EP 2158303 A2 20100303 - METHOD FOR PRODUCING MIDDLE DISTILLATES BY HYDROISOMERISATION AND HYDROCRACKING OF A HEAVY FRACTION FROM A FISCHER-TROPSCH EFFLUENT
Title (en)
METHOD FOR PRODUCING MIDDLE DISTILLATES BY HYDROISOMERISATION AND HYDROCRACKING OF A HEAVY FRACTION FROM A FISCHER-TROPSCH EFFLUENT
Title (de)
VERFAHREN ZUR HERSTELLUNG VON MITTELDESTILLATEN DURCH HYDROISOMERISIERUNG UND HYDROCRACKING EINES SCHWEREN TEILS AUS EINER FISCHER-TROPSCH-EFFLUENZ
Title (fr)
PROCEDE DE PRODUCTION DE DISTILLATS MOYENS PAR HYDROISOMERISATION ET HYDROCRAQUAGE D'UNE FRACTION LOURDE ISSUE D'UN EFFLUENT FISCHER-TROPSCH
Publication
Application
Priority
- FR 2008000753 W 20080603
- FR 0704224 A 20070612
Abstract (en)
[origin: WO2009004179A2] The invention relates to a method in which the paraffin effluent from a Fischer-Tropsch synthesis unit is separated in order to obtain a C5+ heavy fraction, said heavy fraction being then hydrogenated in the presence of a hydrogenation catalyst at a temperature of between 80°C and 200°C, at a global pressure of between 0.5 and 6 MPa, at an hourly volumetric rate of between 1 and 10h-1, and at a hydrogen flow rate corresponding to a volumetric hydrogen/hydrocarbon ratio of between 5 and 80 Nl/l/h, the liquid hydrogenated effluent being then contacted with a hydroisomerisation / hydrocracking catalyst without any preliminary separation step, the hydroisomerised/hydrocracked effluent being then distilled for obtaining the middle distillates and optionally oil bases.
IPC 8 full level
C10G 45/00 (2006.01); C10G 45/58 (2006.01); C10G 65/04 (2006.01)
CPC (source: EP US)
C10G 45/00 (2013.01 - EP US); C10G 45/58 (2013.01 - EP US); C10G 65/043 (2013.01 - EP US)
Citation (search report)
See references of WO 2009004179A2
Designated contracting state (EPC)
AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR
Designated extension state (EPC)
AL BA MK RS
DOCDB simple family (publication)
FR 2917419 A1 20081219; FR 2917419 B1 20141024; AU 2008270132 A1 20090108; BR PI0813815 A2 20141230; BR PI0813815 A8 20170314; CA 2689932 A1 20090108; CA 2689932 C 20160503; CN 101730732 A 20100609; CN 101730732 B 20140528; EP 2158303 A2 20100303; EP 2158303 B1 20170104; MY 157735 A 20160715; RU 2010100634 A 20110720; RU 2469069 C2 20121210; US 2010298451 A1 20101125; US 8709234 B2 20140429; WO 2009004179 A2 20090108; WO 2009004179 A3 20090219; ZA 200908037 B 20120425
DOCDB simple family (application)
FR 0704224 A 20070612; AU 2008270132 A 20080603; BR PI0813815 A 20080603; CA 2689932 A 20080603; CN 200880019675 A 20080603; EP 08805641 A 20080603; FR 2008000753 W 20080603; MY PI20095264 A 20080603; RU 2010100634 A 20080603; US 66418708 A 20080603; ZA 200908037 A 20091116