FI104561B - Förfarande för pyrolys av kolhaltiga råmaterial - Google Patents
Förfarande för pyrolys av kolhaltiga råmaterial Download PDFInfo
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- FI104561B FI104561B FI980456A FI980456A FI104561B FI 104561 B FI104561 B FI 104561B FI 980456 A FI980456 A FI 980456A FI 980456 A FI980456 A FI 980456A FI 104561 B FI104561 B FI 104561B
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- reactor
- regenerator
- cyclone
- unit
- solids
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- 238000000034 method Methods 0.000 title claims abstract description 45
- 238000000197 pyrolysis Methods 0.000 title abstract description 31
- 239000007789 gas Substances 0.000 claims abstract description 45
- 238000006243 chemical reaction Methods 0.000 claims abstract description 31
- 239000002028 Biomass Substances 0.000 claims abstract description 14
- 239000010815 organic waste Substances 0.000 claims abstract description 6
- 239000013618 particulate matter Substances 0.000 claims abstract description 6
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 4
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 4
- 238000000926 separation method Methods 0.000 claims abstract description 4
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 3
- 230000008929 regeneration Effects 0.000 claims abstract 4
- 238000011069 regeneration method Methods 0.000 claims abstract 4
- 239000007787 solid Substances 0.000 claims description 65
- 239000000463 material Substances 0.000 claims description 27
- 238000001035 drying Methods 0.000 claims description 16
- 239000002994 raw material Substances 0.000 claims description 11
- 239000002699 waste material Substances 0.000 claims description 10
- 238000005243 fluidization Methods 0.000 claims description 6
- 239000000446 fuel Substances 0.000 claims description 5
- 240000007817 Olea europaea Species 0.000 claims description 2
- 230000001172 regenerating effect Effects 0.000 claims description 2
- 239000010902 straw Substances 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- 230000000630 rising effect Effects 0.000 claims 2
- 241000209140 Triticum Species 0.000 claims 1
- 235000021307 Triticum Nutrition 0.000 claims 1
- 239000002440 industrial waste Substances 0.000 claims 1
- 230000014759 maintenance of location Effects 0.000 claims 1
- 239000003415 peat Substances 0.000 claims 1
- 238000004148 unit process Methods 0.000 claims 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 abstract description 10
- 238000010348 incorporation Methods 0.000 abstract 1
- 239000000047 product Substances 0.000 description 16
- 239000007858 starting material Substances 0.000 description 12
- 239000007788 liquid Substances 0.000 description 11
- 238000012546 transfer Methods 0.000 description 11
- 239000002245 particle Substances 0.000 description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 9
- 229910052799 carbon Inorganic materials 0.000 description 9
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 239000011236 particulate material Substances 0.000 description 6
- 239000004576 sand Substances 0.000 description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 5
- 239000003570 air Substances 0.000 description 5
- 239000003546 flue gas Substances 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 5
- 238000004064 recycling Methods 0.000 description 5
- 239000003245 coal Substances 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 239000011269 tar Substances 0.000 description 4
- 230000001174 ascending effect Effects 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 3
- 239000000567 combustion gas Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000011551 heat transfer agent Substances 0.000 description 3
- 239000012263 liquid product Substances 0.000 description 3
- 239000011368 organic material Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 239000003575 carbonaceous material Substances 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 230000009089 cytolysis Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000002803 fossil fuel Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000012495 reaction gas Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000003473 refuse derived fuel Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 244000025254 Cannabis sativa Species 0.000 description 1
- 241000218998 Salicaceae Species 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 239000012084 conversion product Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000001722 flash pyrolysis Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 238000003306 harvesting Methods 0.000 description 1
- 150000002605 large molecules Chemical class 0.000 description 1
- 239000012978 lignocellulosic material Substances 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000013502 plastic waste Substances 0.000 description 1
- 239000011120 plywood Substances 0.000 description 1
- 239000012985 polymerization agent Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011027 product recovery Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000004227 thermal cracking Methods 0.000 description 1
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 1
- 238000007158 vacuum pyrolysis Methods 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
Classifications
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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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/0055—Separating solid material from the gas/liquid stream using cyclones
-
- 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
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1845—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with particles moving upwards while fluidised
- B01J8/1854—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with particles moving upwards while fluidised followed by a downward movement inside the reactor to form a loop
-
- 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
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
- C10B49/16—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with moving solid heat-carriers in divided form
- C10B49/20—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with moving solid heat-carriers in divided form in dispersed form
- C10B49/22—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with moving solid heat-carriers in divided form in dispersed form according to the "fluidised bed" technique
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/02—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
-
- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/145—Feedstock the feedstock being materials of biological origin
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Dispersion Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Processing Of Solid Wastes (AREA)
- Cyclones (AREA)
- Carbon And Carbon Compounds (AREA)
- Heterocyclic Carbon Compounds Containing A Hetero Ring Having Nitrogen And Oxygen As The Only Ring Hetero Atoms (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Jellies, Jams, And Syrups (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
Claims (19)
1. Förfarande för termisk konvertering av kolhaltiga rämaterial, valda bland biomassa och organiskt avfall, enligt vilket förfarande 5. rämaterialet inmatas i en reaktor (1-3; 41,42, 52) med fluidiserad bädd, där till- matningen konverteras vid förhöjd temperatur under inverkan av ett partikelfor-migt ämne i fluidiseringstillständ med en fluidiseringsgas, - det partikelformiga ämnet överförs frän reaktom tili en regenerator (24, 28, 29; 43-45) för regenerering och recirkuleras sedan till reaktom efter regenereringen, 10 och - de konverterade kolväteproduktema tas tillvara frän reaktom, kännetecknat avatt - man använder en reaktor (1 - 3) som omfattar ett stigarrör (13; 41) med ett axialt ringformigt tvärsnitt och som är försett med en cyklon (14, 17; 50) med flera in- , 15 lopps-öppningar för separering av det partikelformiga ämnet, och - en regenerator (24, 28, 29; 43-45) som omfattar ett stigarrör (24) med ett axialt ringformigt tvärsnitt och som är koncentriskt anordnat i förhällande tili den an-vända reaktom, varvid sagda regenerator är försedd med en cyklon (25,26; 51) med flera inloppsöppningar. för separation av det regenererade partikelformiga 20 ämnet. 1 2. Förfarande enligt krav 1, kännetecknat avatt reaktom omfattar ett stigarrör med ” ett utrymme (13; 41) mellan tvä innanför varandra liggande, cylindriska och/eller koniska envelopytor. 25
3. Förfarande enligt krav 1 eller 2, kännetecknat av att ängans uppehällstid i pro-cessen uppgär tili 0,1-5 sekunder.
4. Förfarande enligt nägot av kraven 1-3, kännetecknat av att man använder en 30 cyklon (17) med flera inloppsöppningar och med ett ledskovelsystem (14).
5. Förfarande enligt nägot av kraven 1-4, kännetecknat av att reaktom (41, 42, 52) som används är en reaktor med cirkulerande fluidiserad bädd som valbart uppvisar en ka-nal (52) för inre cirkulering. 104561 17
6. Förfarande enligt nägot av kraven 1 tili 5, k ä n n e t e c k n a t av att reaktom (43-45) som används är försedd med en kana! (44) för inre cirkulering.
7. Förfarande enligt nägot av kraven 1 tili 6, k ä n n e t e c k n a t av att regeneratom är 5 försedd med ett sänkrör (29; 45) som stär i kontakt med reaktoms stigarrör.
8. Förfarande enligt nägot av kraven 1 tili 7, kännetecknat av att rämaterialet torkas i en torkningsanordning (46-48) omfattande ett stigarrör (46) med ett axialt ringformigt tvärsnitt och om är försedd med en cyklon (49) med flera inloppsöppningar för separering 10 av torkat material frän de förängade gasema.
9. Förfarande enligt krav 8, kännetecknat av att torkningsanordningen är försedd med ett sänkrör (48), som stär i kontakt med regeneratoms stigarrör (41). 15 10. Förfarande enligt krav 8 eller 9, kännetecknat av att torkanordningen (46-48) är försedd med en kanal (47) för inre cirkulering.
11. Förfarande enligt nägot av kraven 8 tili 10, kännetecknat av att regeneratoms sänkrör (45) stär i kontakt med torkanordningens (46) stigarrör. 20
12. Förfarande enligt nägot av kraven 8 tili 10, kännetecknat av att rämaterialet konverteras termiskt vid en temperatur av 400 - 1000 °C. • · ·
13. Förfarande enligt nägot av de föregäende kraven, kännetecknat av att rämate-25 rialet bestär av skogsbmks- och gallringsrester, jordbruksrester, energigrödor, torv, bränsle av avfall, sägindustriavfall, faneravfall, möbelavfall och och avfall frän annan mekanisk skogsindustri, plastavfall och avfallsslam. m ψ »
14. Förfarande enligt krav 13, kännetecknat av att rämaterialet bestär av halm, 30 olivgallringsrester, vide och energihö. 1 Anordning för termisk konvertering av kolhaltiga rämaterial, vilken anordning omfattar - en torkningsenhet (46-48) för torkning av rämaterialet, 104561 18 - en reaktorenhet (41,42, 52), i vilken rämaterialet bringas i kontakt med hett partikelformigt material i fludiserat tillständ, och - en regeneratorenhet (43-45) för regenerering av partikelformigt material som förorenats i den första enhetsprocessen, 5 kännetecknad avatt - reaktorenheten omfattar ett stigarrör (41) med ett axialt ringformigt tvärsnitt och uppvisande en cyklon (50) med flera inloppsöppningar för separering av fasta ämnen frän gas, och - regeneratorenheten omfattar en reaktor (43,44) med cirkulerande fluidiserad 10 bädd och ett sänkrör (45) anordnat omkring reaktionsenheten (41,42, 52 pä ett symmetriskt sätt, varvid reaktoms stigarrör (43) uppvisar ett axialt ringformigt tvärsnitt och är försett med en cyklon (51) med flera inloppsöppningar för separering av fasta ämnen frän gas och varvid regeneratorenhetens sänkrör (45) star i kontakt med reaktorenhetens stigarrör (41,46) och med torkningsenheten. ; 15
16. Anordning enligt krav 15, kännetecknad avatt regeneratorenheten (43-45) omfattar en kanal (44) för inre cirkulering av fast ämne inom regeneratorenheten.
17. Anordning enligt krav 15 eller 16, kännetecknad avatt reaktionsenheten (41, 20 42, 52) omfattar en kanal (52) för inre cirkulering av fast ämne inom reaktom.
18. Anordning enligt nägot av kraven 15 tili 17, kännetecknad avatt torkningsenheten (46-48) omfattar ett stigarrör (46) anordnat omkring reaktionsenheten pä ett symmet-riski koncentriskt sätt, varvid stigarröret uppvisar ett axialt ringformigt tvärsnitt. 25
19. Anordning enligt krav 18, kännetecknat avatt torkningsenheten (46-48) om- fattar ett sänkrör med ett axialt ringformigt tvärsnitt och stär i kontkt med reaktionsenhe-j . tens stigarrör (41). ...I r Ψ 9
20. Anordning enligt krav 18 eller 19, kännetecknad avatt torkningsenhetens sti garrör (46) är försett med ett organ för separering av gas och fasta ämnen i form av en ; cyklon (49) med flera inloppsöppningar.
Priority Applications (13)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FI980456A FI104561B (sv) | 1998-02-27 | 1998-02-27 | Förfarande för pyrolys av kolhaltiga råmaterial |
| DE69913108T DE69913108T2 (de) | 1998-02-27 | 1999-02-26 | Verfahren zur pyrolyse kohlenstoffhaltiger einspeisungen |
| ES99906280T ES2209399T3 (es) | 1998-02-27 | 1999-02-26 | Procedimiento para la pirolisis de cargas de alimentacion carbonosas. |
| AT99906280T ATE255155T1 (de) | 1998-02-27 | 1999-02-26 | Verfahren zur pyrolyse kohlenstoffhaltiger einspeisungen |
| AU26267/99A AU2626799A (en) | 1998-02-27 | 1999-02-26 | Process for pyrolysing carbonaceous feedstocks |
| US09/623,018 US6814940B1 (en) | 1998-02-27 | 1999-02-26 | Process for pyrolyzing carbonaceous feedstocks |
| PCT/FI1999/000153 WO1999043768A1 (en) | 1998-02-27 | 1999-02-26 | Process for pyrolysing carbonaceous feedstocks |
| EA200000887A EA001850B1 (ru) | 1998-02-27 | 1999-02-26 | Способ пиролиза углеродистого исходного материала |
| IDW20001624A ID28197A (id) | 1998-02-27 | 1999-02-26 | Proses untuk mempirolisis persediaan-persediaan makanan yang mengandung karbon |
| CN99805576A CN1130446C (zh) | 1998-02-27 | 1999-02-26 | 含碳原料的热解方法及其设备 |
| CA002321824A CA2321824C (en) | 1998-02-27 | 1999-02-26 | Process for pyrolysing carbonaceous feedstocks |
| EP99906280A EP1060232B1 (en) | 1998-02-27 | 1999-02-26 | Process for pyrolysing carbonaceous feedstocks |
| BR9908324-8A BR9908324A (pt) | 1998-02-27 | 1999-02-26 | Processo para pirolisação de cargas de alimentação carbonáceas |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FI980456 | 1998-02-27 | ||
| FI980456A FI104561B (sv) | 1998-02-27 | 1998-02-27 | Förfarande för pyrolys av kolhaltiga råmaterial |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| FI980456A0 FI980456A0 (fi) | 1998-02-27 |
| FI980456A7 FI980456A7 (sv) | 1999-08-28 |
| FI104561B true FI104561B (sv) | 2000-02-29 |
Family
ID=8551060
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| FI980456A FI104561B (sv) | 1998-02-27 | 1998-02-27 | Förfarande för pyrolys av kolhaltiga råmaterial |
Country Status (13)
| Country | Link |
|---|---|
| US (1) | US6814940B1 (sv) |
| EP (1) | EP1060232B1 (sv) |
| CN (1) | CN1130446C (sv) |
| AT (1) | ATE255155T1 (sv) |
| AU (1) | AU2626799A (sv) |
| BR (1) | BR9908324A (sv) |
| CA (1) | CA2321824C (sv) |
| DE (1) | DE69913108T2 (sv) |
| EA (1) | EA001850B1 (sv) |
| ES (1) | ES2209399T3 (sv) |
| FI (1) | FI104561B (sv) |
| ID (1) | ID28197A (sv) |
| WO (1) | WO1999043768A1 (sv) |
Families Citing this family (71)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19950062A1 (de) * | 1999-10-16 | 2001-04-26 | Siempelkamp Guss Und Anlagente | Verfahren und Anlage zur Aufbereitung von flüssigen und/oder festen organischen Abfallstoffen |
| US8062503B2 (en) | 2001-09-18 | 2011-11-22 | Ivanhoe Energy Inc. | Products produced from rapid thermal processing of heavy hydrocarbon feedstocks |
| AU1671702A (en) * | 2000-11-17 | 2002-05-27 | Future Energy Resources Corp | Small scale high throughput biomass gasification system and method |
| EP1402591A1 (en) * | 2001-04-16 | 2004-03-31 | Future Energy Resources Corporation | Integrated biomass gasification and fuel cell system |
| FR2827591B1 (fr) * | 2001-07-17 | 2004-09-10 | Cie D Etudes Des Technologies | Procede et dispositif de production d'un gaz riche en hydrogene par pyrolyse thermique d'hydrocarbures |
| US7344622B2 (en) * | 2003-04-08 | 2008-03-18 | Grispin Charles W | Pyrolytic process and apparatus for producing enhanced amounts of aromatic compounds |
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-
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- 1998-02-27 FI FI980456A patent/FI104561B/sv not_active IP Right Cessation
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1999
- 1999-02-26 ID IDW20001624A patent/ID28197A/id unknown
- 1999-02-26 AT AT99906280T patent/ATE255155T1/de not_active IP Right Cessation
- 1999-02-26 WO PCT/FI1999/000153 patent/WO1999043768A1/en not_active Ceased
- 1999-02-26 US US09/623,018 patent/US6814940B1/en not_active Expired - Lifetime
- 1999-02-26 DE DE69913108T patent/DE69913108T2/de not_active Expired - Lifetime
- 1999-02-26 CA CA002321824A patent/CA2321824C/en not_active Expired - Lifetime
- 1999-02-26 EP EP99906280A patent/EP1060232B1/en not_active Expired - Lifetime
- 1999-02-26 BR BR9908324-8A patent/BR9908324A/pt not_active IP Right Cessation
- 1999-02-26 CN CN99805576A patent/CN1130446C/zh not_active Expired - Lifetime
- 1999-02-26 ES ES99906280T patent/ES2209399T3/es not_active Expired - Lifetime
- 1999-02-26 EA EA200000887A patent/EA001850B1/ru not_active IP Right Cessation
- 1999-02-26 AU AU26267/99A patent/AU2626799A/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| EA200000887A1 (ru) | 2001-02-26 |
| EP1060232A1 (en) | 2000-12-20 |
| CN1130446C (zh) | 2003-12-10 |
| CN1298440A (zh) | 2001-06-06 |
| ATE255155T1 (de) | 2003-12-15 |
| EA001850B1 (ru) | 2001-08-27 |
| CA2321824C (en) | 2008-06-10 |
| ES2209399T3 (es) | 2004-06-16 |
| DE69913108D1 (de) | 2004-01-08 |
| US6814940B1 (en) | 2004-11-09 |
| EP1060232B1 (en) | 2003-11-26 |
| CA2321824A1 (en) | 1999-09-02 |
| FI980456A7 (sv) | 1999-08-28 |
| WO1999043768A1 (en) | 1999-09-02 |
| DE69913108T2 (de) | 2004-08-26 |
| AU2626799A (en) | 1999-09-15 |
| BR9908324A (pt) | 2000-11-07 |
| ID28197A (id) | 2001-05-10 |
| FI980456A0 (fi) | 1998-02-27 |
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