Deep conversion combining the demetallization and the conversion of crudes, residues or heavy oils into light liquids with pure or impure oxygenated compounds
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 DEG 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). <IMAGE>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 DEG 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). <IMAGE>
Term
Term ended
Projected expiry passed 7 October 2019, 7 years ago.
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- Projected expiry
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45 members in 25 offices
Priority claims11
| Document | Office | Kind | Date |
|---|---|---|---|
| 9812983 | France | A | |
| 9812983 | France | A | |
| 40593499 | United States of America | A | |
| 40593499 | United States of America | A | |
| 9923325 | United States of America | W | |
| 9923325 | United States of America | W | |
| 989812983 | – | – | – |
| 99405934 | – | – | – |
| FR19980012983 | – | – | – |
| US19990405934 | – | – | – |
| WO1999US23325 | – | – | – |
Members45
| Document | Office | Kind | |
|---|---|---|---|
| CA2346181A1 | Canada | A1 | |
| WO0023540A1 | World Intellectual Property Organization (WIPO) | A1 | |
| FR2785289A1 | France | A1 | |
| AU6418599A | Australia | A | |
| NO20011828D0 | Norway | D0 | |
| NO20011828L | Norway | L | |
| ID29093A | Indonesia | A | |
| BR9915551A | Brazil | A | |
| EP1129153A1 | European Patent Office (EPO) | A1 | |
| KR20010089310A | Republic of Korea | A | |
| EA200100399A1 | Eurasian Patent Organization (EAPO) | A1 | |
| CN1323338A | China | A | |
| PL347248A1This record | Poland | A1 | |
| EA003082B1 | Eurasian Patent Organization (EAPO) | B1 | |
| JP2003525310A | Japan | A | |
| EP1342773A2 | European Patent Office (EPO) | A2 | |
| NZ510706A | New Zealand | A | |
| EP1342773A3 | European Patent Office (EPO) | A3 | |
| US2004065589A1 | United States of America | A1 | |
| AU773537B2 | Australia | B2 | |
| UA66875C2 | Ukraine | C2 | |
| GEP20043409B | Georgia | B | |
| AP1341A | African Regional Intellectual Property Organization (ARIPO) | A | |
| US2005211602A1 | United States of America | A1 | |
| US2005276735A1 | United States of America | A1 | |
| US6989091B2 | United States of America | B2 | |
| EP1129153B1 | European Patent Office (EPO) | B1 | |
| AT324422T | Austria | T | |
| DK1129153T3 | Denmark | T3 | |
| PL191375B1 | Poland | B1 | |
| DE69931064D1 | Germany | D1 | |
| OA12680A | African Intellectual Property Organization (OAPI) | A | |
| CU23154A3 | Cuba | A3 | |
| PT1129153E | Portugal | E | |
| ES2258341T3 | Spain | T3 | |
| DE69931064T2 | Germany | T2 | |
| FR2785289B1 | France | B1 | |
| KR100684141B1 | Republic of Korea | B1 | |
| CA2346181C | Canada | C | |
| JP4080162B2 | Japan | B2 | |
| CN100489066C | China | C | |
| US2010260649A1 | United States of America | A1 | |
| US7967954B2 | United States of America | B2 | |
| BR9915551B1 | Brazil | B1 | |
| US2012055847A1 | United States of America | A1 |
1 legal event, as the office reported them to INPADOC
Events
| Event | Code | |
|---|---|---|
| Decisions on the lapse of the protection rightsLapsedLAPS | LAPS |
Numbers
- Publication, DOCDB
- 347248
- Publication, EPODOC
- PL347248
- Application
- 99347248
- Application, DOCDB
- 34724899
- Application, EPODOC
- PL19990347248
Titles
- English
- DEEP CONVERSION COMBINING THE DEMETALLIZATION AND THE CONVERSION OF CRUDES, RESIDUES OR HEAVY OILS INTO LIGHT LIQUIDS WITH PURE OR IMPURE OXYGENATED COMPOUNDS
Classification
- CPC, 16
- C10G21/02
- C10G55/04
- B01J4/001
- B01J2219/00006
- C10G1/02
- C10G9/00
- C10G9/36
- C10G27/14
- C10G33/06
- Y10S585/923
- Y10S585/922
- C10G2300/107
- C10G2300/1077
- C10G2300/201
- C10G2300/205
- C10G2300/807
- IPC, 11
- B01J4 00
- B01J8 04
- B01J10 00
- C10G1 02
- C10G9 00
- C10G9 36
- C10G21 02
- C10G27 14
- C10G33 06
- C10G33 08
- C10G55 04