METHOD FOR PREPARING POLYOLEFINIC BASES OF SYNTHETIC OILS

• Main Authors: KHANNANOV ROBERT GABDRAKHMANOVICH, DEMIDOV MIKHAIL ALEXANDROVICH, SAVCHENKO VALERY IVANOVICH, ILYASOV GABBAS LUKMANOVICH, YARULLIN RAFINAT SAMATOVICH, SHAMSUTDINOV VLADIMIR GARAFOVICH, ALDOSHIN SERGEI MIKHAILOVICH, MATKOVSKY PETR EVGENIEVICH, TROITSKY VLADIMIR NIKOLAEVICH, STARTSEVA GALINA PAVLOVA
• Format: Patent
• Language: English
• Published: 29.08.2007
• Subjects: ACYCLIC OR CARBOCYCLIC COMPOUNDS; CHEMISTRY; CRACKING HYDROCARBON OILS; FUELS; LUBRICANTS; METALLURGY; MINERAL WAXES; ORGANIC CHEMISTRY; PEAT; PETROLEUM, GAS OR COKE INDUSTRIES; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; TECHNICAL GASES CONTAINING CARBON MONOXIDE

The invention relates to a method for the preparation of the polyolefinic bases of synthetic oils by the cationic oligomerization of olefinic feedstock and can be used in the petrochemical industry. A new method for the preparation of the polyolefinic bases of synthetic oils has been developed, which comprises the steps of conditioning olefinic feedstock, preparing and dosing in a reactor, solutions and suspension of the components of a catalytic system Al(O)-HCI-TBCh, isomerizing alpha-olefins and oligomerizing higher olefins and mixtures thereof under the action of the catalytic system Al(O)-HCI-TBCh, separating spent catalyst, dividing an oligomerizate into fractions and hydrogenating the fractions separated under the action of a catalyst Pd(0.2 % w)/A120 3+NaOH. The invention provides the improvement of all steps of the method elaborated. For the corrosive activity of products to be removed, a method further comprises a step of the dechlorination of oligomerizate present chlorine-containing oligoolefins with metallic aluminum, triethyl aluminum, alcohol KOH solutions or the thermal dehydrochlorination of chlorine-containing polyolefins in the absence or presence of KOH. For improvement of method technico-economic indices owing to an increase in the yield of polyolefin target fractions having a kinetic viscosity of 2-8 cSt at 100°C, the method further comprises a step of the thermal depolymerization of restricted consumable high molecular polyolefins with a kinetic viscosity of 10-20 cSt at 100°C to target polyolefins with a kinetic viscosity of 2-8 cSt at 100°C.