HRP20191787T1 - Pretvaranje ulja koja sadržavaju triacilgliceride - Google Patents

Pretvaranje ulja koja sadržavaju triacilgliceride Download PDF

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Publication number
HRP20191787T1
HRP20191787T1 HRP20191787TT HRP20191787T HRP20191787T1 HR P20191787 T1 HRP20191787 T1 HR P20191787T1 HR P20191787T T HRP20191787T T HR P20191787TT HR P20191787 T HRP20191787 T HR P20191787T HR P20191787 T1 HRP20191787 T1 HR P20191787T1
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Croatia
Prior art keywords
triacylglycerides
oil
carbon dioxide
mixture
reaction
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HRP20191787TT
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English (en)
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Marvin I. Greene
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Lummus Technology Llc
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Publication of HRP20191787T1 publication Critical patent/HRP20191787T1/hr

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • C10G3/40—Thermal non-catalytic treatment
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • C10G3/50—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids in the presence of hydrogen, hydrogen donors or hydrogen generating compounds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/06—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof
    • C10G45/08—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing nickel or cobalt metal, or compounds thereof in combination with chromium, molybdenum, or tungsten metals, or compounds thereof
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
    • C10G45/04—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used
    • C10G45/10—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing characterised by the catalyst used containing platinum group metals or compounds thereof
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G65/00—Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/12—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G69/00—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process
    • C10G69/02—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only
    • C10G69/06—Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process plural serial stages only including at least one step of thermal cracking in the absence of hydrogen
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
    • B01J2208/023—Details
    • B01J2208/027—Beds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
    • B01J2219/00103—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor in a heat exchanger separate from the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/24—Stationary reactors without moving elements inside
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1011—Biomass
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1011—Biomass
    • C10G2300/1014—Biomass of vegetal origin
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1011—Biomass
    • C10G2300/1018—Biomass of animal origin
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/40—Characteristics of the process deviating from typical ways of processing
    • C10G2300/4081—Recycling aspects
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/02—Gasoline
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/04—Diesel oil
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
    • C10G2400/08—Jet fuel
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock

Claims (12)

1. Postupak za pretvaranje ulja koja sadržavaju triacilgliceride u prekursore sirove nafte i / ili destilirana ugljikovodična goriva, naznačen time, da postupak uključuje: miješanje ulja koje sadržava triacilglicerid s ugljičnim dioksidom radi dobivanja smjese triacilglicerida i CO2 (12); reakcija smjese triacilglicerida i CO2 (12) u reakcijskoj zoni toplinskog reformiranja (18), pod reakcijskim uvjetima dovoljnim za pretvaranje barem dijela triacilglicerida toplinskim reformiranjem u ugljikovodične spojeve koji sadržavaju jedan ili više izoolefina, izoparafina, cikloolefine, cikloparafine, i aromatike; i dobivanje reakcijske otpadne tekućine (28) iz reakcijske zone toplinskog reformiranja (18), pri čemu: reakcijski uvjeti uključuju temperaturu u rasponu od oko 250 °C do oko 560 °C i tlak veći od 7,5 MPa (75 bara), smjesa triacilglicerida i CO2 ima omjer mase CO2 u odnosu na triacilgliceride u rasponu od oko 0,001 : 1 do otprilike 1: 1, smjesa triacilglicerida i ugljičnog dioksida (12) nadalje sadržava vodu, a smjesa triacilglicerida i ugljičnog dioksida (12) ima omjer mase vode u odnosu na triacilgliceride u rasponu od oko 0,001: 1 do oko 0,1: 1.
2. Postupak u skladu s patentnim zahtjevom 1, naznačen time, da smjesa triacilglicerida i ugljičnog dioksida (12) nadalje sadržava vodik, pri čemu smjesa triacilglicerida i ugljičnog dioksida ima omjer mase vodika i triacilglicerida u rasponu od oko 0,001: 1 do oko 0,5: 1.
3. Postupak u skladu s patentnim zahtjevom 1, naznačen time, da nadalje obuhvaća odvajanje reakcijske otpadne tekućine (28) radi dobivanja prvog proizvoda odvajanja (64) koji sadržava ugljični dioksid i drugog proizvoda odvajanja (68) koji sadržava ugljikovodike.
4. Postupak u skladu s patentnim zahtjevom 3, naznačen time, da nadalje obuhvaća odvajanje vode (34a) od reakcijske otpadne tekućine (28).
5. Postupak u skladu s patentnim zahtjevom 3, naznačen time, da nadalje obuhvaća hidro obradu barem dijela drugog proizvoda odvajanja (68).
6. Postupak u skladu s patentnim zahtjevom 3, naznačen time, da nadalje obuhvaća ponovnu upotrebu barem dijela (32) prvog proizvoda odvajanja (64) u reakcijskom koraku.
7. Postupak u skladu s patentnim zahtjevom 1, naznačen time, da ulje koje sadržava triacilgliceride sadržava obnovljivo ulje od barem jednog od sljedećih: kamelija, karinata, pamuk, jatrofa, karanja, moringa, palma, ricinus, kukuruz, laneno sjeme, kikiriki, soja, suncokret, tung, babassu ili barem jedno ulje koje sadržava triacilgliceride iz barem jednog od sljedećih: kanola, shea maslac, tall ulje, loj, otpadno biljno ulje, masti iz posuda za odvajanje, rabljeno ulje za kuhanje, ulje algi i pongamia.
8. Postupak u skladu s patentnim zahtjevom 7, naznačen time, da ulje koje sadržava triacilgliceride sadržava slobodne masne kiseline dobivene od barem jednog od sljedećih: kamelija, karinata, pamuk, jatrofa, karanja, moringa, palma, ricinus, kukuruz, laneno sjeme, kikiriki, soja, suncokret, tung, babassu ili barem jedno od sljedećih: kanola, shea maslac, tall ulje, loj, otpadno biljno ulje, masti iz posuda za odvajanje, rabljeno ulje za kuhanje, ulje algi i pongamia.
9. Postupak u skladu s patentnim zahtjevom 3, naznačen time, da nadalje obuhvaća frakcioniranje drugog proizvoda odvajanja (68) kako bi se dobila jedna ili više frakcija ugljikovodika koje vriju u području nafte (38), dizela (42) ili mlaznog goriva (40).
10. Postupak u skladu s patentnim zahtjevom 5, naznačen time, da nadalje obuhvaća frakcioniranje hidro obrađenog proizvoda odvajanja (92) da bi se dobila jedna ili više frakcija ugljikovodika koje vriju u području nafte (38), dizela (42) ili mlaznog goriva (40).
11. Postupak u skladu s patentnim zahtjevom 1, naznačen time, da nadalje uključuje ubrizgavanje tekućeg ugljičnog dioksida u reakcijsku zonu toplinskog reformiranja kako bi se održala temperatura ili temperaturni profil unutar reakcijske zone toplinskog reformiranja.
12. Postupak u skladu s patentnim zahtjevom 1, naznačen time, da se reakcija provodi bez dodatka vodika.
HRP20191787TT 2012-12-11 2019-10-03 Pretvaranje ulja koja sadržavaju triacilgliceride HRP20191787T1 (hr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US13/711,140 US9024096B2 (en) 2012-12-11 2012-12-11 Conversion of triacylglycerides-containing oils
EP13863625.3A EP2931842B1 (en) 2012-12-11 2013-12-04 Conversion of triacylglycerides-containing oils
PCT/US2013/073136 WO2014093099A1 (en) 2012-12-11 2013-12-04 Conversion of triacylglycerides-containing oils

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HRP20191787T1 true HRP20191787T1 (hr) 2019-12-27

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US (2) US9024096B2 (hr)
EP (1) EP2931842B1 (hr)
KR (1) KR101891871B1 (hr)
AR (1) AR093906A1 (hr)
DK (1) DK2931842T3 (hr)
HR (1) HRP20191787T1 (hr)
HU (1) HUE045685T2 (hr)
PL (1) PL2931842T3 (hr)
RS (1) RS59448B1 (hr)
TW (1) TWI510608B (hr)
WO (1) WO2014093099A1 (hr)

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Publication number Priority date Publication date Assignee Title
WO2015132922A1 (ja) * 2014-03-05 2015-09-11 中国電力株式会社 超臨界流体によるガス化装置
JP5865554B1 (ja) * 2014-03-05 2016-02-17 中国電力株式会社 超臨界流体によるガス化装置
CA2975021C (en) 2015-01-28 2021-03-30 Applied Research Associates, Inc. Hydrothermal cleanup process
US10920158B2 (en) 2019-06-14 2021-02-16 Saudi Arabian Oil Company Supercritical water process to produce bottom free hydrocarbons
US11781075B2 (en) 2020-08-11 2023-10-10 Applied Research Associates, Inc. Hydrothermal purification process

Family Cites Families (72)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4504503A (en) * 1981-09-09 1985-03-12 Lever Brothers Company Fractionation of butterfat using a liquefied gas or a gas in the supercritical state
US5071805A (en) 1989-05-10 1991-12-10 Chevron Research And Technology Company Catalyst system for hydrotreating hydrocarbons
US5073530A (en) 1989-05-10 1991-12-17 Chevron Research And Technology Company Hydrocracking catalyst and process
US4990243A (en) 1989-05-10 1991-02-05 Chevron Research And Technology Company Process for hydrodenitrogenating hydrocarbon oils
US5277793A (en) 1989-05-10 1994-01-11 Chevron Research And Technology Company Hydrocracking process
US5069890A (en) 1989-06-19 1991-12-03 Texaco Inc. Zeolite treating process
US5104587A (en) * 1990-05-16 1992-04-14 The Procter & Gamble Company Countercurrent liquid/liquid extraction to fractionate complex mixtures containing medium and long chain fatty acid triglycerides
US5141909A (en) 1991-01-22 1992-08-25 Chevron Research And Technology Company Zeolitic catalyst having selectivity for jet fuel
US5439860A (en) 1992-04-16 1995-08-08 Chevron Research And Technology Company, A Division Of Chevron U.S.A. Inc. Catalyst system for combined hydrotreating and hydrocracking and a process for upgrading hydrocarbonaceous feedstocks
US5959167A (en) 1997-08-25 1999-09-28 The University Of Utah Research Foundation Process for conversion of lignin to reformulated hydrocarbon gasoline
US6514897B1 (en) 1999-01-12 2003-02-04 Hyperion Catalysis International, Inc. Carbide and oxycarbide based compositions, rigid porous structures including the same, methods of making and using the same
US6860986B2 (en) 2002-11-08 2005-03-01 Chevron U.S.A. Inc. Extremely low acidity ultrastable Y zeolite catalyst composition and process
US6902664B2 (en) 2002-11-08 2005-06-07 Chevron U.S.A. Inc. Extremely low acidity USY and homogeneous, amorphous silica-alumina hydrocracking catalyst and process
US6872685B2 (en) 2002-11-08 2005-03-29 Chevron U.S.A. Inc. Method for preparing a highly homogeneous amorphous silica-alumina composition
DE10327059B4 (de) * 2003-06-16 2005-12-22 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Verfahren zum Konvertieren von fett- oder ölhaltigen Roh- und Abfallstoffen in Gemische mit hohem Kohlenwasserstoffanteil, mit diesem Verfahren hergestellte Produkte und deren Verwendung
ITMI20050062A1 (it) 2005-01-20 2006-07-21 Polimeri Europa Spa Processo per la preparazione di fenolo
US7964761B2 (en) 2005-05-02 2011-06-21 University Of Utah Research Foundation Processes for catalytic conversion of lignin to liquid bio-fuels and novel bio-fuels
US7928273B2 (en) * 2005-08-29 2011-04-19 David Bradin Process for producing a renewable fuel in the gasoline or jet fuel range
US7754931B2 (en) * 2005-09-26 2010-07-13 Her Majesty The Queen In Right Of Canada As Represented By The Minister Of Natural Resources Production of high-cetane diesel fuel from low-quality biomass-derived feedstocks
AU2006309212B2 (en) 2005-10-31 2011-09-15 Government Of The United States Of America, Represented By The Secretary Department Of Health And Human Services Polysaccharide-derived nitric oxide-releasing carbon-bound diazeniumdiolates
US7501546B2 (en) 2005-12-12 2009-03-10 Neste Oil Oj Process for producing a branched hydrocarbon component
US7850841B2 (en) 2005-12-12 2010-12-14 Neste Oil Oyj Process for producing a branched hydrocarbon base oil from a feedstock containing aldehyde and/or ketone
US7998339B2 (en) 2005-12-12 2011-08-16 Neste Oil Oyj Process for producing a hydrocarbon component
US7459597B2 (en) 2005-12-13 2008-12-02 Neste Oil Oyj Process for the manufacture of hydrocarbons
US20070137097A1 (en) * 2005-12-16 2007-06-21 Michio Ikura Production of biodiesel from triglycerides via a thermal route
BRPI0601403B1 (pt) 2006-04-17 2015-11-03 Petroleo Brasileiro Sa processo de obtenção de n-parafinas a partir de óleo vegetal
US7511181B2 (en) 2006-05-02 2009-03-31 Uop Llc Production of diesel fuel from biorenewable feedstocks
US7880049B2 (en) 2006-06-06 2011-02-01 Wisconsin Alumni Research Foundation Production of liquid alkanes in the jet fuel range (C8-C15) from biomass-derived carbohydrates
CA2653528C (en) 2006-06-09 2015-02-03 Albemarle Netherlands B.V. Catalytic hydrodeoxygenation of an oxygenate feedstock
US8067653B2 (en) 2006-07-14 2011-11-29 The Governors Of The University Of Alberta Methods for producing fuels and solvents
GB2454635B (en) 2006-09-19 2011-08-31 Applied Res Associates Inc Method of converting triglycerides to biofuels
EP1911734A1 (en) 2006-10-06 2008-04-16 Bp Oil International Limited Process for hydrogenation of carboxylic acids and derivatives to hydrocarbons
ITMI20062193A1 (it) 2006-11-15 2008-05-16 Eni Spa Processo per produrre frazioni idrocarburiche da miscele di origine biologica
KR20090095631A (ko) * 2006-12-01 2009-09-09 노쓰 캐롤라이나 스테이트 유니버시티 바이오매스를 연료로 변환하는 방법
US20080163543A1 (en) 2007-01-05 2008-07-10 Ramin Abhari Process for producing bio-derived fuel with alkyl ester and iso-paraffin components
ITMI20070522A1 (it) 2007-03-16 2008-09-17 Eni Spa Composizione idrocarburica utile come carburante e combustibile contenente una componente petrolifera e una componente di origine biologica
US8084655B2 (en) 2007-06-15 2011-12-27 E. I. Du Pont De Nemours And Company Catalytic process for converting renewable resources into paraffins for use as diesel blending stocks
US8523959B2 (en) 2007-07-26 2013-09-03 Chevron U.S.A. Inc. Paraffinic biologically-derived distillate fuels with bio-oxygenates for improved lubricity and methods of making same
US8148559B1 (en) * 2007-08-31 2012-04-03 Clemson University Research Foundation Supercritical fluid explosion process to aid fractionation of lipids from biomass
US20090077864A1 (en) 2007-09-20 2009-03-26 Marker Terry L Integrated Process of Algae Cultivation and Production of Diesel Fuel from Biorenewable Feedstocks
US7915460B2 (en) 2007-09-20 2011-03-29 Uop Llc Production of diesel fuel from biorenewable feedstocks with heat integration
US7982077B2 (en) 2007-09-20 2011-07-19 Uop Llc Production of diesel fuel from biorenewable feedstocks with selective separation of converted oxygen
US8003834B2 (en) 2007-09-20 2011-08-23 Uop Llc Integrated process for oil extraction and production of diesel fuel from biorenewable feedstocks
US7999143B2 (en) 2007-09-20 2011-08-16 Uop Llc Production of diesel fuel from renewable feedstocks with reduced hydrogen consumption
US7982075B2 (en) 2007-09-20 2011-07-19 Uop Llc Production of diesel fuel from biorenewable feedstocks with lower hydrogen consumption
US7982076B2 (en) 2007-09-20 2011-07-19 Uop Llc Production of diesel fuel from biorenewable feedstocks
US7999142B2 (en) 2007-09-20 2011-08-16 Uop Llc Production of diesel fuel from biorenewable feedstocks
US7982078B2 (en) 2007-09-20 2011-07-19 Uop Llc Production of diesel fuel from biorenewable feedstocks with selective separation of converted oxygen
FI20075794L (fi) 2007-11-09 2009-05-10 Upm Kymmene Oyj Integroitu prosessi diesel-polttoaineen valmistamiseksi biologisesta materiaalista ja prosessiin liittyvät tuotteet, käyttötavat ja laitteisto
US8026401B2 (en) 2007-12-20 2011-09-27 Syntroleum Corporation Hydrodeoxygenation process
US20090166261A1 (en) * 2007-12-28 2009-07-02 Chevron U.S.A. Inc. Upgrading heavy hydrocarbon oils
US8017819B2 (en) * 2008-04-25 2011-09-13 Conocophillips Company Thermal treatment of triglycerides
US20110155631A1 (en) 2008-06-17 2011-06-30 Pekka Knuuttila Integrated Process for Producing Diesel Fuel from Biological Material and Products and Uses Relating to Said Process
US9005429B2 (en) 2008-07-01 2015-04-14 Neste Oil Oyj Process for the manufacture of hydrocarbon components
US20100050502A1 (en) * 2008-08-21 2010-03-04 LiveFuels, Inc. Systems and methods for hydrothermal conversion of algae into biofuel
RU2495082C2 (ru) 2008-09-10 2013-10-10 Хальдор Топсеэ А/С Способ и катализатор гидропереработки
MY159547A (en) 2008-10-01 2017-01-13 Licella Pty Ltd Bio-oil production method
IT1392194B1 (it) 2008-12-12 2012-02-22 Eni Spa Processo per la produzione di idrocarburi, utili per autotrazione, da miscele di origine biologica
FR2940144B1 (fr) 2008-12-23 2016-01-22 Inst Francais Du Petrole Methode de transformation d'effluents d'origine renouvelable en carburant d'excellente qualite mettant en oeuvre un catalyseur a base de molybdene
FR2943071B1 (fr) 2009-03-10 2011-05-13 Inst Francais Du Petrole Procede d'hydrodesoxygenation de charges issues de sources renouvelables avec conversion limitee en decarboxylation mettant en oeuvre un catalyseur a base de nickel et de molybdene
US8193803B2 (en) 2009-03-23 2012-06-05 Consolidated Edison Company Of New York, Inc. Current measuring device
US8492600B2 (en) * 2009-04-07 2013-07-23 Gas Technology Institute Hydropyrolysis of biomass for producing high quality fuels
US20110028773A1 (en) 2009-07-29 2011-02-03 Bala Subramaniam Deoxygenation of Bio-Oils and Other Compounds to Hydrocarbons in Supercritical Media
US8766024B2 (en) * 2009-11-20 2014-07-01 Phillips 66 Company Process to mitigate the corrosion of oils/fats
CN102858728B (zh) 2009-12-30 2014-11-12 维仁特公司 用于对多元醇进行加氢脱氧的改良型催化剂
WO2011094618A1 (en) 2010-02-01 2011-08-04 Conocophillips Company Water-forming hydrogenation reactions utilizing enhanced catalyst supports and methods of use
JP2011246605A (ja) * 2010-05-26 2011-12-08 Hitachi Plant Technologies Ltd バイオ燃料製造方法
US8404911B2 (en) 2010-05-27 2013-03-26 Jumluck Srinakruang Process for producing fuel from vegetable oil by using ore catalyst
US9580660B2 (en) 2010-06-18 2017-02-28 The Texas A&M University System Deoxygenation of biomass derived oxygenates to hydrocarbons via direct methane intervention
US20120016167A1 (en) 2010-07-15 2012-01-19 Exxonmobil Research And Engineering Company Hydroprocessing of biocomponent feeds with low pressure hydrogen-containing streams
US8431756B2 (en) * 2010-12-13 2013-04-30 Exxonmobil Research And Engineering Company Conversion catalysts and processes having oxygenate and water stability
KR101404228B1 (ko) * 2012-01-05 2014-06-11 한국과학기술연구원 초임계유체를 이용한 재생연료의 제조방법

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