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1. (WO1997016506) SINGLE STAGE OIL REFINING PROCESS
Latest bibliographic data on file with the International Bureau

Pub. No.: WO/1997/016506 International Application No.: PCT/RU1996/000312
Publication Date: 09.05.1997 International Filing Date: 31.10.1996
Chapter 2 Demand Filed: 26.05.1997
IPC:
C10G 9/02 (2006.01)
C CHEMISTRY; METALLURGY
10
PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
G
CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
9
Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
02
in retorts
Applicants:
AGASHKOV, Vladimir Petrovich [UA/UA]; UA
KRJUCHKOV, Viktor Alexeevich [RU/RU]; RU
POPOV, Valery Timofeevich [RU/RU]; RU
SLOVETSKY, Dmitry Ippolitovich [RU/RU]; RU
SLOVETSKY, Vladimir Ippolitovich [RU/RU]; RU
Inventors:
AGASHKOV, Vladimir Petrovich; UA
KRJUCHKOV, Viktor Alexeevich; RU
POPOV, Valery Timofeevich; RU
SLOVETSKY, Dmitry Ippolitovich; RU
SLOVETSKY, Vladimir Ippolitovich; RU
Agent:
KVASHNIN, Valery Pavlovich; Sojuzpatent ul. Iliinka, 5/2 Moscow, 103735, RU
Priority Data:
9511799901.11.1995RU
Title (EN) SINGLE STAGE OIL REFINING PROCESS
(FR) PROCESSUS DE RAFFINAGE DE PETROLE EN UNE ETAPE
Abstract:
(EN) A single stage process for completely refining a heavy hydrocarbon feedstock wherein the feedstock is monotonously heated to a final temperature of about 520-580 °C at an average heating rate of at least about 5 °C/minute at atmospheric pressure, and bubbling a non-condensing, non-oxidizing gas through the feedstock at an average flow rate of at least 0.3 wt.% per minute while the feedstock is being heated, and recovering refined liquid and gaseous hydrocarbon products and coke.
(FR) Cette invention concerne un processus en une étape permettant d'effectuer le raffinage complet de matières premières consistant en des hydrocarbures lourds. La matière première est chauffée de manière continue sous pression atmosphérique et à une vitesse minimale d'environ 5° C par minute, ceci jusqu'à ce qu'elle atteigne une température finale située entre 520 et 580° C. Un gaz non oxydant et ne générant pas de condensation est ensuite introduit par barbotage dans la matière première lors du processus de chauffage de cette dernière, ceci selon un débit d'au moins 0,3 % en poids par minute. On procède enfin à la récupération des produits hydrocarbures gazeux et liquides raffinés, ainsi qu'à la récupération du coke.
Designated States: AM, AT, AU, BB, BG, BR, BY, CA, CH, CN, CZ, DE, DK, ES, FI, GB, GE, HU, JP, KE, KG, KP, KR, KZ, LK, LT, LU, LV, MD, MG, MN, MW, NO, NZ, PL, PT, RO, SD, SE, SI, SK, TJ, TT, UA, US, UZ, VN
African Regional Intellectual Property Organization (ARIPO) (KE, LS, MW, SD, SZ, UG)
Eurasian Patent Organization (AM, AZ, BY, KG, KZ, MD, RU, TJ, TM)
European Patent Office (AT, BE, CH, DE, DK, ES, FI, FR, GB, GR, IE, IT, LU, MC, NL, PT, SE)
African Intellectual Property Organization (BF, BJ, CF, CG, CI, CM, GA, GN, ML, MR, NE, SN, TD, TG)
Publication Language: English (EN)
Filing Language: English (EN)
Also published as:
AU1996075106