[go: up one dir, main page]

DK3019577T3 - Fremgangsmåde til fremstilling af carbonhydrider - Google Patents

Fremgangsmåde til fremstilling af carbonhydrider Download PDF

Info

Publication number
DK3019577T3
DK3019577T3 DK14744614.0T DK14744614T DK3019577T3 DK 3019577 T3 DK3019577 T3 DK 3019577T3 DK 14744614 T DK14744614 T DK 14744614T DK 3019577 T3 DK3019577 T3 DK 3019577T3
Authority
DK
Denmark
Prior art keywords
catalyst
hydro
treatment
hydroprocessing
catalysts
Prior art date
Application number
DK14744614.0T
Other languages
English (en)
Inventor
Jaakko Nousiainen
Teemu Lindberg
Isto Eilos
Heli Laumola
Kati Vilonen
Original Assignee
Upm Kymmene Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Upm Kymmene Corp filed Critical Upm Kymmene Corp
Application granted granted Critical
Publication of DK3019577T3 publication Critical patent/DK3019577T3/da

Links

Classifications

    • 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
    • C10G3/00—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids
    • 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
    • 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
    • C10G3/45—Catalytic treatment characterised by the catalyst used containing iron 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
    • 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
    • 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
    • C10G3/47—Catalytic treatment 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
    • 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
    • C10G3/48—Catalytic treatment characterised by the catalyst used further characterised by the catalyst support
    • 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
    • C10G3/48—Catalytic treatment characterised by the catalyst used further characterised by the catalyst support
    • C10G3/49—Catalytic treatment characterised by the catalyst used further characterised by the catalyst support containing crystalline aluminosilicates, e.g. molecular sieves
    • 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
    • C10G3/54—Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids characterised by the catalytic bed
    • 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
    • C10G45/44—Hydrogenation of the aromatic hydrocarbons
    • 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
    • C10G45/44—Hydrogenation of the aromatic hydrocarbons
    • C10G45/46—Hydrogenation of the aromatic hydrocarbons 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
    • C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • 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
    • C10G45/58—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins
    • C10G45/60—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins 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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/007—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 in the presence of hydrogen from a special source or of a special composition or having been purified by a special 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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/22—Separation of effluents
    • 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
    • C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
    • C10G49/24—Starting-up hydrotreatment operations
    • 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
    • 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
    • C10G65/04—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps
    • C10G65/08—Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including only refining steps at least one step being a hydrogenation of the aromatic hydrocarbons
    • 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
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)

Claims (19)

1. Fremgangsmade til omdannelse af ramateriale omfattende materialer af bi-ologisk oprindelse til carbonhydrider, hvilken fremgangsmade omfatter trin-nene,hvor - ramateriale omfattende mindst et materiale af biologisk oprindelse udsasttes forfordampningsbehandling til opnaelse af oprenset ramateriale, - det oprensede ramateriale udsasttes for hydrobehandling, der udfores i to trin, hvor det oprensede ramateriale i det forste hydrobehandlingstrin bringes i kontakt med mindst en hydrodeoxygeneringskatalysator omfattende NiMo, CoMo eller en blanding af Ni, Mo og Co og med mindst en hydroafvoksnings-katalysator omfattende NiW, ved en temperatur pa 330 - 430 °C, til opnaelse af et produkt fra det forste hydrobehandlingstrin, - produktetfra det forste hydrobehandlingstrin i det andet hydrobehandlingstrin bringes i kontakt med mindst en hydrodearomatiseringskatalysator omfattende metaller udvalgt blandt Pt, Pd, Ir, Ru, Rh, Re, Ni, Co, Mo, W, CoMo, NiMo og NiW, ved en temperatur pa 180 - 350 °C, til opnaelse af et hydrobehandlings-produkt, og - hvor hydrodearomatiseringen udfores efter hydrodeoxygenering og hydro-afvoksning.
2. Fremgangsmade ifolge krav 1, hvor fordampningsbehandlingen udfores i en fordampningsenhed omfattende mindst en fordamper, fortrinsvis tre eller fire fordampere.
3. Fremgangsmade ifolge krav 1 eller 2, hvor det oprensede ramateriale udsasttes for forbehandling, der udfores under anvendelse af superkritisk eks-traktionsteknologi eller med et eller fiere beskyttelseslejer.
4. Fremgangsmade ifolge krav 3, hvor beskyttelseslejerne er udvalgt blandt aktive beskyttelseslejer, inaktive beskyttelseslejer og kombinationer deraf.
5. Fremgangsmade ifolge et hvilket som helst af kravene 1-4, hvor hydrobe-handlingen udfores under et tryk pa 5 - 200 bar.
6. Fremgangsmade if0lge et hvilket som helst af kravene 1-5, hvor hydrobe-handlingen udfores i et hydrobehandlingsreaktorsystem omfattende mindst to katalysatorlejer, hvor det forste katalysatorleje omfatter en kombination af hy-drodeoxygenerings- og hydroafvoksningskatalysatorer, og det andet katalysatorleje omfatter hydrodearomatiseringskatalysator(er).
7. Fremgangsmade ifolge et hvilket som helst af kravene 1-6, hvor hydrobe-handlingen udfores i et hydrobehandlingsreaktorsystem omfattende tre eller fiere katalysatorlejer, hvor det/de forste katalysator leje(r) omfatter en hydro-deoxygeneringskatalysator eller en kombination af hydrodeoxygenerings- og hydroafvoksningskatalysatorer, det/de anden katalysatorleje(r) omfatter hy-droafvoksningskatalysator(er), og det/de tredje katalysatorleje(r) omfatter hy-drodearomatiseringskatalysator(er).
8. Fremgangsmade ifolge et hvilket som helst af kravene 1-7, hvor hydrobe-handlingen udfores i et hydrobehandlingsreaktorsystem omfattende tre eller fiere katalysatorlejer, hvor hydrodeoxygenerings-, hydroafvoksnings- og hy-drodearomatiseringskatalysatorer hver er anbragt i separate katalysatorlejer.
9. Fremgangsmade ifolge et hvilket som helst af kravene 1-8, hvortrykket i det forste hydrobehandlingstrin er 50-180 bar, fortrinsvis 70-120 bar, og trykket i det andet hydrobehandlingstrin er 5 -110 bar, fortrinsvis 10-90 bar.
10. Fremgangsmade ifolge et hvilket som helst af kravene 6-9, hvor hydrobe-handlingsreaktorsystemet i det forste hydrobehandlingstrin omfatter mindst et katalysatorleje, der omfatter en kombination af hydrodeoxygenerings- og hydroafvoksningskatalysatorer, eller to eller fiere katalysatorlejer, der omfatter kombinationer af hydrodeoxygenerings- og hydroafvoksningskatalysatorer, eller katalysatorlejer, der omfatter hydrodeoxygeneringskatalysatorer, og katalysatorlejer, der omfatter hydroafvoksningskatalysatorer, eller kombinationer af nasvnte katalysatorlejer, og hydrobehandlingsreaktorsystemet i det andet hydrobehandlingstrin omfatter mindst et katalysatorleje, der omfatter en hydro-dearomatiseringskatalysator.
11. Fremgangsmade if0lge et hvilket som helst af kravene 1 -10, hvor et hydro-behandlingsprodukt, efter hydrobehandlingen eller efter det forste hydrobe-handlingstrin, udsasttes forfraktionering til opnaelse af carbonhydridfraktioner, som koger i flydende brasndstof-omraderne, og en tung rest.
12. Fremgangsmade ifolge krav 11, hvor mindst en af fraktionerne udsasttes for det andet hydrobehandlingstrin i nasrvasr af mindst en hydrodearomatise-ringskatalysator.
13. Fremgangsmade ifolge krav 11 eller 12, hvor mindst en del af en tung rest recirkuleres til det oprensede ramateriale.
14. Fremgangsmade ifolge et hvilket som helst af kravene 1-13, hvor hydro-deoxygeneringskatalysatoren omfatter mindst et metal udvalgt blandt NiMo, CoMo og blandinger af Ni, Mo og Co og mindst en basrer udvalgt blandt AI2O3, S1O2, ZrÜ2 og blandinger deraf.
15. Fremgangsmade ifolge et hvilket som helst af kravene 1-14, hvor hydro-deoxygeneringskatalysatoren er udvalgt blandt N1M0/AI2O3, NiMo/Si02, C0M0/AI2O3, C0M0/S1O2 N1M0C0/AI2O3 og NiMoCo/Si02.
16. Fremgangsmade ifolge et hvilket som helst af kravene 1-15, hvor hydro-afvoksningskatalysatoren omfatter en basrer udvalgt blandt aluminiumsilicat-molekylsigte, zeoliter og oxider.
17. Fremgangsmade ifolge et hvilket som helst af kravene 1-16, hvor hydro-afvoksningskatalysatoren er NiW pa en basrer udvalgt blandt AI2O3, zeolit, ze-olit-Al203 og AI2O3-S1O, fortrinsvis N1W/AI2O3 eller NiW/zeolit/Al203.
18. Fremgangsmade ifolge et hvilket som helst af kravene 1-17, hvor hydro-dearomatiseringskatalysatoren omfatter en basrer udvalgt blandt oxidbasrere, carbon, traskul, zeoliter og kombinationer deraf.
19. Fremgangsmade ifolge et hvilket som helst af kravene 1-18, hvor hydro-dearomatiseringskatalysatoren omfatter Pd og/eller Pt pa zeolit Y/AI2O3, Pd og/eller Pt pa zirconiumdioxid/siliciumdioxid, Pd og/eller Pt pa aluminium-oxid/aluminiumoxid-siliciumdioxid, Pd eller Pt eller Ir pa carbon eller traakul, Pd, Pt, Ir, Ru, Rh og/eller Re pa siliciumdioxid/aluminiumoxid, sulfideret CoMo og NiMo-katalysatorer pa aluminiumoxid/aluminiunnoxid-siliciunndioxid eller Pd-Pt pa AI2O3 - B2O3.
DK14744614.0T 2013-07-12 2014-07-11 Fremgangsmåde til fremstilling af carbonhydrider DK3019577T3 (da)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI20135770A FI126674B (en) 2013-07-12 2013-07-12 Process for the preparation of hydrocarbons
PCT/FI2014/050570 WO2015004329A1 (en) 2013-07-12 2014-07-11 Process for producing hydrocarbons

Publications (1)

Publication Number Publication Date
DK3019577T3 true DK3019577T3 (da) 2018-06-25

Family

ID=51229938

Family Applications (1)

Application Number Title Priority Date Filing Date
DK14744614.0T DK3019577T3 (da) 2013-07-12 2014-07-11 Fremgangsmåde til fremstilling af carbonhydrider

Country Status (11)

Country Link
US (1) US9663720B2 (da)
EP (1) EP3019577B1 (da)
CN (1) CN105378034B (da)
CA (1) CA2915977C (da)
DK (1) DK3019577T3 (da)
ES (1) ES2677116T3 (da)
FI (1) FI126674B (da)
HU (1) HUE038344T2 (da)
PL (1) PL3019577T3 (da)
RU (1) RU2663669C2 (da)
WO (1) WO2015004329A1 (da)

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3095839A1 (en) 2015-05-20 2016-11-23 Total Marketing Services Biodegradable hydrocarbon fluids by hydrogenation
LT3371279T (lt) * 2015-11-04 2020-02-25 Sca Forest Products Ab Angliavandenilių produkto iš lignino alyvos gamybos procesas
FI127519B (en) * 2015-12-31 2018-08-15 Neste Oyj Process for producing high octane fuel component from renewable raw material
EP3342842A1 (en) * 2017-01-03 2018-07-04 Total Marketing Services Dewaxing and dearomating process of hydrocarbon in a slurry reactor
ES2831075T3 (es) * 2017-06-29 2021-06-07 Neste Oyj Método para aumentar la selectividad de destilado medio y gasolina en craqueo catalítico
US10577547B2 (en) 2018-02-27 2020-03-03 Uop Llc Process for producing fuels from a blended biorenewable feed
FI20185412A1 (en) 2018-05-03 2019-11-04 Upm Kymmene Corp Process for the production of renewable fuels
CN108579735A (zh) * 2018-05-28 2018-09-28 中国中化股份有限公司 一种铂-钯双金属加氢脱芳烃催化剂的制备方法
FI128121B (en) 2018-07-20 2019-10-15 Neste Oyj Production of hydrocarbons from recycled or renewable organic material
FI128069B2 (en) 2018-07-20 2024-04-24 Neste Oyj Purification of recycled and renewable organic material
FI128115B2 (en) 2018-07-20 2024-08-20 Neste Oyj Purification of recycled and renewable organic material
FI128911B (en) * 2018-07-20 2021-03-15 Neste Oyj Purification of recycled and renewable organic material
FI128174B (en) 2018-07-20 2019-11-29 Neste Oyj Purification of recycled and renewable organic material
MY204466A (en) 2018-10-24 2024-08-29 Haldor Topsoe As Method for production of aviation fuel
FI128819B (en) * 2019-12-06 2020-12-31 Neste Oyj Process for processing a bio-based material and processed material
EP4423213A1 (en) * 2021-10-26 2024-09-04 Topsoe A/S Process for production of a low-aromatic hydrocarbon from pyrolysis oil
CN119013377A (zh) * 2021-12-30 2024-11-22 耐思特公司 由生物来源的有机材料生产烃
EP4457317A1 (en) * 2021-12-30 2024-11-06 Neste Oyj Middle distillate fuel from organic material of biological origin

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7232935B2 (en) 2002-09-06 2007-06-19 Fortum Oyj Process for producing a hydrocarbon component of biological origin
ITMI20062193A1 (it) * 2006-11-15 2008-05-16 Eni Spa Processo per produrre frazioni idrocarburiche da miscele di origine biologica
ATE493484T1 (de) * 2006-12-01 2011-01-15 Univ North Carolina State Verfahren zur umwandlung von biomasse in treibstoff
US8039682B2 (en) 2008-03-17 2011-10-18 Uop Llc Production of aviation fuel from renewable feedstocks
US8324438B2 (en) * 2008-04-06 2012-12-04 Uop Llc Production of blended gasoline and blended aviation fuel from renewable feedstocks
US8314274B2 (en) 2008-12-17 2012-11-20 Uop Llc Controlling cold flow properties of transportation fuels from renewable feedstocks
US20110099891A1 (en) 2009-11-04 2011-05-05 Exxonmobil Research And Engineering Company Hydroprocessing feedstock containing lipid material to produce transportation fuel
FI128142B (fi) * 2010-02-02 2019-10-31 Upm Kymmene Corp Menetelmä ja laitteisto hiilivetyjen tuottamiseksi
FI125632B (fi) * 2010-05-25 2015-12-31 Upm Kymmene Corp Menetelmä ja laite hiilivetyjen tuottamiseksi
FI125931B (fi) * 2010-05-25 2016-04-15 Upm Kymmene Corp Menetelmä ja laitteisto hiilivetyjen valmistamiseksi
SG185577A1 (en) 2010-06-30 2012-12-28 Exxonmobil Res & Eng Co Gas and liquid phase hydroprocessing for biocomponent feedstocks
FI20106252A0 (fi) 2010-11-26 2010-11-26 Upm Kymmene Corp Menetelmä ja systeemi polttoainekomponenttien valmistamiseksi
EP2699652B9 (en) * 2011-04-18 2023-10-25 UPM-Kymmene Corporation Catalytic process for producing hydrocarbons from biooils
FR2982271B1 (fr) 2011-11-08 2013-11-08 Ifp Energies Now Production de carburants paraffiniques a partir de matieres renouvelables par un procede d'hydrotraitement en continu comprenant une etape de pretraitement sous hydrogene

Also Published As

Publication number Publication date
WO2015004329A1 (en) 2015-01-15
ES2677116T3 (es) 2018-07-30
CA2915977A1 (en) 2015-01-15
EP3019577B1 (en) 2018-04-18
US9663720B2 (en) 2017-05-30
HUE038344T2 (hu) 2018-10-29
FI20135770L (fi) 2015-01-13
CN105378034B (zh) 2018-07-03
PL3019577T3 (pl) 2018-09-28
CN105378034A (zh) 2016-03-02
FI126674B (en) 2017-03-31
RU2663669C2 (ru) 2018-08-08
EP3019577A1 (en) 2016-05-18
CA2915977C (en) 2021-10-26
RU2016102730A (ru) 2017-08-16
US20160130509A1 (en) 2016-05-12

Similar Documents

Publication Publication Date Title
DK3019577T3 (da) Fremgangsmåde til fremstilling af carbonhydrider
CA2927863C (en) Process for producing hydrocarbons from crude tall oil and tall oil pitch
FI127491B (fi) Järjestelmä polttoainekomponenttien tuottamiseksi
CA2870831C (en) Process for purification of biological feed material
US10011785B2 (en) Integrated process for producing hydrocarbons
FI127333B (en) Process for the preparation of hydrocarbons
FI128374B (en) Process for the production of hydrocarbons
US20250066676A1 (en) Method for producing renewable aviation fuel