METHOD OF RECOVERY OF HYDROCARBON FUEL
FIELD: petroleum processing. SUBSTANCE: petroleum rectification yields (130-160)-(260-315) C and (260-315)-(330-400) C fractions, the latter being subjected to hydrofining. Heavy fuel oil is either vacuum distilled yielding (300-400)-(480-520) C vacuum distillate and petroleum tar which is subjected...
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| creator | KARIBOV A.K LAZ'JAN N.G ZENCHENKOV A.N DEM'JANENKO E.A KHAVKIN V.A PROSFIROV V.I KURGANOV V.M IL'IN V.V GULJAEVA L.A BIRJUKOV F.I STURE N.N GNATJUK A.S |
| description | FIELD: petroleum processing. SUBSTANCE: petroleum rectification yields (130-160)-(260-315) C and (260-315)-(330-400) C fractions, the latter being subjected to hydrofining. Heavy fuel oil is either vacuum distilled yielding (300-400)-(480-520) C vacuum distillate and petroleum tar which is subjected to heat treatment, or divided into two streams one of which is subjected to heat treatment. Hydrofined fraction is mixed with vacuum distillate or heavy fuel oil and products of heat treated petroleum tar or heavy fuel oil taken in amounts 30-50, 25-65, and 5-25% of mixture mass, respectively. EFFECT: recovery of hydrocarbon fuel improved. 1 tbl
Использование: нефтепереработка. Сущность изобретения: при ректификации нефти получают фракции: (130 - 160) - (260 - 315)С и (260 - 315) - (330 - 400)С. Последнюю подвергают гидроочистке. Мазут либо подвергают вакуумной перегонке с получением вакуумного дистиллята (300 - 400) - (480 - 520)С и гудрона, который подвергают термической переработке, либо разделяют на два потока, один из которых подвергают термической переработке. Гидроочищенную фракцию смешивают с вакуумным дистиллятом или мазутом и продуктами термической переработке гудрона или мазута, взятыми в количестве соответственно 30 - 50, 25 - 65 и 5 - 25% от массы смеси. 1 табл. |
| format | Patent |
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Использование: нефтепереработка. Сущность изобретения: при ректификации нефти получают фракции: (130 - 160) - (260 - 315)С и (260 - 315) - (330 - 400)С. Последнюю подвергают гидроочистке. Мазут либо подвергают вакуумной перегонке с получением вакуумного дистиллята (300 - 400) - (480 - 520)С и гудрона, который подвергают термической переработке, либо разделяют на два потока, один из которых подвергают термической переработке. Гидроочищенную фракцию смешивают с вакуумным дистиллятом или мазутом и продуктами термической переработке гудрона или мазута, взятыми в количестве соответственно 30 - 50, 25 - 65 и 5 - 25% от массы смеси. 1 табл.</description><language>eng ; rus</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>1994</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=19940415&DB=EPODOC&CC=SU&NR=1746702A1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19940415&DB=EPODOC&CC=SU&NR=1746702A1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>KARIBOV A.K</creatorcontrib><creatorcontrib>LAZ'JAN N.G</creatorcontrib><creatorcontrib>ZENCHENKOV A.N</creatorcontrib><creatorcontrib>DEM'JANENKO E.A</creatorcontrib><creatorcontrib>KHAVKIN V.A</creatorcontrib><creatorcontrib>PROSFIROV V.I</creatorcontrib><creatorcontrib>KURGANOV V.M</creatorcontrib><creatorcontrib>IL'IN V.V</creatorcontrib><creatorcontrib>GULJAEVA L.A</creatorcontrib><creatorcontrib>BIRJUKOV F.I</creatorcontrib><creatorcontrib>STURE N.N</creatorcontrib><creatorcontrib>GNATJUK A.S</creatorcontrib><title>METHOD OF RECOVERY OF HYDROCARBON FUEL</title><description>FIELD: petroleum processing. SUBSTANCE: petroleum rectification yields (130-160)-(260-315) C and (260-315)-(330-400) C fractions, the latter being subjected to hydrofining. Heavy fuel oil is either vacuum distilled yielding (300-400)-(480-520) C vacuum distillate and petroleum tar which is subjected to heat treatment, or divided into two streams one of which is subjected to heat treatment. Hydrofined fraction is mixed with vacuum distillate or heavy fuel oil and products of heat treated petroleum tar or heavy fuel oil taken in amounts 30-50, 25-65, and 5-25% of mixture mass, respectively. EFFECT: recovery of hydrocarbon fuel improved. 1 tbl
Использование: нефтепереработка. Сущность изобретения: при ректификации нефти получают фракции: (130 - 160) - (260 - 315)С и (260 - 315) - (330 - 400)С. Последнюю подвергают гидроочистке. Мазут либо подвергают вакуумной перегонке с получением вакуумного дистиллята (300 - 400) - (480 - 520)С и гудрона, который подвергают термической переработке, либо разделяют на два потока, один из которых подвергают термической переработке. Гидроочищенную фракцию смешивают с вакуумным дистиллятом или мазутом и продуктами термической переработке гудрона или мазута, взятыми в количестве соответственно 30 - 50, 25 - 65 и 5 - 25% от массы смеси. 1 табл.</description><subject>CHEMISTRY</subject><subject>CRACKING HYDROCARBON OILS</subject><subject>FUELS</subject><subject>LUBRICANTS</subject><subject>METALLURGY</subject><subject>MINERAL WAXES</subject><subject>PEAT</subject><subject>PETROLEUM, GAS OR COKE INDUSTRIES</subject><subject>PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION</subject><subject>RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES</subject><subject>REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS</subject><subject>REFORMING OF NAPHTHA</subject><subject>TECHNICAL GASES CONTAINING CARBON MONOXIDE</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>1994</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZFDzdQ3x8HdR8HdTCHJ19g9zDYoEsT0iXYL8nR2DnPz9FNxCXX14GFjTEnOKU3mhNDeDgptriLOHbmpBfnxqcUFicmpeakl8cKihuYmZuYGRo6ExEUoAd-kjMg</recordid><startdate>19940415</startdate><enddate>19940415</enddate><creator>KARIBOV A.K</creator><creator>LAZ'JAN N.G</creator><creator>ZENCHENKOV A.N</creator><creator>DEM'JANENKO E.A</creator><creator>KHAVKIN V.A</creator><creator>PROSFIROV V.I</creator><creator>KURGANOV V.M</creator><creator>IL'IN V.V</creator><creator>GULJAEVA L.A</creator><creator>BIRJUKOV F.I</creator><creator>STURE N.N</creator><creator>GNATJUK A.S</creator><scope>EVB</scope></search><sort><creationdate>19940415</creationdate><title>METHOD OF RECOVERY OF HYDROCARBON FUEL</title><author>KARIBOV A.K ; LAZ'JAN N.G ; ZENCHENKOV A.N ; DEM'JANENKO E.A ; KHAVKIN V.A ; PROSFIROV V.I ; KURGANOV V.M ; IL'IN V.V ; GULJAEVA L.A ; BIRJUKOV F.I ; STURE N.N ; GNATJUK A.S</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_SU1746702A13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; rus</language><creationdate>1994</creationdate><topic>CHEMISTRY</topic><topic>CRACKING HYDROCARBON OILS</topic><topic>FUELS</topic><topic>LUBRICANTS</topic><topic>METALLURGY</topic><topic>MINERAL WAXES</topic><topic>PEAT</topic><topic>PETROLEUM, GAS OR COKE INDUSTRIES</topic><topic>PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION</topic><topic>RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES</topic><topic>REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS</topic><topic>REFORMING OF NAPHTHA</topic><topic>TECHNICAL GASES CONTAINING CARBON MONOXIDE</topic><toplevel>online_resources</toplevel><creatorcontrib>KARIBOV A.K</creatorcontrib><creatorcontrib>LAZ'JAN N.G</creatorcontrib><creatorcontrib>ZENCHENKOV A.N</creatorcontrib><creatorcontrib>DEM'JANENKO E.A</creatorcontrib><creatorcontrib>KHAVKIN V.A</creatorcontrib><creatorcontrib>PROSFIROV V.I</creatorcontrib><creatorcontrib>KURGANOV V.M</creatorcontrib><creatorcontrib>IL'IN V.V</creatorcontrib><creatorcontrib>GULJAEVA L.A</creatorcontrib><creatorcontrib>BIRJUKOV F.I</creatorcontrib><creatorcontrib>STURE N.N</creatorcontrib><creatorcontrib>GNATJUK A.S</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>KARIBOV A.K</au><au>LAZ'JAN N.G</au><au>ZENCHENKOV A.N</au><au>DEM'JANENKO E.A</au><au>KHAVKIN V.A</au><au>PROSFIROV V.I</au><au>KURGANOV V.M</au><au>IL'IN V.V</au><au>GULJAEVA L.A</au><au>BIRJUKOV F.I</au><au>STURE N.N</au><au>GNATJUK A.S</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>METHOD OF RECOVERY OF HYDROCARBON FUEL</title><date>1994-04-15</date><risdate>1994</risdate><abstract>FIELD: petroleum processing. SUBSTANCE: petroleum rectification yields (130-160)-(260-315) C and (260-315)-(330-400) C fractions, the latter being subjected to hydrofining. Heavy fuel oil is either vacuum distilled yielding (300-400)-(480-520) C vacuum distillate and petroleum tar which is subjected to heat treatment, or divided into two streams one of which is subjected to heat treatment. Hydrofined fraction is mixed with vacuum distillate or heavy fuel oil and products of heat treated petroleum tar or heavy fuel oil taken in amounts 30-50, 25-65, and 5-25% of mixture mass, respectively. EFFECT: recovery of hydrocarbon fuel improved. 1 tbl
Использование: нефтепереработка. Сущность изобретения: при ректификации нефти получают фракции: (130 - 160) - (260 - 315)С и (260 - 315) - (330 - 400)С. Последнюю подвергают гидроочистке. Мазут либо подвергают вакуумной перегонке с получением вакуумного дистиллята (300 - 400) - (480 - 520)С и гудрона, который подвергают термической переработке, либо разделяют на два потока, один из которых подвергают термической переработке. Гидроочищенную фракцию смешивают с вакуумным дистиллятом или мазутом и продуктами термической переработке гудрона или мазута, взятыми в количестве соответственно 30 - 50, 25 - 65 и 5 - 25% от массы смеси. 1 табл.</abstract><oa>free_for_read</oa></addata></record> |
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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 RECOVERY OF HYDROCARBON FUEL |
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