区域ZR中，酸性化合物与吸收剂溶液分离。酸化合物通过管线7排出。再生的吸收剂溶液通过管线6和9再循环到区域ZA。

3. 发明授权

US07419646B2 Method of deacidizing a gas with a fractional regeneration absorbent solution 有权
$Method of deacidizing a gas with a fractional regeneration absorbent solution$
标题翻译：使用分级再生吸收剂溶液使气体脱酸的方法
公开(公告)号：US07419646B2
公开(公告)日：2008-09-02
申请号：US11264040
申请日：2005-11-02
申请人： Renaud Cadours , Pierre-Louis Carrette , Pierre Boucot , Pascal Mougin
发明人： Renaud Cadours , Pierre-Louis Carrette , Pierre Boucot , Pascal Mougin
IPC分类号： B01D53/40 , B01D53/48 , B01D53/50 , B01D53/52 , B01D53/62
CPC分类号： C10L3/10 , B01D53/48 , B01D53/62 , B01D53/75 , Y02C10/04 , Y02C10/06
摘要： The gaseous effluent flowing in through line 1 is contacted in absorption zone ZA with the liquid absorbent solution flowing in through line 9. The gaseous effluent depleted in acid compounds is discharged through line 2. The absorbent solution laden with acid compounds is discharged through line 3. The absorbent solution once laden with acid compounds comprises two phases: a first phase poor in acid compounds and a second phase rich in acid compounds. The two phases are separated in zone ZS. The first phase is recycled through lines 5 and 9 to absorption zone ZA. The second phase is fed through line 4 into regeneration zone ZR. In zone ZR, the acid compounds are separated from the absorbent solution. The acid compounds are discharged through line 7. The regenerated absorbent solution is recycled through lines 6 and 9 to zone ZA.
摘要翻译：通过管线1流动的气态流出物在吸收区ZA中与液体吸收剂溶液通过管线9流动。通过管线2排出贫酸化合物的气态流出物。载有酸性化合物的吸收剂溶液通过管线3排出一旦载有酸性化合物的吸收剂溶液包含两相：第一相酸性化合物不良，第二相富含酸化合物。两相在区域ZS中分离。第一阶段通过管线5和9再循环到吸收区ZA。第二相通过管线4进入再生区ZR。在区域ZR中，酸性化合物与吸收剂溶液分离。酸化合物通过管线7排出。再生的吸收剂溶液通过管线6和9再循环到区域ZA。

4. 发明授权

US07985331B2 Method for eliminating the carbonyl sulfide contained in a liquid hydrocarbon stream 有权
标题翻译：消除液态烃流中所含羰基硫化物的方法
公开(公告)号：US07985331B2
公开(公告)日：2011-07-26
申请号：US11483742
申请日：2006-07-11
申请人： Arnaud Baudot , Renaud Cadours , Raphaël Huyghe , Elsa Jolimaitre , Pascal Mougin , Eszter Toth
发明人： Arnaud Baudot , Renaud Cadours , Raphaël Huyghe , Elsa Jolimaitre , Pascal Mougin , Eszter Toth
IPC分类号： C10G45/00 , B01J19/00 , B01D69/00
CPC分类号： C10L3/10 , B01D61/246 , C10G19/02 , C10G29/20 , C10G31/11 , C10G53/12 , C10L3/102
摘要： The liquid hydrocarbon stream including COS is introduced via line 1 into membrane contactor CM to be placed in contact, through membrane M, with the aqueous alkanolamine solution arriving via line 3. The COS contained in the hydrocarbon stream is absorbed by the aqueous alkanolamine solution. The liquid hydrocarbons from which the COS has been removed are evacuated from CM via line 2. The aqueous solution containing COS is sent via line 4 to zone R to be regenerated. The compounds released during regeneration, particularly COS and COS-derived products, are evacuated from zone R via line 5. The regenerated aqueous alkanolamine solution is recycled via line 3 into membrane contactor CM.
摘要翻译：包括COS的液态烃流通过管线1引入膜接触器CM中，通过膜M与烷基胺胺水溶液通过管线3到达。包含在烃流中的COS被链烷醇胺水溶液吸收。已经从中除去COS的液体烃通过管线2从CM排出。含有COS的水溶液通过管线4送到区R以再生。在再生期间释放的化合物，特别是COS和COS衍生产物通过管线5从区域R排出。再生的链烷醇胺水溶液通过管线3再循环到膜接触器CM中。

5. 发明申请

US20070039854A1 Method for eliminating the carbonyl sulfide contained in a liquid hydrocarbon stream 有权
标题翻译：消除液态烃流中所含羰基硫化物的方法
公开(公告)号：US20070039854A1
公开(公告)日：2007-02-22
申请号：US11483742
申请日：2006-07-11
申请人： Arnaud Baudot , Renaud Cadours , Raphael Huyghe , Elsa Jolimaitre , Pascal Mougin , Eszter Toth
发明人： Arnaud Baudot , Renaud Cadours , Raphael Huyghe , Elsa Jolimaitre , Pascal Mougin , Eszter Toth
IPC分类号： C10G45/00 , B01J19/00 , B01D69/00
CPC分类号： C10L3/10 , B01D61/246 , C10G19/02 , C10G29/20 , C10G31/11 , C10G53/12 , C10L3/102
摘要： The liquid hydrocarbon stream including COS is introduced via line 1 into membrane contactor CM to be placed in contact, through membrane M, with the aqueous alkanolamine solution arriving via line 3. The COS contained in the hydrocarbon stream is absorbed by the aqueous alkanolamine solution. The liquid hydrocarbons from which the COS has been removed are evacuated from CM via line 2. The aqueous solution containing COS is sent via line 4 to zone R to be regenerated. The compounds released during regeneration, particularly COS and COS-derived products, are evacuated from zone R via line 5. The regenerated aqueous alkanolamine solution is recycled via line 3 into membrane contactor CM.
摘要翻译：包括COS的液态烃流通过管线1引入膜接触器CM中，通过膜M与烷基胺胺水溶液经由管线3到达接触。包含在烃流中的COS被链烷醇胺水溶液吸收。已经从其中除去COS的液体烃通过管线2从CM排出。含有COS的水溶液通过管线4送至区R以再生。在再生期间释放的化合物，特别是COS和COS衍生产物，经由管线5从区域R排出。再生的链烷醇胺水溶液通过管线3再循环到膜接触器CM中。

6. 发明授权

US06666908B2 Process for deacidizing a gas with washing of the hydrocarbons desorbed upon regeneration of the solvent 有权
公开(公告)号：US06666908B2
公开(公告)日：2003-12-23
申请号：US10057895
申请日：2002-01-29
申请人： Renaud Cadours , Fabrice Lecomte , Pascal Mougin
发明人： Renaud Cadours , Fabrice Lecomte , Pascal Mougin
IPC分类号： B01D5314
CPC分类号： C10L3/10 , B01D53/1462 , B01D53/1487 , C10L3/102
摘要： Within the scope of a process using two absorption sections for treating a natural gas containing CO2 and/or H2S, as well as mercaptans, COS and/or CS2, the present invention aims to wash the gaseous hydrocarbons desorbed upon expansion of the solvent from the first absorption section with the solvent from the second absorption section.

7. 发明申请

US20090127164A9 Method for eliminating the carbonyl sulfide contained in a liquid hydrocarbon stream 有权
标题翻译：消除液态烃流中所含羰基硫化物的方法
公开(公告)号：US20090127164A9
公开(公告)日：2009-05-21
申请号：US11483742
申请日：2006-07-11
申请人： Arnaud Baudot , Renaud Cadours , Raphael Huyghe , Elsa Jolimaitre , Pascal Mougin , Eszter Toth
发明人： Arnaud Baudot , Renaud Cadours , Raphael Huyghe , Elsa Jolimaitre , Pascal Mougin , Eszter Toth
IPC分类号： C10G45/00 , B01J19/00 , B01D69/00
CPC分类号： C10L3/10 , B01D61/246 , C10G19/02 , C10G29/20 , C10G31/11 , C10G53/12 , C10L3/102
摘要： The liquid hydrocarbon stream including COS is introduced via line 1 into membrane contactor CM to be placed in contact, through membrane M, with the aqueous alkanolamine solution arriving via line 3. The COS contained in the hydrocarbon stream is absorbed by the aqueous alkanolamine solution. The liquid hydrocarbons from which the COS has been removed are evacuated from CM via line 2. The aqueous solution containing COS is sent via line 4 to zone R to be regenerated. The compounds released during regeneration, particularly COS and COS-derived products, are evacuated from zone R via line 5. The regenerated aqueous alkanolamine solution is recycled via line 3 into membrane contactor CM.
摘要翻译：包括COS的液态烃流通过管线1引入膜接触器CM中，通过膜M与烷基胺胺水溶液通过管线3到达。包含在烃流中的COS被链烷醇胺水溶液吸收。已经从中除去COS的液体烃通过管线2从CM排出。含有COS的水溶液通过管线4送到区R以再生。在再生期间释放的化合物，特别是COS和COS衍生产物通过管线5从区域R排出。再生的链烷醇胺水溶液通过管线3再循环到膜接触器CM中。

8. 发明授权

US06690453B2 Method and device for predicting the flocculation threshold of asphaltenes contained in hydrocarbon mixtures 失效
标题翻译：用于预测含烃混合物中沥青质絮凝阈值的方法和装置
公开(公告)号：US06690453B2
公开(公告)日：2004-02-10
申请号：US10067232
申请日：2002-02-07
申请人： Pascal Mougin
发明人： Pascal Mougin
IPC分类号： G01N3326
CPC分类号： G01N21/41 , G01N33/28 , G01N33/42
摘要： Method and device for predicting the flocculation threshold of asphaltenes contained in hydrocarbon mixtures. The method comprises the following stages: determining the refraction index (nA) of several asphaltenes used as reference asphaltenes; determining experimentally, for predetermined thermodynamic conditions, the variation of solubility index (&dgr;) in connection with the refraction index of hydrocarbon constituents including light hydrocarbons and reference asphaltenes; deducing therefrom a correlation relation modelling this variation of solubility index (&dgr;). These preliminary operations being performed, refraction index (nA) of the asphaltenes of the hydrocarbon mixture is determined under the same thermodynamic conditions and by reference to said correlation relation, solubility index (&dgr;) of the asphaltenes of said mixture is deduced therefrom; and from the solubility index of the asphaltenes of said mixture and from a thermodynamic equilibrium model, the flocculation threshold thereof is directly predicted. Applications: fast laboratory determination of asphaltene flocculation risks likely to hinder production and transport of crudes so as to quickly implement solutions intended to prevent them.
摘要翻译：用于预测烃类混合物中沥青质絮凝阈值的方法和装置。该方法包括以下阶段：确定用作参考沥青质的几种沥青质的折射率（nA）;实验确定，对于预定的热力学条件，溶解度指数的变化（δ），与碳氢化合物成分（包括轻质烃类和参考沥青质）的折射指数相关;推导出这种溶度指数（delta）变化的相关关系。所进行的这些初步操作，沥青质的折射率（nA）烃混合物在相同的热力学条件下并通过参考所述相关关系确定，从而推导出所述混合物的沥青质的溶解度指数（delta）; 并从所述混合物的沥青质的溶解度指数和热力学平衡模型中直接预测其絮凝阈值。应用：快速实验室测定沥青质絮凝风险可能会阻碍原油的生产和运输，以便快速实施旨在防止他们

9. 发明授权

US06318149B1 Method and device for determining the joule-thomson coefficient of a fluid 失效
标题翻译：用于确定流体焦耳系数的方法和装置
公开(公告)号：US06318149B1
公开(公告)日：2001-11-20
申请号：US09550203
申请日：2000-04-17
申请人： Pascal Mougin , Roxane Peumery , Gérard Moracchini , José Sanchez
发明人： Pascal Mougin , Roxane Peumery , Gérard Moracchini , José Sanchez
IPC分类号： G01N2500
CPC分类号： G01N33/2823
摘要： The invention is a method for determining the Joule-Thomson coefficient of a fluid, expressing the temperature variation in relation to a pressure variation thereof. The fluid is injected at a determined injection temperature into a thin tube (8) (preferably a capillary tube in order to obtain a high pressure drop with reasonable flow rates) which contains a temperature detector (TC1) leading to a pressure drop for the fluid. The temperature variation of the fluid in relation to the injection temperature is measured by means of this temperature detector. The pressure drop undergone by the fluid in tube (8), due to the presence of this temperature detector, is also measured and the Joule-Thomson coefficient is calculated by combination of measurements of the pressure drop and of the temperature variation of the fluid. The method can be applied notably in the field of hydrocarbon production, more particularly hydrocarbons coming from high-pressure and high-temperature reservoirs and in gas lines.
摘要翻译：本发明是用于确定流体的焦耳 - 汤姆逊系数的方法，其表示相对于其压力变化的温度变化。将流体以确定的注射温度注入细管（8）（优选毛细管中以获得具有合理流速的高压降），其包含导致流体压降的温度检测器（TC1）。通过该温度检测器测量流体相对于注射温度的温度变化。还测量了由于存在该温度检测器而由管（8）中的流体引起的压降，并且通过组合压降和流体温度变化的测量来计算焦耳 - 汤姆森系数。该方法可以显着地应用于烃生产领域，特别是来自高压和高温储层以及气体管线的烃。

10. 发明授权

US07343270B2 Method for modeling asphaltenes flocculation conditions in hydrocarbon-containing fluids related to a reference fluid 有权
标题翻译：用于建模与参考流体相关的含烃流体中沥青质絮凝条件的方法
公开(公告)号：US07343270B2
公开(公告)日：2008-03-11
申请号：US10376303
申请日：2003-03-03
申请人： Pascal Mougin , Annabelle Pina , Sophie Jullian
发明人： Pascal Mougin , Annabelle Pina , Sophie Jullian
IPC分类号： G06F17/10
CPC分类号： G01N33/28 , G01N33/2823 , G01N33/2835
摘要： Method for modeling the flocculation conditions of hydrocarbon-containing fluids under pressure, related to a reference fluid. The asphaltenic properties are modeled from the results of an experimental study of a single asphaltenic reference fluid and by means of homothetic transformation laws. These reduced data allow to deal with asphaltenes flocculation in an industrial simulator working according to a simplified model. It is then possible to predict the amounts of asphaltenes that will flocculate in a reservoir or in a reactor during development, considering the variable pressure and composition conditions. Application: optimization of the development conditions of reservoirs or of an industrial reactor in which asphaltenic fluids undergo expansions.
摘要翻译：对与参考流体有关的压力下的含烃流体的絮凝条件建模的方法。沥青性质是从单一沥青质参考流体的实验研究结果和借助于同质转化定律得出的。这些减少的数据允许处理根据简化模型工作的工业模拟器中的沥青质絮凝。因此，考虑到可变压力和组成条件，可以预测在开发过程中在储层或反应器中絮凝的沥青质的量。应用：优化储层或沥青液经历膨胀的工业反应堆的开发条件。

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