-
公开(公告)号：US4566961A
公开(公告)日：1986-01-28
申请号：US668280
申请日：1984-10-18
Applicant: Henri Diaz , Pierre Jorgensen , Pierre Vernet
Inventor： Henri Diaz , Pierre Jorgensen , Pierre Vernet
Abstract: Electric arc conversion process in which C.sub.1 -C.sub.4 alkane is brought into contact with an electric arc and higher molecular weight carbonaceous material is brought into contact with the hot gas derived from the C.sub.1 -C.sub.4 hydrocarbon in the vicinity of the arc.
Abstract translation: PCT No.PCT / GB84 / 00067 Sec。 371日期1984年10月18日 102（e）日期1984年10月18日PCT提交1984年3月1日PCT公布。 出版物WO84 / 03515 日期：1984年9月13日。电弧转换法，其中C1-C4烷烃与电弧接触，较高分子量的碳质材料与来自C 1 -C 4烃附近的热气体接触 电弧。
-
2.发明申请DEEP CONVERSION COMBINING THE DEMETALLIZATION AND THE CONVERSION OF CRUDES, RESIDUES OR HEAVY OILS INTO LIGHT LIQUIDS WITH PURE OR IMPURE OXYGENATED COMPOUNDS 有权深度转换结合使用纯化或不纯氧化的化合物将沉淀物转化为沉淀物或残留物或重油转化成轻液体公开(公告)号：US20100260649A1
公开(公告)日：2010-10-14
申请号：US12824362
申请日：2010-06-28
Applicant: Pierre Jorgensen
Inventor： Pierre Jorgensen
IPC: B01J19/00
CPC classification number: C10G21/02 , B01J4/001 , B01J2219/00006 , C10G1/02 , C10G9/00 , C10G9/36 , C10G27/14 , C10G33/06 , C10G55/04 , C10G2300/107 , C10G2300/1077 , C10G2300/201 , C10G2300/205 , C10G2300/807 , Y10S585/922 , Y10S585/923
Abstract: A process for the conversion of hydrocarbons that are solid or have a high boiling temperature and may be laden with metals, sulfur or sediments, into liquids (gasolines, gas oil, fuels) with the help of a jet of gas properly superheated between 600 and 800° C. The process comprises preheating a feed 5 in a heater 8 to a temperature below the selected temperature of a reactor 10. This feed is injected by injectors 4 into the empty reactor 10 (i.e., without catalyst.) The feed is treated with a jet of gas or superheated steam from superheater 2 to activate the feed. The activated products in the feed are allowed to stabilize at the selected temperature and at a selected pressure in the reactor and are then run through a series of extractors 13 to separate heavy and light hydrocarbons and to demetallize the feed. Useful products appearing in the form of water/hydrocarbon emulsions are generally demulsified in emulsion breaker 16 to form water laden with different impurities. The light phase containing the final hydrocarbons is heated in heater 98 and is separated into cuts of conventional products, according to the demand for refining by an extractor 18 similar to 13.
Abstract translation: 一种将固体或具有高沸点温度的烃转化成金属，硫或沉淀物的烃转化为液体（汽油，瓦斯油，燃料）的方法，借助于600〜 该方法包括将加热器8中的进料5预热到低于反应器10的选定温度的温度。该进料通过喷射器4注入空反应器10（即，不含催化剂）。进料被处理 用过热器2的气体喷射或过热蒸汽激活进料。 允许进料中的活化产物在反应器中选定的温度和选择的压力下稳定，然后通过一系列萃取器13分离重质烃和轻质烃并使进料脱金属。 以水/烃乳液形式出现的有用产品通常在破乳剂16中破乳以形成含有不同杂质的水。 含有最终碳氢化合物的轻相在加热器98中加热，并根据类似于13的萃取器18的精炼需求分离成常规产品的切割。
-
3.发明申请Deep conversion combining the demetallization and the conversion of crudes, residues or heavy oils into light liquids with pure or impure oxygenated compounds 审中-公开深层转换将原油，残渣或重油转化为纯化或不纯氧化化合物的轻质液体脱金属公开(公告)号：US20050276735A1
公开(公告)日：2005-12-15
申请号：US11130988
申请日：2005-05-17
Applicant: Pierre Jorgensen
Inventor： Pierre Jorgensen
IPC: B01J4/00 , B01J8/04 , B01J10/00 , C10G1/02 , C10G9/00 , C10G9/36 , C10G21/02 , C10G27/14 , C10G33/06 , C10G33/08 , C10G55/04
CPC classification number: C10G21/02 , B01J4/001 , B01J2219/00006 , C10G1/02 , C10G9/00 , C10G9/36 , C10G27/14 , C10G33/06 , C10G55/04 , C10G2300/107 , C10G2300/1077 , C10G2300/201 , C10G2300/205 , C10G2300/807 , Y10S585/922 , Y10S585/923
Abstract: A process for the conversion of hydrocarbons that are solid or have a high boiling temperature and may be laden with metals, sulfur or sediments, into liquids (gasolines, gas oil, fuels) with the help of a jet of gas properly superheated between 600 and 800° C. The process comprises preheating a feed 5 in a heater 8 to a temperature below the selected temperature of a reactor 10. This feed is injected by injectors 4 into the empty reactor 10 (i.e., without catalyst.) The feed is treated with a jet of gas or superheated steam from superheater 2 to activate the feed. The activated products in the feed are allowed to stabilize at the selected temperature and at a selected pressure in the reactor and are then run through a series of extractors 13 to separate heavy and light hydrocarbons and to demetallize the feed. Useful products appearing in the form of water/hydrocarbon emulsions are generally demulsified in emulsion breaker 16 to form water laden with different impurities. The light phase containing the final hydrocarbons is heated in heater 98 and is separated into cuts of conventional products, according to the demand for refining by an extractor 18 similar to 13.
Abstract translation: 一种将固体或具有高沸点温度的烃转化成金属，硫或沉淀物的烃转化为液体（汽油，瓦斯油，燃料）的方法，借助于600〜 800℃。该方法包括将加热器8中的进料5预热到低于反应器10的选定温度的温度。 该进料通过喷射器4注入空的反应器10（即，不含催化剂）。用来自过热器2的气体或过热蒸汽进行进料处理以活化进料。 允许进料中的活化产物在反应器中选定的温度和选择的压力下稳定，然后通过一系列萃取器13分离重质烃和轻质烃并使进料脱金属。 以水/烃乳液形式出现的有用产品通常在破乳剂16中破乳以形成含有不同杂质的水。 含有最终碳氢化合物的轻相在加热器98中加热，并根据类似于13的萃取器18的精炼需求分离成常规产品的切割。
-
Patent Agency Ranking
4.发明申请Deep conversion combining the demetallization and the conversion of crudes, residues or heavy oils into light liquids with pure or impure oxygenated compounds 审中-公开深层转换将原油，残渣或重油转化为纯化或不纯氧化化合物的轻质液体脱金属公开(公告)号：US20120055847A1
公开(公告)日：2012-03-08
申请号：US13136042
申请日：2011-07-21
Applicant: Pierre Jorgensen
Inventor： Pierre Jorgensen
CPC classification number: C10G21/02 , B01J4/001 , B01J2219/00006 , C10G1/02 , C10G9/00 , C10G9/36 , C10G27/14 , C10G33/06 , C10G55/04 , C10G2300/107 , C10G2300/1077 , C10G2300/201 , C10G2300/205 , C10G2300/807 , Y10S585/922 , Y10S585/923
Abstract: A process for the conversion of hydrocarbons that are solid or have a high boiling temperature and may be laden with metals, sulfur or sediments, into liquids (gasolines, gas oil, fuels) with the help of a jet of gas properly superheated between 600 and 800° C. The process comprises preheating a feed 5 in a heater 8 to a temperature below the selected temperature of a reactor 10. This feed is injected by injectors 4 into the empty reactor 10 (i.e., without catalyst.) The feed is treated with a jet of gas or superheated steam from superheater 2 to activate the feed. The activated products in the feed are allowed to stabilize at the selected temperature and at a selected pressure in the reactor and are then run through a series of extractors 13 to separate heavy and light hydrocarbons and to demetallize the feed. Useful products appearing in the form of water/hydrocarbon emulsions are generally demulsified in emulsion breaker 16 to form water laden with different impurities. The light phase containing the final hydrocarbons is heated in heater 98 and is separated into cuts of conventional products, according to the demand for refining by an extractor 18 similar to 13.
Abstract translation: 一种将固体或具有高沸点温度的烃转化成金属，硫或沉淀物的烃转化成液体（汽油，瓦斯油，燃料）的方法，借助于600〜 该方法包括将加热器8中的进料5预热到低于反应器10的选定温度的温度。该进料通过喷射器4注入空反应器10（即，不含催化剂）。进料被处理 用过热器2的气体喷射或过热蒸汽激活进料。 允许进料中的活化产物在反应器中选定的温度和选择的压力下稳定，然后通过一系列萃取器13分离重质烃和轻质烃并使进料脱金属。 以水/烃乳液形式出现的有用产品通常在破乳剂16中破乳以形成含有不同杂质的水。 含有最终碳氢化合物的轻相在加热器98中加热，并根据类似于13的萃取器18的精炼需求分离成常规产品的切割。
-
5.发明授权公开(公告)号：US07967954B2
公开(公告)日：2011-06-28
申请号：US12824362
申请日：2010-06-28
Applicant: Pierre Jorgensen
Inventor： Pierre Jorgensen
CPC classification number: C10G21/02 , B01J4/001 , B01J2219/00006 , C10G1/02 , C10G9/00 , C10G9/36 , C10G27/14 , C10G33/06 , C10G55/04 , C10G2300/107 , C10G2300/1077 , C10G2300/201 , C10G2300/205 , C10G2300/807 , Y10S585/922 , Y10S585/923
Abstract: A process for the conversion of hydrocarbons that are solid or have a high boiling temperature and may be laden with metals, sulfur or sediments, into liquids (gasolines, gas oil, fuels) with the help of a jet of gas properly superheated between 600 and 800° C. The process comprises preheating a feed 5 in a heater 8 to a temperature below the selected temperature of a reactor 10. This feed is injected by injectors 4 into the empty reactor 10 (i.e., without catalyst.) The feed is treated with a jet of gas or superheated steam from superheater 2 to activate the feed. The activated products in the feed are allowed to stabilize at the selected temperature and at a selected pressure in the reactor and are then run through a series of extractors 13 to separate heavy and light hydrocarbons and to demetallize the feed. Useful products appearing in the form of water/hydrocarbon emulsions are generally demulsified in emulsion breaker 16 to form water laden with different impurities. The light phase containing the final hydrocarbons is heated in heater 98 and is separated into cuts of conventional products, according to the demand for refining by an extractor 18 similar to 13.
Abstract translation: 一种将固体或具有高沸点温度的烃转化成金属，硫或沉淀物的烃转化为液体（汽油，瓦斯油，燃料）的方法，借助于600〜 该方法包括将加热器8中的进料5预热到低于反应器10的选定温度的温度。该进料通过喷射器4注入空反应器10（即，不含催化剂）。进料被处理 用过热器2的气体喷射或过热蒸汽激活进料。 允许进料中的活化产物在反应器中选定的温度和选择的压力下稳定，然后通过一系列萃取器13分离重质烃和轻质烃并使进料脱金属。 以水/烃乳液形式出现的有用产品通常在破乳剂16中破乳以形成含有不同杂质的水。 含有最终碳氢化合物的轻相在加热器98中加热，并根据类似于13的萃取器18的精炼需求分离成常规产品的切割。
-
6.发明授权公开(公告)号：US06989091B2
公开(公告)日：2006-01-24
申请号：US10428212
申请日：2003-05-02
Applicant: Pierre Jorgensen
Inventor： Pierre Jorgensen
IPC: C10G9/00
CPC classification number: C10G21/02 , B01J4/001 , B01J2219/00006 , C10G1/02 , C10G9/00 , C10G9/36 , C10G27/14 , C10G33/06 , C10G55/04 , C10G2300/107 , C10G2300/1077 , C10G2300/201 , C10G2300/205 , C10G2300/807 , Y10S585/922 , Y10S585/923
Abstract: A process for the conversion of hydrocarbons that are solid or have a high boiling temperature and may be laden with metals, sulfur or sediments, into liquids (gasolines, gas oil, fuels) with the help of a jet of gas properly superheated between 600 and 800° C. The process comprises preheating of feed 5 in a heater 8 to a temperature below the selected temperature of a reactor 10. This feed is injected by injectors 4 into the empty reactor 10 (i.e., without catalyst.) The feed is treated with a jet of gas or superheated steam from superheater 2 to activate the feed. The activated products in the feed are allowed to stabilize at the selected temperature and at a selected pressure in the reactor and are then run through a series of extractors 13 to separate heavy and light hydrocarbons and to demetallize the feed. Useful products appearing in the form of water/hydrogen emulsions are generally demulsified in emulsion breaker 16 to form water laden with different impurities. The light phase containing the final hydrocarbons is heated in heater 98 and is separated into cuts of conventional products, according to the demand for refining by an extractor 18 similar to 13.
Abstract translation: 一种将固体或具有高沸点温度的烃转化成金属，硫或沉淀物的烃转化为液体（汽油，瓦斯油，燃料）的方法，借助于600〜 该方法包括将加热器8中的进料5预热到低于反应器10的选定温度的温度。该进料通过喷射器4注入空的反应器10（即，不含催化剂）。进料被处理 用过热器2的气体喷射或过热蒸汽激活进料。 允许进料中的活化产物在反应器中选定的温度和选择的压力下稳定，然后通过一系列萃取器13分离重质烃和轻质烃并使进料脱金属。 以水/氢乳液形式出现的有用产品通常在破乳剂16中破乳以形成含有不同杂质的水。 含有最终碳氢化合物的轻相在加热器98中加热，并根据类似于13的萃取器18的精炼需求分离成常规产品的切割。
-
7.发明申请Deep conversion combining the demetallization and the conversion of crudes, residues or heavy oils into light liquids with pure or impure oxygenated compounds 审中-公开深层转换将原油，残渣或重油转化为纯化或不纯氧化化合物的轻质液体脱金属公开(公告)号：US20050211602A1
公开(公告)日：2005-09-29
申请号：US11131167
申请日：2005-05-17
Applicant: Pierre Jorgensen
Inventor： Pierre Jorgensen
IPC: B01J4/00 , B01J8/04 , B01J10/00 , C10G1/02 , C10G9/00 , C10G9/36 , C10G21/02 , C10G27/14 , C10G33/06 , C10G33/08 , C10G55/04
CPC classification number: C10G21/02 , B01J4/001 , B01J2219/00006 , C10G1/02 , C10G9/00 , C10G9/36 , C10G27/14 , C10G33/06 , C10G55/04 , C10G2300/107 , C10G2300/1077 , C10G2300/201 , C10G2300/205 , C10G2300/807 , Y10S585/922 , Y10S585/923
Abstract: A process for the conversion of hydrocarbons that are solid or have a high boiling temperature and may be laden with metals, sulfur or sediments, into liquids (gasolines, gas oil, fuels) with the help of a jet of gas pity superheated between 600 and 800° C. The process comprises preheating a feed 5 in a heater 8 to a temperature below the selected temperature of a reactor 10. This feed is injected by injectors 4 into the empty reactor 10 (i.e., without catalyst.) The feed is treated with a jet of gas or superheated stem from superheater 2 to activate the feed. The activated products in the feed are allowed to stabilize at the selected temperature and at a selected pressure in the reactor and are then run through a series of extractors 13 to separate heavy and light hydrocarbons and to demetallize the feed. Useful products appearing in the form of water/hydrocarbon emulsions are generally demulsified in emulsion breaker 16 to form water laden with different impurities. The light phase containing the final hydrocarbons is heated in heater 98 and is separated into cuts of conventional products, according to the demand for refining by an extractor 18 similar to 13.
Abstract translation: 通过在600和600之间过热的燃气喷射，将固体或具有高沸点温度的烃转化成金属，硫或沉淀物的液体（汽油，瓦斯油，燃料）的方法 该方法包括将加热器8中的进料5预热到低于反应器10的选定温度的温度。该进料通过喷射器4注入空反应器10（即，不含催化剂）。进料被处理 用过热器2的气体喷射或过热茎激活饲料。 允许进料中的活化产物在反应器中选定的温度和选择的压力下稳定，然后通过一系列萃取器13分离重质烃和轻质烃并使进料脱金属。 以水/烃乳液形式出现的有用产品通常在破乳剂16中破乳以形成含有不同杂质的水。 含有最终碳氢化合物的轻相在加热器98中加热，并根据类似于13的萃取器18的精炼需求分离成常规产品的切割。
-
公开(公告)号：US4509326A
公开(公告)日：1985-04-09
申请号：US404360
申请日：1982-08-02
Applicant: Pierre Jorgensen
Inventor： Pierre Jorgensen
CPC classification number: F01K23/064
Abstract: Energy is extracted from hot dust-laden gases by a process in which the hot gases, before being cooled or purified, are used to generate steam in a boiler. The solid particles are then removed from the gases which are then supplied to a turbine.
Abstract translation: 通过这样的方法从热的含尘气体中提取能量，其中在冷却或纯化之前，热气体在锅炉中产生蒸汽。 然后将固体颗粒从气体中除去，然后将其提供给涡轮机。
-
-
-
-
-
-
-
Search Results
8
records
(took 0.017 seconds)
