CONVERSION OF TRIACYLGLYCERIDE-CONTAINING OILS TO HYDROCARBONS
The disclosure relates to a system for converting triacylglycerides-containing oils into crude oil precursors and/or distillate hydrocarbon fuels. The system may include at least one mixing device for mixing a triacylglycerides-containing oil feed (2) with water (10) and diatomic hydrogen (14) to fo...
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| creator | Rine, Jeffrey Arora, Arun Greene, Marvin I Baxley, J., Steven Coppola, Edward Mukherjee, Ujjal K Red, Charles, Jr Nana, Sanjay |
| description | The disclosure relates to a system for converting triacylglycerides-containing oils into crude oil precursors and/or distillate hydrocarbon fuels. The system may include at least one mixing device for mixing a triacylglycerides-containing oil feed (2) with water (10) and diatomic hydrogen (14) to form an oil-water-diatomic hydrogen feed mixture (16); a hydrothermolysis reactor (18) for reacting the feed mixture (16) at a temperature in the range of 250°C to 560°C and a pressure greater than 7.5 MPa (75 bar) to produce a reaction effluent (28); a hydrotreater (29; 82) for hydrotreating the reaction effluent (28); a separator (30; 60) for separating water (32) and diatomic hydrogen (36) from hydrocarbons (68) in the hydrotreated effluent (34; 84). The hydrotreater (29; 82) is close-coupled to the hydrothermolysis reactor (18). |
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The system may include at least one mixing device for mixing a triacylglycerides-containing oil feed (2) with water (10) and diatomic hydrogen (14) to form an oil-water-diatomic hydrogen feed mixture (16); a hydrothermolysis reactor (18) for reacting the feed mixture (16) at a temperature in the range of 250°C to 560°C and a pressure greater than 7.5 MPa (75 bar) to produce a reaction effluent (28); a hydrotreater (29; 82) for hydrotreating the reaction effluent (28); a separator (30; 60) for separating water (32) and diatomic hydrogen (36) from hydrocarbons (68) in the hydrotreated effluent (34; 84). The hydrotreater (29; 82) is close-coupled to the hydrothermolysis reactor (18).</description><language>hrv ; eng</language><subject>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</subject><creationdate>2019</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=20191115&DB=EPODOC&CC=HR&NR=P20191415T1$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20191115&DB=EPODOC&CC=HR&NR=P20191415T1$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>Rine, Jeffrey</creatorcontrib><creatorcontrib>Arora, Arun</creatorcontrib><creatorcontrib>Greene, Marvin I</creatorcontrib><creatorcontrib>Baxley, J., Steven</creatorcontrib><creatorcontrib>Coppola, Edward</creatorcontrib><creatorcontrib>Mukherjee, Ujjal K</creatorcontrib><creatorcontrib>Red, Charles, Jr</creatorcontrib><creatorcontrib>Nana, Sanjay</creatorcontrib><title>CONVERSION OF TRIACYLGLYCERIDE-CONTAINING OILS TO HYDROCARBONS</title><description>The disclosure relates to a system for converting triacylglycerides-containing oils into crude oil precursors and/or distillate hydrocarbon fuels. The system may include at least one mixing device for mixing a triacylglycerides-containing oil feed (2) with water (10) and diatomic hydrogen (14) to form an oil-water-diatomic hydrogen feed mixture (16); a hydrothermolysis reactor (18) for reacting the feed mixture (16) at a temperature in the range of 250°C to 560°C and a pressure greater than 7.5 MPa (75 bar) to produce a reaction effluent (28); a hydrotreater (29; 82) for hydrotreating the reaction effluent (28); a separator (30; 60) for separating water (32) and diatomic hydrogen (36) from hydrocarbons (68) in the hydrotreated effluent (34; 84). 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The system may include at least one mixing device for mixing a triacylglycerides-containing oil feed (2) with water (10) and diatomic hydrogen (14) to form an oil-water-diatomic hydrogen feed mixture (16); a hydrothermolysis reactor (18) for reacting the feed mixture (16) at a temperature in the range of 250°C to 560°C and a pressure greater than 7.5 MPa (75 bar) to produce a reaction effluent (28); a hydrotreater (29; 82) for hydrotreating the reaction effluent (28); a separator (30; 60) for separating water (32) and diatomic hydrogen (36) from hydrocarbons (68) in the hydrotreated effluent (34; 84). The hydrotreater (29; 82) is close-coupled to the hydrothermolysis reactor (18).</abstract><oa>free_for_read</oa></addata></record> |
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| 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 |
| title | CONVERSION OF TRIACYLGLYCERIDE-CONTAINING OILS TO HYDROCARBONS |
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