METHOD OF CONDUCTING THERMAL CRACKING OF HIGH-VISCOSITY OIL STOCK
FIELD: petroleum processing. SUBSTANCE: method consists in mixing raw material with light hydrocarbon fractions, heating mixture in pipe furnace, and aging of mixture in reaction chamber, followed by separation of products into gas, gasoline, and cracking residue. Distinguishing feature of method is...
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| creator | RUDNEV A.P KHAJRULLIN R.N KHAJRUDINOV I.R MALYSHEVA N.JU ZAGIDULLIN R.M SITNIKOV S.A GASKAROV N.S IMASHEV U.B MINGARAEV S.S VIL'DANOV S.G SAZHINA T.I |
| description | FIELD: petroleum processing. SUBSTANCE: method consists in mixing raw material with light hydrocarbon fractions, heating mixture in pipe furnace, and aging of mixture in reaction chamber, followed by separation of products into gas, gasoline, and cracking residue. Distinguishing feature of method is that mixture is heated in pipe furnace at 455-465 C and aged in reaction chamber at 420-425 C for 4- 15 min. EFFECT: decreased viscosity of cracking residue and increased overhaul life of thermal cracking plant. 1 tbl, 7 ex |
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SUBSTANCE: method consists in mixing raw material with light hydrocarbon fractions, heating mixture in pipe furnace, and aging of mixture in reaction chamber, followed by separation of products into gas, gasoline, and cracking residue. Distinguishing feature of method is that mixture is heated in pipe furnace at 455-465 C and aged in reaction chamber at 420-425 C for 4- 15 min. EFFECT: decreased viscosity of cracking residue and increased overhaul life of thermal cracking plant. 1 tbl, 7 ex</description><edition>6</edition><language>eng</language><subject>CHEMISTRY ; CRACKING HYDROCARBON OILS ; FUELS ; LUBRICANTS ; METALLURGY ; MINERAL WAXES ; 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</subject><creationdate>1999</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19990120&DB=EPODOC&CC=RU&NR=2125078C1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19990120&DB=EPODOC&CC=RU&NR=2125078C1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>RUDNEV A.P</creatorcontrib><creatorcontrib>KHAJRULLIN R.N</creatorcontrib><creatorcontrib>KHAJRUDINOV I.R</creatorcontrib><creatorcontrib>MALYSHEVA N.JU</creatorcontrib><creatorcontrib>ZAGIDULLIN R.M</creatorcontrib><creatorcontrib>SITNIKOV S.A</creatorcontrib><creatorcontrib>GASKAROV N.S</creatorcontrib><creatorcontrib>IMASHEV U.B</creatorcontrib><creatorcontrib>MINGARAEV S.S</creatorcontrib><creatorcontrib>VIL'DANOV S.G</creatorcontrib><creatorcontrib>SAZHINA T.I</creatorcontrib><title>METHOD OF CONDUCTING THERMAL CRACKING OF HIGH-VISCOSITY OIL STOCK</title><description>FIELD: petroleum processing. SUBSTANCE: method consists in mixing raw material with light hydrocarbon fractions, heating mixture in pipe furnace, and aging of mixture in reaction chamber, followed by separation of products into gas, gasoline, and cracking residue. Distinguishing feature of method is that mixture is heated in pipe furnace at 455-465 C and aged in reaction chamber at 420-425 C for 4- 15 min. 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SUBSTANCE: method consists in mixing raw material with light hydrocarbon fractions, heating mixture in pipe furnace, and aging of mixture in reaction chamber, followed by separation of products into gas, gasoline, and cracking residue. Distinguishing feature of method is that mixture is heated in pipe furnace at 455-465 C and aged in reaction chamber at 420-425 C for 4- 15 min. EFFECT: decreased viscosity of cracking residue and increased overhaul life of thermal cracking plant. 1 tbl, 7 ex</abstract><edition>6</edition><oa>free_for_read</oa></addata></record> |
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| language | eng |
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| subjects | CHEMISTRY CRACKING HYDROCARBON OILS FUELS LUBRICANTS METALLURGY MINERAL WAXES 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 |
| title | METHOD OF CONDUCTING THERMAL CRACKING OF HIGH-VISCOSITY OIL STOCK |
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