PL347248A1

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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45 members in 25 offices

This recordMember, by publication datePriority claim15 more offices are in the list below

Priority claims11

Priority claims
DocumentOfficeKindDate
9812983FranceA
9812983FranceA
40593499United States of AmericaA
40593499United States of AmericaA
9923325United States of AmericaW
9923325United States of AmericaW
989812983
99405934
FR19980012983
US19990405934
WO1999US23325

Members45

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CA2346181A1CanadaA1
WO0023540A1World Intellectual Property Organization (WIPO)A1
FR2785289A1FranceA1
AU6418599AAustraliaA
NO20011828D0NorwayD0
NO20011828LNorwayL
ID29093AIndonesiaA
BR9915551ABrazilA
EP1129153A1European Patent Office (EPO)A1
KR20010089310ARepublic of KoreaA
EA200100399A1Eurasian Patent Organization (EAPO)A1
CN1323338AChinaA
PL347248A1This recordPolandA1
EA003082B1Eurasian Patent Organization (EAPO)B1
JP2003525310AJapanA
EP1342773A2European Patent Office (EPO)A2
NZ510706ANew ZealandA
EP1342773A3European Patent Office (EPO)A3
US2004065589A1United States of AmericaA1
AU773537B2AustraliaB2
UA66875C2UkraineC2
GEP20043409BGeorgiaB
AP1341AAfrican Regional Intellectual Property Organization (ARIPO)A
US2005211602A1United States of AmericaA1
US2005276735A1United States of AmericaA1
US6989091B2United States of AmericaB2
EP1129153B1European Patent Office (EPO)B1
AT324422TAustriaT
DK1129153T3DenmarkT3
PL191375B1PolandB1
DE69931064D1GermanyD1
OA12680AAfrican Intellectual Property Organization (OAPI)A
CU23154A3CubaA3
PT1129153EPortugalE
ES2258341T3SpainT3
DE69931064T2GermanyT2
FR2785289B1FranceB1
KR100684141B1Republic of KoreaB1
CA2346181CCanadaC
JP4080162B2JapanB2
CN100489066CChinaC
US2010260649A1United States of AmericaA1
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BR9915551B1BrazilB1
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