FI127332B - Polttoainekoostumuksen valmistaminen - Google Patents

Polttoainekoostumuksen valmistaminen Download PDF

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FI127332B
FI127332B FI20166034A FI20166034A FI127332B FI 127332 B FI127332 B FI 127332B FI 20166034 A FI20166034 A FI 20166034A FI 20166034 A FI20166034 A FI 20166034A FI 127332 B FI127332 B FI 127332B
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composition
oil
fuel composition
fuel
diesel
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FI20166034A
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English (en)
Swedish (sv)
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FI20166034A (fi
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Ulla Kiiski
Marina Lindblad
Marja Tiitta
Kaija Isokoski
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Neste Oyj
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Priority to FI20166034A priority Critical patent/FI127332B/fi
Priority to CN201780078178.XA priority patent/CN110088250B/zh
Priority to US16/470,867 priority patent/US10947457B2/en
Priority to BR112019012830-1A priority patent/BR112019012830B1/pt
Priority to PCT/EP2017/082660 priority patent/WO2018114534A1/en
Priority to CA3045218A priority patent/CA3045218A1/en
Priority to EP17829165.4A priority patent/EP3559172A1/en
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Publication of FI20166034A publication Critical patent/FI20166034A/fi
Publication of FI127332B publication Critical patent/FI127332B/fi

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    • 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
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    • 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
    • C10G3/42—Catalytic treatment
    • C10G3/44—Catalytic treatment characterised by the catalyst used
    • C10G3/45—Catalytic treatment characterised by the catalyst used containing iron group metals or compounds thereof
    • C10G3/46—Catalytic treatment characterised by the catalyst used containing iron group metals or compounds thereof in combination with chromium, molybdenum, tungsten metals or compounds thereof
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
    • C07C1/24—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms by elimination of water
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
    • C07D307/02—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
    • C07D307/34—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
    • C07D307/38—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with substituted hydrocarbon radicals attached to ring carbon atoms
    • 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
    • C10G3/42—Catalytic treatment
    • C10G3/44—Catalytic treatment characterised by the catalyst used
    • 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
    • C10G50/00—Production of liquid hydrocarbon mixtures from lower carbon number hydrocarbons, e.g. by oligomerisation
    • 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
    • C10G69/08—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 reforming naphtha
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • C10L1/08—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for compression ignition
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/1802—Organic compounds containing oxygen natural products, e.g. waxes, extracts, fatty oils
    • 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
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/304—Pour point, cloud point, cold flow properties
    • 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
    • C10G2300/20—Characteristics of the feedstock or the products
    • C10G2300/30—Physical properties of feedstocks or products
    • C10G2300/308—Gravity, density, e.g. API
    • 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
    • C10G2400/30—Aromatics
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/10—Biofuels, e.g. bio-diesel
    • 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
    • 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
    • Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T50/00—Aeronautics or air transport
    • Y02T50/60—Efficient propulsion technologies, e.g. for aircraft
    • Y02T50/678—Aviation using fuels of non-fossil origin

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  • Chemical & Material Sciences (AREA)
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  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Emergency Medicine (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Claims (6)

  1. Patenttivaatimukset
    20166034 prh 09 -02- 2018
    1. Menetelmä polttoainekoostumuksen valmistamiseksi, joka menetelmä käsittää vaiheet, joissa
    5 a) 2-metyylifuraani (2-MF) oligomerisoidaan käyttämällä happokatalyyttiä, mistä syntyy furanyyliä sisältävä oligomerisointikoostumus, joka käsittää vähintään 70 painoprosenttia oligomeerejä, jotka valitaan sellaisten 2-MF:n trimeerien, tetrameerien ja pentameerien joukosta, jotka käsittävät 24 furanyyliryhmää
    10 b) yhtä tai useampaa materiaalin ainesosaa, jotka käsittävät rasvahappoja tai rasvahappojohdannaisia, sekoitetaan mahdollisesti vaiheessa a) saadun furanyyliä sisältävän oligomerisointikoostumuksen kanssa, jolloin syntyy yhteissyötevirtakoostumus
    c) vaiheessa a) saadulle furanyyliä sisältävälle oligerisointikoostumukselle tai
    15 vaiheessa b) saadulle yhteissyötevirtakoostumukselle suoritetaan hapenpoistokäsittely vedyn avulla vetyavusteisen hapenpoiston yksikössä, joka käsittää molybdeeni- ja/tai volframikatalyyttiä, mahdollisesti molybdeeni- ja/tai volframikatalyyttiä, johon on lisätty promoottoria, mahdollisesti sulfidoitua molybdeeni- ja/tai volframikatalyyttiä, jolloin
    20 saadaan polttoainekoostumusta jolloin mainittu polttoainekoostumus käsittää vähintään 55 painoprosenttia sekä mono- että dinafteenejä ja aromaattisia aineita siinä osassa polttoainekoostumusta, joka syntyy furanyyliä sisältävän oligomerisointikoostumuksen vedyn avulla tehtävästä hapenpoistokäsittelystä.
  2. 2. Patenttivaatimuksen 1 mukainen menetelmä, jossa vaihe b on pakollinen.
  3. 3. Patenttivaatimuksen 1 tai 2 mukainen menetelmä, jossa polttoainekoostumus on keskitisleen polttoainekoostumus.
    36/39
    20166034 prh 09 -02- 2018
  4. 4. Jonkin edellä olevan patenttivaatimuksen mukainen menetelmä, jossa polttoainekoostumus on ilman muutoksia olemassa oleviin järjestelmiin sopiva polttoainekoostumus.
  5. 5 5. Jonkin edellä olevan patenttivaatimuksen mukainen menetelmä, jossa yksi tai useampi materiaalin ainesosa, jotka käsittävät rasvahappoja tai rasvahappojohdannaisia, valitaan kasviöljyn/-rasvojen, mukaan lukien raaka mäntyöljy tai mäntyöljyn rasvahapot, kasvisöljyn/-rasvojen, eläinöljyn/-rasvojen, mukaan lukien kalaöljy/-rasvat ja leväöljy/-rasvat, tai muista mikrobiprosesseista
    10 saatavien öljyn/-rasvojen, esimerkiksi geneettisesti manipuloitujen leväöljyjen/rasvojen, muista mikrobiprosesseista saatavien geneettisesti manipuloitujen öljyjen/-rasvojen sekä geneettisesti manipuloitujen kasvisöljyjen/-rasvojen, kierrätettävän jätteen, kierrätettävän jäämän tai niiden yhdistelmän joukosta.
    15 6. Jonkin edellä olevan patenttivaatimuksen mukainen menetelmä, jossa 2metyylifuraanin (2-MF) oligomerisointi vaiheessa a) johtaa furanyyliä sisältävään oligomerisointikoostumukseen, joka käsittää vähintään 80 painoprosenttia oligomeerejä, jotka valitaan sellaisten 2-MF:n trimeerien, tetrameerien ja pentameerien joukosta, jotka käsittävät 2-4 furanyyliryhmää.
    7. Jonkin edellä olevan patenttivaatimuksen mukainen menetelmä, jossa kiehumispistealue yli 60 painoprosentissa polttoainekoostumuksesta on 150400 °C, kuten 180-400 °C, kuten 180-360 °C.
    25 8. Jonkin edellä olevan patenttivaatimuksen mukainen menetelmä, jossa polttoainekoostumuksessa ei suoriteta mitään isomerisointireaktioita.
    9. Jonkin edellä olevan patenttivaatimuksen mukainen menetelmä, jossa happokatalyytti vaiheessa a) on happoioninvaihtohartsikatalyytti, kuten
    30 polystyreeniin jadivinyylibentseenisulfonihappohartsiin pohjautuva katalyytti.
    37/39
    10. Jonkin edellä olevan patenttivaatimuksen mukainen menetelmä, jossa vaiheen
    c) molybdeeni- ja/tai volframikatalyyttiin on lisätty promoottorina nikkeliä tai kobolttia.
    5 11. Patenttivaatimuksen 10 mukainen menetelmä, jossa vaiheen c) joudutettu molybdeeni-ja/tai volframikatalyytti on sulfidoitu Ni-Mo-katalyytti.
    12. Jonkin edellä olevan patenttivaatimuksen mukainen menetelmä, jossa vaihe c) suoritetaan reaktio-olosuhteissa, joissa lämpötila on 200-400 °C, kuten 22010 380 °C, kuten 250-350 °C, kuten 295-335 °C, ja joissa paine on 20-150 baaria, kuten 60-120 baaria, kuten 90-110 baaria, kuten 95-100 baaria.
    13. Koostumus, joka käsittää furanyyliä sisältävää oligomerisointikoostumusta, joka käsittää vähintään 70 painoprosenttia oligomeerejä, jotka valitaan sellaisten
    15 2-MF:n trimeerien, tetrameerien ja pentameerien joukosta, jotka käsittävät 24 furanyyliryhmää sekoitettuna yhden tai useamman sellaisen materiaalin ainesosan kanssa, jotka käsittävät rasvahappoja tai rasvahappojohdannaisia.
    20 14. Patenttivaatimuksen 13 mukainen koostumus, jossa suurin osa trimeereistä, tetrameereistä ja pentameereistä valitaan yhden tai useamman seuraavan ainesosan tai niiden isomeerien joukosta:
    20166034 prh 09 -02- 2018
  6. 6 EMSni-rPf:ys,h-2-rura!'jfjili;2 ρίΊι'.ΊΐΓΐΐ,· > H, Li irtsulekyyl SdiRu 24b ef-jifirnc-ssaykslikcd;
    l hvdmksi 1 4 4 tic mptyvH 2 kiranyyii i-ieriLtari i s h .n. i,nric>=h»virainri l.h rfljin
    2.2.5 b-telidö-i-ieiyyl -z-tiranyviii itprii ,„i n
    CrUr.O. iirioli.-kyykpajiifj 392 itamimassaytisMiGä:
    38/39
    20166034 prh 09 -02- 2018
    15. Patenttivaatimuksen 13 tai 14 mukainen koostumus, jossa suurin osa koostumuksesta koostuu yhdestä tai useammasta materiaalin ainesosasta, jotka käsittävät rasvahappoja tai rasvahappojohdannaisia.
    5 16. Patenttivaatimuksen 15 mukainen koostumus, joka käsittää 5090 painoprosenttia yhtä tai useampaa materiaalin ainesosaa, jotka käsittävät rasvahappoja tai rasvahappojohdannaisia.
    17. Jonkin patenttivaatimuksen 13-16 mukainen koostumus, jossa yksi tai 10 useampi materiaalin ainesosa, jotka käsittävät rasvahappoja tai rasvahappojohdannaisia, valitaan kasviöljyn/-rasvojen, mukaan lukien raaka mäntyöljy tai mäntyöljyn rasvahapot, kasvisöljyn/-rasvojen, eläinöljyn/-rasvojen, mukaan lukien kalaöljy/-rasvat ja leväöljy/-rasvat, tai muista mikrobiprosesseista saatavien öljyn/-rasvojen, esimerkiksi geneettisesti manipuloitujen leväöljyjen/15 rasvojen, muista mikrobiprosesseista saatavien geneettisesti manipuloitujen öljyjen/-rasvojen sekä geneettisesti manipuloitujen kasvisöljyjen/-rasvojen, kierrätettävän jätteen, kierrätettävän jäämän tai niiden yhdistelmän joukosta.
    18. Jonkin patenttivaatimuksen 13-17 mukaisen koostumuksen käyttö
    20 seosainesosana, joka lisää dieselhiilivetykoostumusta käsittävän seoskoostumuksen tiheyttä.
    19. Jonkin patenttivaatimuksen 13-17 mukaisen koostumuksen käyttö seosainesosana, joka parantaa dieselhiilivetykoostumusta käsittävän
    25 seoskoostum uksen kylmävirtausominaisuutta.
    20. Sellaisen furanyyliä sisältävän oligomerisointikoostumuksen käyttö, joka käsittää vähintään 70 painoprosenttia oligomeerejä, jotka valitaan sellaisten 2MF:n trimeerien, tetrameerien ja pentameerien joukosta, jotka käsittävät 230 4 furanyyliryhmää, yhteissyötevirtana olemassa olevassa jalostamon vetykäsittelyyksikössä.
    39/39
    21. Polttoainekoostumus, jota voidaan saada jonkin patenttivaatimuksen 1-12 mukaisella menetelmällä.
    22. Polttoainekoostumus, jota voidaan saada jonkin patenttivaatimuksen 2-12 5 mukaisella menetelmällä.
    23. Seoskoostumus, joka käsittää polttoainekoostumusta, jota voidaan saada jonkin patenttivaatimuksen 1-12 mukaisella menetelmällä, ja dieselhiilivetykoostumusta.
    20166034 prh 09 -02- 2018
    1-16007 / P81604908FI00
    1/6
    20166034 prh 23 -12- 2016
    1-16007 / P81604908FI00
    2/6
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FI20166034A FI127332B (fi) 2016-12-23 2016-12-23 Polttoainekoostumuksen valmistaminen
CN201780078178.XA CN110088250B (zh) 2016-12-23 2017-12-13 燃料组合物的生产
US16/470,867 US10947457B2 (en) 2016-12-23 2017-12-13 Production of a fuel composition
BR112019012830-1A BR112019012830B1 (pt) 2016-12-23 2017-12-13 Método para produção de uma composição de combustível destilado médio drop-in e uso de uma composição de oligomerização contendo furanila
PCT/EP2017/082660 WO2018114534A1 (en) 2016-12-23 2017-12-13 Production of a fuel composition
CA3045218A CA3045218A1 (en) 2016-12-23 2017-12-13 Production of a fuel composition
EP17829165.4A EP3559172A1 (en) 2016-12-23 2017-12-13 Production of a fuel composition

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FI20166034A FI127332B (fi) 2016-12-23 2016-12-23 Polttoainekoostumuksen valmistaminen

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EP (1) EP3559172A1 (fi)
CN (1) CN110088250B (fi)
BR (1) BR112019012830B1 (fi)
CA (1) CA3045218A1 (fi)
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WO (1) WO2018114534A1 (fi)

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3287374A (en) 1963-08-15 1966-11-22 Quaker Oats Co Novel furan compounds and processes for preparation
US5454842A (en) 1994-12-02 1995-10-03 Exxon Research & Engineering Co. Cetane improver compositions comprising nitrated fatty acid derivatives
US8022258B2 (en) 2005-07-05 2011-09-20 Neste Oil Oyj Process for the manufacture of diesel range hydrocarbons
AU2008222628B2 (en) * 2007-03-08 2013-05-23 Virent, Inc. Synthesis of liquid fuels and chemicals from oxygenated hydrocarbons
ES2362248B1 (es) 2009-12-11 2012-05-10 Universidad Politecnica De Valencia Producción de combustibles l�?quidos (sylvan-liquid fuels) a partir de 2 -metilfurano.
ES2371839B1 (es) * 2010-06-16 2012-11-19 Consejo Superior De Investigaciones Científicas (Csic) Proceso de conversión de biomasa en combustible líquido.
US20130144094A1 (en) 2011-12-06 2013-06-06 Phillips 66 Company Renewable gas oil derived from biomass
US8629310B2 (en) * 2012-03-09 2014-01-14 Phillips 66 Company Transportation fuels from biomass oxygenates

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US20200087578A1 (en) 2020-03-19
CN110088250B (zh) 2022-09-27
US10947457B2 (en) 2021-03-16
CN110088250A (zh) 2019-08-02
WO2018114534A1 (en) 2018-06-28
EP3559172A1 (en) 2019-10-30
BR112019012830B1 (pt) 2022-09-06
FI20166034A (fi) 2018-03-29
BR112019012830A2 (pt) 2019-11-26
CA3045218A1 (en) 2018-06-28

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