FI126812B - Integroitu prosessi hiilivetyjen valmistamiseksi - Google Patents

Integroitu prosessi hiilivetyjen valmistamiseksi Download PDF

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FI126812B
FI126812B FI20136163A FI20136163A FI126812B FI 126812 B FI126812 B FI 126812B FI 20136163 A FI20136163 A FI 20136163A FI 20136163 A FI20136163 A FI 20136163A FI 126812 B FI126812 B FI 126812B
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hydrogen
hydrocarbons
stream
integrated process
recycle stream
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FI20136163A
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English (en)
Swedish (sv)
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FI20136163A (fi
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Isto Eilos
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Upm Kymmene Corp
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First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=52002993&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=FI126812(B) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Upm Kymmene Corp filed Critical Upm Kymmene Corp
Priority to FI20136163A priority Critical patent/FI126812B/fi
Priority to DK14805967.8T priority patent/DK3071670T3/da
Priority to CA2930797A priority patent/CA2930797C/en
Priority to HRP20220054TT priority patent/HRP20220054T1/hr
Priority to US15/035,873 priority patent/US10011785B2/en
Priority to HUE14805967A priority patent/HUE057530T2/hu
Priority to ES14805967T priority patent/ES2906240T3/es
Priority to PT148059678T priority patent/PT3071670T/pt
Priority to EP21201833.7A priority patent/EP3971265A1/en
Priority to PCT/FI2014/050889 priority patent/WO2015075315A1/en
Priority to PL14805967T priority patent/PL3071670T3/pl
Priority to EP14805967.8A priority patent/EP3071670B1/en
Publication of FI20136163A publication Critical patent/FI20136163A/fi
Publication of FI126812B publication Critical patent/FI126812B/fi
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Claims (23)

1. Integroitu prosessi hiilivetyjen valmistamiseksi, mainitun prosessin käsittäessä vaiheet, missä uusiutuvista lähteistä peräisin olevalle syötteelle suoritetaan katalyyttinen vetyprosessointi vetyprosessointijärjestelmässä vedyn läsnä ollessa vedyn osapaineessa alueella 25 - 250 bar, sen jälkeen erotetaan vesipitoinen komponentti, raskas komponentti, joka käsittää hiililuvultaan yli 5 olevia hiilivetyjä, ja kevyt komponentti, joka käsittää kaasuja ja hiililuvultaan välillä 1-5 olevia hiilivetyjä, johdetaan mainittu kevyt komponentti erotukseen hiilidioksidin ja rikkivedyn poistamiseksi, jolloin saadaan vetyä ja hiililuvultaan välillä 1-5 olevia hiilivetyjä käsittävä kierrätysvirta, sitten kierrätysvirta jaetaan ensimmäiseen kierrätysvirtaan ja toiseen kierrätysvirtaan, johdetaan ensimmäinen kierrätysvirta vetyprosessointijärjestelmään, ja toinen kierrätysvirta höyryreformointiyksikön, ennen höyryreformointiyksikköä sijaitsevan rikinpoistoyksikön ja vesi-kaasumuunnosyksikön käsittävään vetylaitokseen, konvertoidaan mainitut hiililuvultaan välillä 1-5 olevat hiilivedyt mainitussa vetylaitoksessa vedyksi, ja johdetaan mainittua vetyä käsittävä vetyvirta vetyprosessointijärjestelmään.
2. Patenttivaatimuksen 1 mukainen integroitu prosessi hiilivetyjen valmistamiseksi, missä maakaasua, LPG:a, naftaa, biokaasua, metaania, etaania, propaania, butaania tai näiden yhdistelmää käytetään vetylaitoksen lähtöaineena.
3. Patenttivaatimuksen 2 mukainen integroitu prosessi hiilivetyjen valmistamiseksi, missä toinen kierrätysvirta johdetaan vetylaitoksen rikinpoistoyksikköön ja rikkiyhdisteet poistetaan lähtöaineesta.
4. Jonkin patenttivaatimuksen 1-3 mukainen integroitu prosessi hiilivetyjen valmistamiseksi, missä vetylaitos käsittää hiilidioksidin/hiilimonoksidin/veden erotusyksikön.
5. Jonkin patenttivaatimuksen 1-4 mukainen integroitu prosessi hiilivetyjen valmistamiseksi, missä ensimmäinen kierrätysvirta yhdistetään vetyvirran kanssa, jolloin saadaan yhdistetty virta, ja hiililuvultaan välillä 1-5 olevien hiilivetyjen määrä yhdistetyssä virrassa säädetään alueelle enintään 30 mooli-%, laskettuna vetyprosessointijärjestelmän syötteen kokonaismäärästä.
6. Patenttivaatimuksen 5 mukainen integroitu prosessi hiilivetyjen valmistamiseksi, missä hiililuvultaan välillä 1-5 olevat hiilivedyt käsittävät metaania.
7. Jonkin patenttivaatimuksen 1-6 mukainen integroitu prosessi hiilivetyjen valmistamiseksi, missä kevyelle komponentille suoritetaan erotus käyttäen yhtä tai useampaa amiinipesuria, joka kykenee poistamaan rikkivetyä ja hiilidioksidia.
8. Jonkin patenttivaatimuksen 1-7 mukainen integroitu prosessi hiilivetyjen valmistamiseksi, missä vesipitoisen komponentin, raskaan komponentin ja kevyen komponentin erotus suoritetaan kylmäerottimen avulla.
9. Jonkin patenttivaatimuksen 1-8 mukainen integroitu prosessi hiilivetyjen valmistamiseksi, missä raskaalle komponentille suoritetaan erotus ja/tai fraktionointi, jolloin saadaan liikennepolttoaineiden alueella kiehuvia hiilivetyjä.
10. Jonkin patenttivaatimuksen 1-9 mukainen integroitu prosessi hiilivetyjen valmistamiseksi, missä uusiutuvista lähteistä peräisin oleva syöte valitaan kasveista, eläimistä, levistä, kaloista ja mikrobiologisista prosesseista peräisin olevista syötteistä, mainittujen syötteiden prosessoinnista peräsin olevista sivuvirroista ja jätevirroista, ja viemärilietteestä.
11. Jonkin patenttivaatimuksen 1-10 mukainen integroitu prosessi hiilivetyjen valmistamiseksi, missä syöte käsittää kasviöljyä tai metsäteollisuuden sivutuotteina saatavia yhdisteitä, tai näiden yhdistelmiä.
12. Jonkin patenttivaatimuksen 1-11 mukainen integroitu prosessi hiilivetyjen valmistamiseksi, missä vedyn osapaine katalyyttisessä vetyprosessoinnissa on alueella 60 - 200 bar, edullisesti 80 - 150 bar.
13. Jonkin patenttivaatimuksen 1-12 mukainen integroitu prosessi hiilivetyjen valmistamiseksi, missä katalyyttisessä vetyprosessoinnissa kokonaispaine on alueella 25 - 250 bar, edullisesti 80 - 160 bar.
14. Jonkin patenttivaatimuksen 1-13 mukainen integroitu prosessi hiilivetyjen valmistamiseksi, missä katalyyttinen vetyprosessointi suoritetaan alueella 280 -450°C olevassa lämpötilassa.
15. Jonkin patenttivaatimuksen 1-14 mukaisella prosessilla saatava hiilivetytuote.
16. Integroitu prosessi hiililuvultaan välillä 1-5 olevien hiilivetyjen konvertoimiseksi, missä mainittu prosessi käsittää vaiheet, missä uusiutuvista lähteistä peräisin olevalle syötteelle suoritetaan katalyyttinen vetyprosessointi vetyprosessointijärjestelmässä vedyn läsnä ollessa vedyn osapaineessa alueella 25 - 250 bar, sen jälkeen erotetaan vesipitoinen komponentti, raskas komponentti, joka käsittää hiililuvultaan yli 5 olevia hiilivetyjä, ja kevyt komponentti, joka käsittää kaasuja ja hiililuvultaan välillä 1-5 olevia hiilivetyjä, johdetaan mainittu kevyt komponentti erotukseen hiilidioksidin ja rikkivedyn poistamiseksi, jolloin saadaan vetyä ja hiililuvultaan välillä 1-5 olevia hiilivetyjä käsittävä kierrätysvirta, sitten kierrätysvirta jaetaan ensimmäiseen kierrätysvirtaan ja toiseen kierrätysvirtaan, johdetaan ensimmäinen kierrätysvirta vetyprosessointijärjestelmään, ja toinen kierrätysvirta höyryreformointiyksikön, ennen höyryreformointiyksikköä sijaitsevan rikinpoistoyksikön ja vesi-kaasumuunnosyksikön käsittävään vetylaitokseen, konvertoidaan mainitut hiililuvultaan välillä 1-5 olevat hiilivedyt mainitussa vetylaitoksessa vedyksi.
17. Patenttivaatimuksen 16 mukainen integroitu prosessi hiililuvultaan välillä 1-5 olevien hiilivetyjen konvertoimiseksi, missä mainitussa vetylaitoksessa konvertoitua vetyä käsittävä vetyvirta johdetaan vetyprosessointijärjestelmään.
18. Patenttivaatimuksen 16 tai 17 mukainen integroitu prosessi hiililuvultaan välillä 1-5 olevien hiilivetyjen konvertoimiseksi, missä maakaasua, LPG:a, naftaa, biokaasua, metaania, etaania, propaania, butaania tai näiden yhdistelmää käytetään vetylaitoksen lähtöaineena.
19. Patenttivaatimuksen 18 mukainen integroitu prosessi hiililuvultaan välillä 1-5 olevien hiilivetyjen konvertoimiseksi, missä toinen kierrätysvirta johdetaan vetylaitoksen rikinpoistoyksikköön ja rikkiyhdisteet poistetaan lähtöaineesta.
20. Jonkin patenttivaatimuksen 16 - 19 mukainen integroitu prosessi hiililuvultaan välillä 1-5 olevien hiilivetyjen konvertoimiseksi, missä vetylaitos käsittää hiilidioksidin/hiilimonoksidin/veden erotusyksikön.
21. Jonkin patenttivaatimuksen 16 - 20 mukainen integroitu prosessi hiililuvultaan välillä 1-5 olevien hiilivetyjen konvertoimiseksi, missä kevyelle komponentille suoritetaan erotus käyttäen yhtä tai useampaa amiinipesuria, joka kykenee poistamaan rikkivetyä ja hiilidioksidia.
22. Jonkin patenttivaatimuksen 16 - 21 mukainen integroitu prosessi hiililuvultaan välillä 1-5 olevien hiilivetyjen konvertoimiseksi, missä uusiutuvista lähteistä peräisin oleva syöte valitaan kasveista, eläimistä, levistä, kaloista ja mikrobiologisista prosesseista peräisin olevista syötteistä, mainittujen syötteiden prosessoinnista peräsin olevista sivuvirroista ja jätevirroista, ja viemäri lietteestä.
23. Jonkin patenttivaatimuksen 16 - 22 mukainen integroitu prosessi hiililuvultaan välillä 1-5 olevien hiilivetyjen konvertoimiseksi, missä syöte käsittää kasviöljyä tai metsäteollisuuden sivutuotteina saatavia yhdisteitä, tai näiden yhdistelmiä.
FI20136163A 2013-11-21 2013-11-21 Integroitu prosessi hiilivetyjen valmistamiseksi FI126812B (fi)

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FI20136163A FI126812B (fi) 2013-11-21 2013-11-21 Integroitu prosessi hiilivetyjen valmistamiseksi
ES14805967T ES2906240T3 (es) 2013-11-21 2014-11-20 Procedimiento integrado para producir hidrocarburos
EP21201833.7A EP3971265A1 (en) 2013-11-21 2014-11-20 Integrated process for producing hydrocarbons
HRP20220054TT HRP20220054T1 (hr) 2013-11-21 2014-11-20 Integrirani postupak proizvodnje ugljikovodika
US15/035,873 US10011785B2 (en) 2013-11-21 2014-11-20 Integrated process for producing hydrocarbons
HUE14805967A HUE057530T2 (hu) 2013-11-21 2014-11-20 Integrált eljárás szénhidrogének elõállítására
DK14805967.8T DK3071670T3 (da) 2013-11-21 2014-11-20 Integreret fremgangsmåde til fremstilling af carbonhydrider
PT148059678T PT3071670T (pt) 2013-11-21 2014-11-20 Processo integrado para produzir hidrocarbonetos
CA2930797A CA2930797C (en) 2013-11-21 2014-11-20 Integrated process for producing hydrocarbons
PCT/FI2014/050889 WO2015075315A1 (en) 2013-11-21 2014-11-20 Integrated process for producing hydrocarbons
PL14805967T PL3071670T3 (pl) 2013-11-21 2014-11-20 Zintegrowany sposób wytwarzania węglowodorów
EP14805967.8A EP3071670B1 (en) 2013-11-21 2014-11-20 Integrated process for producing hydrocarbons

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US20160289576A1 (en) 2016-10-06
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PL3071670T3 (pl) 2022-03-07
CA2930797C (en) 2022-01-04
HUE057530T2 (hu) 2022-05-28
FI20136163A (fi) 2015-05-22
PT3071670T (pt) 2021-12-06
WO2015075315A1 (en) 2015-05-28
ES2906240T3 (es) 2022-04-13
CA2930797A1 (en) 2015-05-28
EP3971265A1 (en) 2022-03-23
EP3071670B1 (en) 2021-11-17
EP3071670A1 (en) 2016-09-28

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