FI122786B - Användning av i framställningen av syntetiska kolvätekedjor uppkommen koldioxid - Google Patents

Användning av i framställningen av syntetiska kolvätekedjor uppkommen koldioxid Download PDF

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Publication number
FI122786B
FI122786B FI20075557A FI20075557A FI122786B FI 122786 B FI122786 B FI 122786B FI 20075557 A FI20075557 A FI 20075557A FI 20075557 A FI20075557 A FI 20075557A FI 122786 B FI122786 B FI 122786B
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Finland
Prior art keywords
carbon dioxide
dioxide stream
calcium
bar
production
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FI20075557A
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English (en)
Finnish (fi)
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FI20075557A0 (sv
FI20075557A (sv
Inventor
Markku Karlsson
Esko Kukkamaeki
Pekka Jokela
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Upm Kymmene Oyj
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First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=38331645&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=FI122786(B) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Upm Kymmene Oyj filed Critical Upm Kymmene Oyj
Priority to FI20075557A priority Critical patent/FI122786B/sv
Publication of FI20075557A0 publication Critical patent/FI20075557A0/sv
Priority to US12/669,769 priority patent/US9434615B2/en
Priority to EP08775217.6A priority patent/EP2190950B1/en
Priority to PCT/EP2008/059440 priority patent/WO2009013232A2/en
Priority to PCT/FI2008/050438 priority patent/WO2009013392A2/en
Priority to US12/669,767 priority patent/US20100288458A1/en
Priority to CN200880107652A priority patent/CN101802142A/zh
Priority to CA 2696867 priority patent/CA2696867A1/en
Priority to US12/669,764 priority patent/US9133027B2/en
Priority to CN200880025115A priority patent/CN101848979A/zh
Priority to EP16187479.7A priority patent/EP3135747B1/en
Priority to PL16187479T priority patent/PL3135747T3/pl
Priority to DK08775217.6T priority patent/DK2190950T3/en
Priority to RU2010121237/04A priority patent/RU2459857C2/ru
Priority to JP2010517429A priority patent/JP2010534184A/ja
Priority to PL08775217T priority patent/PL2190950T3/pl
Priority to CA 2696860 priority patent/CA2696860A1/en
Priority to EP08775216.8A priority patent/EP2185670B1/en
Priority to CA2693401A priority patent/CA2693401C/en
Priority to ES16187479T priority patent/ES2873524T3/es
Priority to KR20107003762A priority patent/KR101435991B1/ko
Priority to ES08775217.6T priority patent/ES2603281T3/es
Priority to EP08787711A priority patent/EP2179009A2/en
Priority to BRPI0814273 priority patent/BRPI0814273A2/pt
Priority to PCT/EP2008/059441 priority patent/WO2009013233A2/en
Priority to CN200880107048A priority patent/CN101802141A/zh
Priority to DK16187479.7T priority patent/DK3135747T3/da
Publication of FI20075557A publication Critical patent/FI20075557A/sv
Priority to ZA201001128A priority patent/ZA201001128B/xx
Publication of FI122786B publication Critical patent/FI122786B/sv
Application granted granted Critical

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    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
    • C01B3/52—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with liquids; Regeneration of used liquids
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    • C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00—Compounds of calcium, strontium, or barium
    • C01F11/18—Carbonates
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    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
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    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/48—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents followed by reaction of water vapour with carbon monoxide
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    • C10G2/00—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon
    • C10G2/30—Production of liquid hydrocarbon mixtures of undefined composition from oxides of carbon from carbon monoxide with hydrogen
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    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
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    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46—Gasification of granular or pulverulent flues in suspension
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    • C10J3/50—Fuel charging devices
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    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
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    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72—Other features
    • C10J3/82—Gas withdrawal means
    • C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63—Inorganic compounds
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    • C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
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    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
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    • C10J2300/16—Integration of gasification processes with another plant or parts within the plant
    • C10J2300/164—Integration of gasification processes with another plant or parts within the plant with conversion of synthesis gas
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Claims (34)

1. Användning av en koldioxidström, som uppkommit vid syreförgasning av organisk materia, för karbonisering av kalcium ur en lösning innehällande kalciumjoner. 5
2. Användning av en koldioxidström enligt patentkrav 1 kännetecknad av att nämnda koldioxidström uppkommer som en biprodukt vid framställning av syntetiska kolvätekedjor.
3. Användning av en koldioxidström enligt patentkrav 2 kännetecknad av att nämnda framställning av syntetiska kolvätekedjor omfattar produktion av biobränslen.
4. Användning av en koldioxidström enligt patentkrav 2 eller 3 kännetecknad 15 av att framställningen av syntetiska kolvätekedjor omfattar användning av fysikalisk rengöring som kräver trycksatt syntesgasblandning och/eller Fischer-Tropsch-syntes.
5. Användning av en koldioxidström enligt nägot av de föregäende patentkraven 20 kännetecknad av att nämnda organiska materia är biomassa säsom träbaserat material, jordbruksavfall, biprodukter fran skogsindustrin, avloppsslam fran skogsindustrin eller kommunalt avfall.
6. Användning av en koldioxidström enligt patentkrav 5 kännetecknad av att 25 nämnda träbaserade material omfattar träbaserade biprodukter som bildats i samband med skogsskötsel och skogsavverkning sasom utgallringsvirke, oj stubbar, rotstockar, grenar, kvistar och bark. δ CM
7. Användning av en koldioxidström enligt nägot av de föregäende patentkraven O q 30 kännetecknad av att renheten av koldioxidströmmen är över 90 %, c\] fördelaktigt över 95 %, mer fördelaktigt över 97 % och mest fördelaktigt över £ 99 %. l^. tn tn tn h-· o o CM
8. Användning av en koldioxidström enligt nagot av de föregäende patentkraven kännetecknad av att koldioxidströmmens tryck är over 5 bar, fördelaktigt over 10 bar, mer fördelaktigt över 20 bar, mest fördelaktigt över 30 bar.
9. Användning av en koldioxidström enligt nagot av de föregäende patentkraven kännetecknad av att koldioxidströmmen innehaller under 1 ppm svavel.
10. Användning av en koldioxidström enligt nagot av de föregäende patentkraven kännetecknad av att nämnda koldioxidström innehaller under 10 % kväve, 10 fördelaktigt under 5 %, mer fördelaktigt under 3 %, mest fördelaktigt under 1 %.
11. Användning av en koldioxidström enligt nagot av de föregäende patentkraven kännetecknad av att kalcium karboniseras i en kontinuerlig reaktor. 15
12. Användning av en koldioxidström patentkrav 11 kännetecknad av att trycket i den kontinuerliga reaktorn är över 5 bar, fördelaktigt över 10 bar, mer fördelaktigt över 20 bar, mest fördelaktigt 20-30 bar.
13. Användning av en koldioxidström enligt nagot av patentkraven 1-10 kännetecknad av att kalcium karboniseras i en satsreaktor eller i en halvkontinuerlig reaktor.
14. Användning av en koldioxidström enligt nagot av patentkraven 1-10 25 kännetecknad av att kalcium karboniseras in-situ i en pappersframställningsprocess. CM
15. Användning av en koldioxidström enligt nagot av de föregäende patentkraven 4· kännetecknad av att förgasningen av organisk materia är integrerad med O q 30 karboniseringen av kalcium för att fa den uppkomna koldioxidströmmen i 00 nyttobruk. x X CL
16. Användning av en koldioxidström enligt nagot av patentkraven 1-14 tn kännetecknad av att förgasningen av organisk materia och karboniseringen Is- o o CM av kalcium sker pa samma fabriksomräde för att koldioxidens tryck skall kurina utnyttjas.
17. Ett förfarande för framställning av papper eller kartong, kännetecknat av att 5 man för att karbonisera kalcium förgasar organisk materia med syre, later den uppkomna koldioxidströmmen reagera med en lösning innehallande kalciumjoner, och tillsätter det karboniserade kalciumet som fyllnadsämne i maiden i samband med pappers- och kartongframställningen och/eller som bestrykning pä 10 färdigt papper.
18. Förfarande enligt patentkrav 17 kännetecknat av att nämnda koldioxidström uppkommer som en biprodukt vid framställning av syntetiska kolvätekedjor. 15
19. Förfarande enligt patentkrav 18 kännetecknat av att nämnda framställning av syntetiska kolvätekedjor omfattar produktion av biobränslen.
20. Förfarande enligt patentkrav 18 eller 19 kännetecknat av att syntesgasblandningen som erhallits fran nämnda syreförgasning rengörs med 20 en fysikalisk rengöring som kräver trycksättning av syntesgasblandningen och/eller nämnda syntetiska kolvätekedjor bildas med Fischer-Tropsch-syntes.
21. Förfarande enligt nagot av patentkraven 17-20 kännetecknat av att nämnda 25 organiska materia är biomassa sasom träbaserat material, jordbruksavfall, biprodukter fran skogsindustrin, avloppsslam fran skogsindustrin eller c\j kommunalt avfall. δ CM 4
22. Förfarande enligt patentkrav 21 kännetecknat av att nämnda träbaserade o q 30 material omfattar träbaserade biprodukter som bildats i samband med CM o skogsskötsel och skogsavverkning sasom utgallringsvirke, stubbar, X £ rotstockar, grenar, kvistar och bark. N· LO LO LO N- o o CM
23. Förfarande enligt nägot av patentkraven 17-22 kännetecknat av att renheten av koldioxidströmmen är över 90 %, fördelaktigt över 95 %, mer fördelaktigt över 97 % och mest fördelaktigt över 99 %. 5
24. Förfarande enligt nägot av patentkraven 17-23 kännetecknat av att koldioxidströmmens tryck är över 5 bar, fördelaktigt över 10 bar, mer fördelaktigt över 20 bar, mest fördelaktigt över 30 bar.
25. Förfarande enligt nägot av patentkraven 17-24 kännetecknat av att 10 koldioxidströmmen innehäller under 1 ppm svavel.
26. Förfarande enligt nägot av patentkraven 17-25 kännetecknat av att nämnda koldioxidström innehäller under 10 % kväve, fördelaktigt under 5 %, mer fördelaktigt under 3 %, mest fördelaktigt under 1 %. 15
27. Förfarande enligt nägot av patentkraven 17-26 kännetecknat av att karboniseringen av kalcium justeras enligt behoven vid pappersframställningen och användningen av nämnda koldioxidström justeras enligt behovet av kalciumkarbonat.
28. Förfarande enligt nägot av patentkraven 17-27 kännetecknat av att kalcium karboniseras i en kontinuerlig reaktor.
29. Förfarande enligt patentkrav 28 kännetecknat av att trycket i den 25 kontinuerliga reaktorn är över 5 bar, fördelaktigt över 10 bar, mer fördelaktigt över 20 bar, mest fördelaktigt 20-30 bar. CM o
30. Förfarande enligt patentkrav 28 eller 29 kännetecknat av att nämnda 4 kontinuerliga reaktor är kombinerad med pappersframställningsprocessen. o o 30
31. Förfarande enligt nägot av patentkraven 17-27 kännetecknat av att kalcium x £ karboniseras i en satsreaktor eller en halvkontinuerlig reaktor. r*» m
32. Förfarande enligt nägot av patentkraven 17-27 kännetecknat av att kalcium r- g 35 karboniseras in-situ i pappersframställningsprocessen. CM
33. Förfarande enligt nagot av patentkraven 17-32 kännetecknat av att förgasningen av organisk materia är integrerad med karboniseringen av kalcium för att fä den uppkomna koldioxidströmmen i nyttobruk. 5
34. Förfarande enligt nagot av patentkraven 17-32 kännetecknat av att förgasningen av organisk materia och karboniseringen av kalcium sker pa samma fabriksomrade. cvj δ CM M" O O cvj X cc CL t'- LO LO LO o o CVJ
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FI20075557A FI122786B (sv) 2007-07-20 2007-07-20 Användning av i framställningen av syntetiska kolvätekedjor uppkommen koldioxid
DK16187479.7T DK3135747T3 (da) 2007-07-20 2008-07-18 Fremgangsmåde og apparat til fremstilling af flydende hydrokulstofholdigt produkt fra fast biomasse
RU2010121237/04A RU2459857C2 (ru) 2007-07-20 2008-07-18 Способ и устройство для получения жидкого биотоплива из твердой биомассы
CA 2696860 CA2696860A1 (en) 2007-07-20 2008-07-18 Method and apparatus for producing synthesis gas from biomass
PCT/EP2008/059440 WO2009013232A2 (en) 2007-07-20 2008-07-18 Method and apparatus for producing synthesis gas from biomass
PCT/FI2008/050438 WO2009013392A2 (en) 2007-07-20 2008-07-18 Use of carbon dioxide generated in manufacturing synthetic hydrocarbon chains
US12/669,767 US20100288458A1 (en) 2007-07-20 2008-07-18 Use of carbon dioxide generated in manufacturing synthetic hydrocarbon chains
CN200880107652A CN101802142A (zh) 2007-07-20 2008-07-18 用于由生物物质制备合成气的方法和设备
CA 2696867 CA2696867A1 (en) 2007-07-20 2008-07-18 Use of carbon dioxide generated in manufacturing synthetic hydrocarbon chains
US12/669,764 US9133027B2 (en) 2007-07-20 2008-07-18 Method and apparatus for producing synthesis gas from biomass
CN200880025115A CN101848979A (zh) 2007-07-20 2008-07-18 由固体生物质生产液体生物燃料的方法和装置
EP16187479.7A EP3135747B1 (en) 2007-07-20 2008-07-18 Method and apparatus for producing liquid hydrocarbonaceous product from solid biomass
PL16187479T PL3135747T3 (pl) 2007-07-20 2008-07-18 Sposób i urządzenie do wytwarzania ciekłego produktu węglowodorowego ze stałej biomasy
DK08775217.6T DK2190950T3 (en) 2007-07-20 2008-07-18 Method and apparatus for production of liquid biofuel from solid biomass
US12/669,769 US9434615B2 (en) 2007-07-20 2008-07-18 Method and apparatus for producing liquid biofuel from solid biomass
JP2010517429A JP2010534184A (ja) 2007-07-20 2008-07-18 合成炭化水素鎖の製造において発生する二酸化炭素の使用
PL08775217T PL2190950T3 (pl) 2007-07-20 2008-07-18 Sposób i urządzenie do wytwarzania ciekłego biopaliwa ze stałej biomasy
EP08775217.6A EP2190950B1 (en) 2007-07-20 2008-07-18 Method and apparatus for producing liquid biofuel from solid biomass
EP08775216.8A EP2185670B1 (en) 2007-07-20 2008-07-18 Method and apparatus for producing synthesis gas from biomass
CA2693401A CA2693401C (en) 2007-07-20 2008-07-18 Method and apparatus for producing liquid biofuel from solid biomass
ES16187479T ES2873524T3 (es) 2007-07-20 2008-07-18 Procedimiento y aparato para producir producto hidrocarbonoso líquido a partir de biomasa sólida
KR20107003762A KR101435991B1 (ko) 2007-07-20 2008-07-18 합성 탄화수소 쇄의 제조에서 발생되는 이산화탄소의 용도
ES08775217.6T ES2603281T3 (es) 2007-07-20 2008-07-18 Procedimiento y aparato para producir biocombustible líquido a partir de biomasa sólida
EP08787711A EP2179009A2 (en) 2007-07-20 2008-07-18 Use of carbon dioxide generated in manufacturing synthetic hydrocarbon chains
BRPI0814273 BRPI0814273A2 (pt) 2007-07-20 2008-07-18 Uso de uma corrente de dióxido de carbono e processo para preparar papel ou papelão
PCT/EP2008/059441 WO2009013233A2 (en) 2007-07-20 2008-07-18 Method and apparatus for producing liquid biofuel from solid biomass
CN200880107048A CN101802141A (zh) 2007-07-20 2008-07-18 合成烃链生产过程中产生的二氧化碳的应用
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