PETROLEUM FRACTION HYDROFINING PROCESS
FIELD: petroleum processing. ^ SUBSTANCE: invention, in particular, relates to petroleum fraction hydrofining process utilizing presulfided catalysts. Hydrofining process is described involving contacting petroleum fractions with presulfided catalyst containing alumina-carried cobalt, molybdenum, ph...
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| creator | REZNICHENKO IRINA DMITRIEVNA ALIEV RAMIZ RZA OGLY ELSHIN ANATOLIJ IVANOVICH KUKS IGOR' VITAL'EVICH KRJACHEK SERGEJ LAVRENT'EVICH KASTERIN VLADIMIR NIKOLAEVICH TROFIMOVA MARINA VITAL'EVNA TSELJUTINA MARINA IVANOVNA |
| description | FIELD: petroleum processing. ^ SUBSTANCE: invention, in particular, relates to petroleum fraction hydrofining process utilizing presulfided catalysts. Hydrofining process is described involving contacting petroleum fractions with presulfided catalyst containing alumina-carried cobalt, molybdenum, phosphorus, and boron, said process being conducted at 320-340°C, pressure 3.0-5.0 MPa, volumetric feed supply rate 1.0-6.0 h-1, normalized volumetric hydrogen-containing gas-to-feed ratio (500-1000):1 in presence of catalyst sulfided outside of reactor. Sulfidizing of catalyst is accomplished with hydrogen sulfide at 80-500°C and volumetric hydrogen sulfide flow rate 0.02-6.0 h-1. Chemical composition of catalyst is the following, wt %: MoS2 8.0-17.0, Co3S2 1.5-4.0, P2O3 2.5-5.0, B2O3 0.3-1.0, La2O3 1.0-5.0, and aluminum oxide - the balance. ^ EFFECT: simplified process. ^ 2 cl, 1 tbl, 3 ex |
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Hydrofining process is described involving contacting petroleum fractions with presulfided catalyst containing alumina-carried cobalt, molybdenum, phosphorus, and boron, said process being conducted at 320-340°C, pressure 3.0-5.0 MPa, volumetric feed supply rate 1.0-6.0 h-1, normalized volumetric hydrogen-containing gas-to-feed ratio (500-1000):1 in presence of catalyst sulfided outside of reactor. Sulfidizing of catalyst is accomplished with hydrogen sulfide at 80-500°C and volumetric hydrogen sulfide flow rate 0.02-6.0 h-1. Chemical composition of catalyst is the following, wt %: MoS2 8.0-17.0, Co3S2 1.5-4.0, P2O3 2.5-5.0, B2O3 0.3-1.0, La2O3 1.0-5.0, and aluminum oxide - the balance. ^ EFFECT: simplified process. ^ 2 cl, 1 tbl, 3 ex</description><language>eng ; rus</language><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY ; CHEMISTRY ; CRACKING HYDROCARBON OILS ; FUELS ; LUBRICANTS ; METALLURGY ; MINERAL WAXES ; PEAT ; PERFORMING OPERATIONS ; PETROLEUM, GAS OR COKE INDUSTRIES ; PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL ; 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 ; THEIR RELEVANT APPARATUS ; TRANSPORTING</subject><creationdate>2007</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=20070210&DB=EPODOC&CC=RU&NR=2293107C1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20070210&DB=EPODOC&CC=RU&NR=2293107C1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>REZNICHENKO IRINA DMITRIEVNA</creatorcontrib><creatorcontrib>ALIEV RAMIZ RZA OGLY</creatorcontrib><creatorcontrib>ELSHIN ANATOLIJ IVANOVICH</creatorcontrib><creatorcontrib>KUKS IGOR' VITAL'EVICH</creatorcontrib><creatorcontrib>KRJACHEK SERGEJ LAVRENT'EVICH</creatorcontrib><creatorcontrib>KASTERIN VLADIMIR NIKOLAEVICH</creatorcontrib><creatorcontrib>TROFIMOVA MARINA VITAL'EVNA</creatorcontrib><creatorcontrib>TSELJUTINA MARINA IVANOVNA</creatorcontrib><title>PETROLEUM FRACTION HYDROFINING PROCESS</title><description>FIELD: petroleum processing. ^ SUBSTANCE: invention, in particular, relates to petroleum fraction hydrofining process utilizing presulfided catalysts. Hydrofining process is described involving contacting petroleum fractions with presulfided catalyst containing alumina-carried cobalt, molybdenum, phosphorus, and boron, said process being conducted at 320-340°C, pressure 3.0-5.0 MPa, volumetric feed supply rate 1.0-6.0 h-1, normalized volumetric hydrogen-containing gas-to-feed ratio (500-1000):1 in presence of catalyst sulfided outside of reactor. Sulfidizing of catalyst is accomplished with hydrogen sulfide at 80-500°C and volumetric hydrogen sulfide flow rate 0.02-6.0 h-1. Chemical composition of catalyst is the following, wt %: MoS2 8.0-17.0, Co3S2 1.5-4.0, P2O3 2.5-5.0, B2O3 0.3-1.0, La2O3 1.0-5.0, and aluminum oxide - the balance. ^ EFFECT: simplified process. ^ 2 cl, 1 tbl, 3 ex</description><subject>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</subject><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>PERFORMING OPERATIONS</subject><subject>PETROLEUM, GAS OR COKE INDUSTRIES</subject><subject>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</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><subject>THEIR RELEVANT APPARATUS</subject><subject>TRANSPORTING</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>2007</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNrjZFALcA0J8vdxDfVVcAtydA7x9PdT8Ih0CfJ38_Tz9HNXCAjyd3YNDuZhYE1LzClO5YXS3AwKbq4hzh66qQX58anFBYnJqXmpJfFBoUZGlsaGBubOhsZEKAEAp3UjoA</recordid><startdate>20070210</startdate><enddate>20070210</enddate><creator>REZNICHENKO IRINA DMITRIEVNA</creator><creator>ALIEV RAMIZ RZA OGLY</creator><creator>ELSHIN ANATOLIJ IVANOVICH</creator><creator>KUKS IGOR' VITAL'EVICH</creator><creator>KRJACHEK SERGEJ LAVRENT'EVICH</creator><creator>KASTERIN VLADIMIR NIKOLAEVICH</creator><creator>TROFIMOVA MARINA VITAL'EVNA</creator><creator>TSELJUTINA MARINA IVANOVNA</creator><scope>EVB</scope></search><sort><creationdate>20070210</creationdate><title>PETROLEUM FRACTION HYDROFINING PROCESS</title><author>REZNICHENKO IRINA DMITRIEVNA ; ALIEV RAMIZ RZA OGLY ; ELSHIN ANATOLIJ IVANOVICH ; KUKS IGOR' VITAL'EVICH ; KRJACHEK SERGEJ LAVRENT'EVICH ; KASTERIN VLADIMIR NIKOLAEVICH ; TROFIMOVA MARINA VITAL'EVNA ; TSELJUTINA MARINA IVANOVNA</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_RU2293107C13</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>eng ; rus</language><creationdate>2007</creationdate><topic>CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY</topic><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>PERFORMING OPERATIONS</topic><topic>PETROLEUM, GAS OR COKE INDUSTRIES</topic><topic>PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL</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><topic>THEIR RELEVANT APPARATUS</topic><topic>TRANSPORTING</topic><toplevel>online_resources</toplevel><creatorcontrib>REZNICHENKO IRINA DMITRIEVNA</creatorcontrib><creatorcontrib>ALIEV RAMIZ RZA OGLY</creatorcontrib><creatorcontrib>ELSHIN ANATOLIJ IVANOVICH</creatorcontrib><creatorcontrib>KUKS IGOR' VITAL'EVICH</creatorcontrib><creatorcontrib>KRJACHEK SERGEJ LAVRENT'EVICH</creatorcontrib><creatorcontrib>KASTERIN VLADIMIR NIKOLAEVICH</creatorcontrib><creatorcontrib>TROFIMOVA MARINA VITAL'EVNA</creatorcontrib><creatorcontrib>TSELJUTINA MARINA IVANOVNA</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>REZNICHENKO IRINA DMITRIEVNA</au><au>ALIEV RAMIZ RZA OGLY</au><au>ELSHIN ANATOLIJ IVANOVICH</au><au>KUKS IGOR' VITAL'EVICH</au><au>KRJACHEK SERGEJ LAVRENT'EVICH</au><au>KASTERIN VLADIMIR NIKOLAEVICH</au><au>TROFIMOVA MARINA VITAL'EVNA</au><au>TSELJUTINA MARINA IVANOVNA</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>PETROLEUM FRACTION HYDROFINING PROCESS</title><date>2007-02-10</date><risdate>2007</risdate><abstract>FIELD: petroleum processing. ^ SUBSTANCE: invention, in particular, relates to petroleum fraction hydrofining process utilizing presulfided catalysts. Hydrofining process is described involving contacting petroleum fractions with presulfided catalyst containing alumina-carried cobalt, molybdenum, phosphorus, and boron, said process being conducted at 320-340°C, pressure 3.0-5.0 MPa, volumetric feed supply rate 1.0-6.0 h-1, normalized volumetric hydrogen-containing gas-to-feed ratio (500-1000):1 in presence of catalyst sulfided outside of reactor. Sulfidizing of catalyst is accomplished with hydrogen sulfide at 80-500°C and volumetric hydrogen sulfide flow rate 0.02-6.0 h-1. Chemical composition of catalyst is the following, wt %: MoS2 8.0-17.0, Co3S2 1.5-4.0, P2O3 2.5-5.0, B2O3 0.3-1.0, La2O3 1.0-5.0, and aluminum oxide - the balance. ^ EFFECT: simplified process. ^ 2 cl, 1 tbl, 3 ex</abstract><oa>free_for_read</oa></addata></record> |
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| subjects | CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY CHEMISTRY CRACKING HYDROCARBON OILS FUELS LUBRICANTS METALLURGY MINERAL WAXES PEAT PERFORMING OPERATIONS PETROLEUM, GAS OR COKE INDUSTRIES PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL 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 THEIR RELEVANT APPARATUS TRANSPORTING |
| title | PETROLEUM FRACTION HYDROFINING PROCESS |
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