公开(公告)号：EP1342773A3

公开(公告)日：2003-11-19

申请号：EP03076459.1

申请日：1999-10-07

申请人： Carbon Resources Limited

发明人： Jorgensen, Pierre

IPC分类号： C10G27/14 ,  C10G9/36

CPC分类号： 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

摘要： 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).

公开(公告)号：EP1342773A2

公开(公告)日：2003-09-10

申请号：EP03076459.1

申请日：1999-10-07

申请人： Carbon Resources Limited

发明人： Jorgensen, Pierre

IPC分类号： C10G27/14

CPC分类号： 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

摘要： 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).

摘要翻译： 一种用于烃类转化过程中确实是固体或具有高沸点温度，并且可以是负载金属，硫或沉积物，成液体（汽油，瓦斯油，燃料）与气体射流的帮助600之间适当的过热和 800℃，该方法包括在预热的加热器（8）的进料（5）到反应器（10）的选定的温度以下的温度。 该进料通过喷射器（4）到空反应器（10）注射（即，无催化剂）将进料气体的射流或从过热器过热蒸汽（2）以激活料治疗。 被激活的产品在饲料中被允许在选定的温度和在反应器中所选择的压力稳定，并且然后通过一系列提取的（13）以分离的重和轻的烃，并demetallize进料运行。 有用的产品在水/烃乳液的形式亮相的是破乳在破乳剂（16）的负载具有不同的杂质，以形成水基因集会。 轻相含有最终的烃是在加热器（98）加热，并被分离成类似于（13）常规产品，gemäß的削减通过在提取器（18），用于精炼的需求。 一种烃类转化过程中确实是固体或具有高沸点温度，并且可以是负载金属，硫或沉积物，成液体（汽油，瓦斯油，燃料）与气体射流的帮助下适当地过热 600和800℃之间，该方法包括在预热的进料（5）一个加热器（8）的反应器（10）的选定的温度以下的温度。 该进料通过喷射器（4）到空反应器（10）注射（即，无催化剂）将进料气体的射流或从过热器过热蒸汽（2）以激活料治疗。 被激活的产品在饲料中被允许在选定的温度和在反应器中所选择的压力稳定，并且然后通过一系列提取的（13）以分离的重和轻的烃，并demetallize进料运行。 有用的产品在水/烃乳液的形式亮相的是破乳在破乳剂（16）的负载具有不同的杂质，以形成水基因集会。 轻相含有最终的烃是在加热器（98）加热，并被分离成类似于（13）常规产品，gemäß的削减通过在提取器（18），用于精炼的需求。