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1. 发明专利

NO20042131A 未知
公开(公告)号：NO20042131A
公开(公告)日：2004-05-24
申请号：NO20042131
申请日：2004-05-24
申请人： SHELL INT RESEARCH
发明人： ANSORGE JOACHIM , NAGELVOORT ROBERT KLEIN , PUNT ADRIANUS REINIER , WIDJAJA ROY
IPC分类号： F25J1/00 , C01B3/34 , C10G2/00 , C10G5/00 , F25J1/02 , F25J3/02 , F25J3/06 , F25J3/08
CPC分类号： C10G2/32 , C01B3/34 , C01B2203/0227 , C01B2203/025 , C01B2203/043 , C01B2203/062 , C01B2203/142 , F25J1/0022 , F25J1/004 , F25J1/0229 , F25J1/0274 , F25J2205/02 , F25J2220/62

2. 发明专利

AU2002346989B2 Process for liquefying natural gas and producing hydrocarbons 未知
公开(公告)号：AU2002346989B2
公开(公告)日：2007-08-09
申请号：AU2002346989
申请日：2002-10-25
申请人： SHELL INT RESEARCH
发明人： PUNT ADRIANUS REINIER , ANSORGE JOACHIM , NAGELVOORT ROBERT KLEIN , WIDJAJA ROY
IPC分类号： F25J1/02 , C01B3/34 , C10G2/00
摘要： Process for the preparation of liquid hydrocarbons from a light hydrocarbonaceous feedstock in combination with a process for liquefying natural gas, which liquefaction process comprises the steps of: (a) passing the natural gas at liquefaction pressure through the product side of a main heat exchanger; (b) introducing cooled liquefied refrigerant at refrigerant pressure in the cold side of the main heat exchanger, allowing the cooled refrigerant to evaporate at the refrigerant pressure in the cold side of the main heat exchanger to obtain vaporous refrigerant at refrigerant pressure, and removing vaporous refrigerant from the cold side of the main heat exchanger; (c) removing the liquefied gas at liquefaction pressure from the product side of the main heat exchanger; (d) allowing the cooled liquefied gas to expand to a lower pressure to obtain expanded fluid; (e) supplying the expanded fluid to a separator vessel; (f) withdrawing from the bottom of the separator vessel a liquid product stream; (g) withdrawing from the top of the separator vessel a gaseous stream; (h) introducing the gaseous stream obtained in step (g) as feed and/or fuel in the process for the preparation of liquid hydrocarbons, which process for the preparation of hydrocarbons comprises converting a light hydrocarbonaceous feedstock into synthesis gas, followed by catalytic conversion of the synthesis gas into liquid hydrocarbons.

3. 发明专利

MY129192A PROCESS FOR LIQUEFYING NATURAL GAS AND PRODUCING HYDROCARBONS 未知
公开(公告)号：MY129192A
公开(公告)日：2007-03-30
申请号：MYPI20023992
申请日：2002-10-25
申请人： SHELL INT RESEARCH
发明人： NAGELVOORT ROBERT KLEIN , ANSORGE JOACHIM , PUNT ADRIANUS REINIER , WIDJAJA ROY
IPC分类号： F25J1/00 , C01B3/34 , C01G5/00 , C10G2/00 , F25J1/02 , F25J3/02 , F25J3/06 , F25J3/08
摘要： PROCESS FOR THE PREPARATION OF LIQUID HYDROCARBONS FROM A LIGHT HYDROCARBONACEOUS FEEDSTOCK IN COMBINATION WITH A PROCESS FOR LIQUEFYING NATURAL GAS, WHICH LIQUEFACTION PROCESS COMPRISES THE STEPS OF: (A) PASSING THE NATURAL GAS AT LIQUEFACTION PRESSURE THROUGH THE PRODUCT SIDE OF A MAIN HEAT EXCHANGER; (B) INTRODUCING COOLED LIQUEFIED REFRIGERANT AT REFRIGERANT PRESSURE IN THE COLD SIDE OF THE MAIN HEAT EXCHANGER, ALLOWING THE COOLED REFRIGERANT TO EVAPORATE AT THE REFRIGERANT PRESSURE IN THE COLD SIDE OF THE MAIN HEAT EXCHANGER TO OBTAIN VAPOROUS REFRIGERANT AT REFRIGERANT PRESSURE, AND REMOVING VAPOROUS REFRIGERANT FROM THE COLD SIDE OF THE MAIN HEAT EXCHANGER; (C) REMOVING THE LIQUEFIED GAS AT LIQUEFACTION PRESSURE FROM THE PRODUCT SIDE OF THE MAIN HEAT EXCHANGER; (D) ALLOWING THE COOLED LIQUEFIED GAS TO EXPAND TO A LOWER PRESSURE TO OBTAIN EXPANDED FLUID; (E) SUPPLYING THE EXPANDED FLUID TO A SEPARATOR VESSEL; (F) WITHDRAWING FROM THE BOTTOM OF THE SEPARATOR VESSEL A LIQUID PRODUCT STREAM; (G) WITHDRAWING FROM THE TOP OF THE SEPARATOR VESSEL A GASEOUS STREAM; (H) INTRODUCING THE GASEOUS STREAM OBTAINED IN STEP (G) AS FEED AND/OR FUEL IN THE PROCESS FOR THE PREPARATION OF LIQUID HYDROCARBONS, WHICH PROCESS FOR THE PREPARATION OF HYDROCARBONS COMPRISES CONVERTING A LIGHT HYDROCARBONACEOUS FEEDSTOCK INTO SYNTHESIS GAS, FOLLOWED BY CATALYTIC CONVERSION OF THE SYNTHESIS GAS INTO LIQUID HYDROCARBONS.

4. 发明专利

BR0213515A 未知
公开(公告)号：BR0213515A
公开(公告)日：2004-11-16
申请号：BR0213515
申请日：2002-10-25
申请人： SHELL INT RESEARCH
发明人： ANSORGE JOACHIM , NAGELVOORT ROBERT KLEIN , PUNT ADRIANUS REINIER , WIDJAJA ROY
IPC分类号： C01B3/34 , C10G2/00 , F25J1/02 , F25J1/00 , F25J3/02 , F25J3/06 , F25J3/08 , C10G5/00
摘要： Process for the preparation of liquid hydrocarbons from a light hydrocarbonaceous feedstock in combination with a process for liquefying natural gas, which liquefaction process comprises the steps of: (a) passing the natural gas at liquefaction pressure through the product side of a main heat exchanger; (b) introducing cooled liquefied refrigerant at refrigerant pressure in the cold side of the main heat exchanger, allowing the cooled refrigerant to evaporate at the refrigerant pressure in the cold side of the main heat exchanger to obtain vaporous refrigerant at refrigerant pressure, and removing vaporous refrigerant from the cold side of the main heat exchanger; (c) removing the liquefied gas at liquefaction pressure from the product side of the main heat exchanger; (d) allowing the cooled liquefied gas to expand to a lower pressure to obtain expanded fluid; (e) supplying the expanded fluid to a separator vessel; (f) withdrawing from the bottom of the separator vessel a liquid product stream; (g) withdrawing from the top of the separator vessel a gaseous stream; (h) introducing the gaseous stream obtained in step (g) as feed and/or fuel in the process for the preparation of liquid hydrocarbons, which process for the preparation of hydrocarbons comprises converting a light hydrocarbonaceous feedstock into synthesis gas, followed by catalytic conversion of the synthesis gas into liquid hydrocarbons.

5. 发明专利

AR036952A1 PROCEDIMIENTO PARA LICUAR GAS NATURAL Y PRODUCIR HIDROCARBUROS 未知
公开(公告)号：AR036952A1
公开(公告)日：2004-10-13
申请号：ARP020104022
申请日：2002-10-24
申请人： SHELL INT RESEARCH
发明人： ANSORGE JOACHIM , KLEIN NAGELVOORT ROBERT , PUNT ADRIANUS REINIER , WIDJAJA ROY
IPC分类号： C01B3/34 , C10G2/00 , F25J1/02 , F25J1/00 , F25J3/02 , F25J3/06 , F25J3/08 , C10G5/00
摘要： Un proceso para la preparación de hidrocarburos líquidos a partir de una materia prima de hidrocarburos ligeros en combinación con un proceso para licuar gas natural, cuyo proceso de licuefacción incluye los pasos de: 1) hacer pasar el gas natural a presión de licuefacción a través del lado del producto de un intercambiador térmico principal; 2) introducción de refrigerante licuado enfriado a presión refrigerante en el lado frío del intercambiador térmico principal, permitiendo que el refrigerante enfriado se evapore a presión refrigerante en el lado frío del intercambiador térmico principal para obtener un refrigerante vaporoso a presión refrigerante, y eliminación del refrigerante vaporoso del lado frío del intercambiador térmico principal; 3) eliminación del gas licuado a presión de licuefacción del lado del producto del intercambiador térmico principal; 4) permitir que el gas licuado refrigerado se expanda a una presión inferior para obtener fluido expandido; 5) colocar el fluido expandido en un recipiente separador; 6) retirar el fondo del recipiente separador una corriente de producto líquido; 7) retirar de la parte superior del recipiente separador una corriente gaseosa; 8) introducir en la corriente gaseosa obtenida en el paso (7) como materia prima y/o combustible en el proceso para la preparación de hidrocarburos líquidos, incluyendo dicho proceso para la preparación de hidrocarburos, la conversión de una materia prima de hidrocarburos ligeros en gas sintético, seguida por una conversión catalítica del gas sintético en hidrocarburos líquidos.

6. 发明专利

NO20042131L 未知
公开(公告)号：NO20042131L
公开(公告)日：2004-05-24
申请号：NO20042131
申请日：2004-05-24
申请人： SHELL INT RESEARCH
发明人： ANSORGE JOACHIM , NAGELVOORT ROBERT KLEIN , PUNT ADRIANUS REINIER , WIDJAJA ROY
IPC分类号： F25J1/00 , C01B3/34 , C10G2/00 , C10G5/00 , F25J1/02 , F25J3/02 , F25J3/06 , F25J3/08
摘要： Process for the preparation of liquid hydrocarbons from a light hydrocarbonaceous feedstock in combination with a process for liquefying natural gas, which liquefaction process comprises the steps of: (a) passing the natural gas at liquefaction pressure through the product side of a main heat exchanger; (b) introducing cooled liquefied refrigerant at refrigerant pressure in the cold side of the main heat exchanger, allowing the cooled refrigerant to evaporate at the refrigerant pressure in the cold side of the main heat exchanger to obtain vaporous refrigerant at refrigerant pressure, and removing vaporous refrigerant from the cold side of the main heat exchanger; (c) removing the liquefied gas at liquefaction pressure from the product side of the main heat exchanger; (d) allowing the cooled liquefied gas to expand to a lower pressure to obtain expanded fluid; (e) supplying the expanded fluid to a separator vessel; (f) withdrawing from the bottom of the separator vessel a liquid product stream; (g) withdrawing from the top of the separator vessel a gaseous stream; (h) introducing the gaseous stream obtained in step (g) as feed and/or fuel in the process for the preparation of liquid hydrocarbons, which process for the preparation of hydrocarbons comprises converting a light hydrocarbonaceous feedstock into synthesis gas, followed by catalytic conversion of the synthesis gas into liquid hydrocarbons.

7. 发明专利

NO20042131D0 未知
公开(公告)号：NO20042131D0
公开(公告)日：2004-05-24
申请号：NO20042131
申请日：2004-05-24
申请人： SHELL INT RESEARCH
发明人： ANSORGE JOACHIM , NAGELVOORT ROBERT KLEIN , PUNT ADRIANUS REINIER , WIDJAJA ROY
IPC分类号： C01B3/34 , C10G2/00 , F25J1/02 , F25J
摘要： Process for the preparation of liquid hydrocarbons from a light hydrocarbonaceous feedstock in combination with a process for liquefying natural gas, which liquefaction process comprises the steps of: (a) passing the natural gas at liquefaction pressure through the product side of a main heat exchanger; (b) introducing cooled liquefied refrigerant at refrigerant pressure in the cold side of the main heat exchanger, allowing the cooled refrigerant to evaporate at the refrigerant pressure in the cold side of the main heat exchanger to obtain vaporous refrigerant at refrigerant pressure, and removing vaporous refrigerant from the cold side of the main heat exchanger; (c) removing the liquefied gas at liquefaction pressure from the product side of the main heat exchanger; (d) allowing the cooled liquefied gas to expand to a lower pressure to obtain expanded fluid; (e) supplying the expanded fluid to a separator vessel; (f) withdrawing from the bottom of the separator vessel a liquid product stream; (g) withdrawing from the top of the separator vessel a gaseous stream; (h) introducing the gaseous stream obtained in step (g) as feed and/or fuel in the process for the preparation of liquid hydrocarbons, which process for the preparation of hydrocarbons comprises converting a light hydrocarbonaceous feedstock into synthesis gas, followed by catalytic conversion of the synthesis gas into liquid hydrocarbons.

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