PL404458A1 - Method of autothermal valorisation of biomass or organic waste and a device for autoothermal valorization of biomass or organic waste - Google Patents
Method of autothermal valorisation of biomass or organic waste and a device for autoothermal valorization of biomass or organic wasteInfo
- Publication number
- PL404458A1 PL404458A1 PL404458A PL40445813A PL404458A1 PL 404458 A1 PL404458 A1 PL 404458A1 PL 404458 A PL404458 A PL 404458A PL 40445813 A PL40445813 A PL 40445813A PL 404458 A1 PL404458 A1 PL 404458A1
- Authority
- PL
- Poland
- Prior art keywords
- chamber
- reactor
- biomass
- organic waste
- valorization
- Prior art date
Links
- 239000002028 Biomass Substances 0.000 title abstract 5
- 239000010815 organic waste Substances 0.000 title abstract 5
- 238000000034 method Methods 0.000 title abstract 2
- 239000007789 gas Substances 0.000 abstract 4
- 239000000203 mixture Substances 0.000 abstract 3
- 238000002485 combustion reaction Methods 0.000 abstract 2
- 239000003546 flue gas Substances 0.000 abstract 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract 1
- 239000000567 combustion gas Substances 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 230000013011 mating Effects 0.000 abstract 1
- 239000002699 waste material Substances 0.000 abstract 1
Classifications
-
- 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
Landscapes
- Treating Waste Gases (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Sposób autotermicznej waloryzacji biomasy lub odpadów organicznych charakteryzuje się tym, że wstępnie przygotowaną biomasę lub odpady organiczne przemieszcza się na powierzchniach kolejno co najmniej dwóch, usytuowanych nad sobą, przenośników w komorze zamkniętego reaktora, podgrzewanych od dołu przepływającymi w przeciwprądzie, wymieszanymi z powietrzem spalinami o temperaturze od 180 °C do 320 °C w czasie od 30 do 60 minut, ze spalania gazów z autotermicznej waloryzacji mieszanki w reaktorze, w cyklonowej komorze spalania z kontrolowanym dopływem powietrza podawanego, gdzie spaliny grzewcze odprowadza się z komory reaktora do komina, natomiast toryfikat po wyjściu z reaktora schładza się do temperatury co najmniej 70 °C i odprowadza do zbiornika. Urządzenie do autotermicznej waloryzacji biomasy lub odpadów organicznych posiada reaktor (1) z komorą (2), posiadającą wewnątrz usytuowane nad sobą przenośniki zgrzebłowe, górny (14) i dolny (17) przenoszenia toryfikowanej mieszanki (44), których wnętrza (16, 17) i górne taśmy {15, 18) są podgrzewane spalinami ze spalania gazów z toryfikacji w komorze cyklonowej (21) z palnikiem (22) w jej dnie (23) i króćcami wylotowymi (24, 25), poprzez współpracujące kanały, górny (36) i dolny (37) i odpowiednio przez wloty (6, 7) w ścianie bocznej (5) komory (2), mającej ściany: górną (3) z wlotem (4), współpracującym z podajnikiem celkowym (34), połączonym przez przenośnik ślimakowy (33) z bunkrem załadowczym (32) odpadów, dolną (12) z wylotem (13) toryfikatu (45), odprowadzanego poprzez przenośnik ślimakowy (35) do zbiornika (43) i tylną (10) z wylotem (11) gazów z toryfikowanej mieszanki przez kanał (31) do komory cyklonowej (21) zasilanej powietrzem z wentylatorów, głównego (27) i pomocniczego (29) odpowiednio przez kanał (28), kanał (30) i wlot (26), gdzie wyloty spalin (8, 9) w ścianie bocznej (5) są połączone odpowiednio poprzez kanały (38, 40) i ich wyloty (39, 41) z kominem (52), a pompa (42) jest połączona z podajnikiem ślimakowym (33) toryfikatu, natomiast komora cyklonowa, komora (2) reaktora (1) oraz kanały spalin, komin (52) i przenośnik (35) toryfikatu są odpowiednio zaopatrzone w termopary T1 (46), T2 (47), T3 (48), T4 (49) i T5 (50), a także w automatyczny analizator spalin A (51) odprowadzanych do komina (52).The method of autothermal valorization of biomass or organic waste is characterized by the fact that the pre-prepared biomass or organic waste moves on the surfaces of at least two successively located above each other conveyors in the chamber of a closed reactor, heated from below, flowing counter-current, mixed with air at a temperature of from 180 ° C to 320 ° C for 30 to 60 minutes, from the combustion of gases from the autothermal mixture valorization in the reactor, in a cyclone combustion chamber with a controlled supply of air, where the heating flue gases are discharged from the reactor chamber to the chimney, while leaving the reactor cooled to a temperature of at least 70 ° C and discharged into a vessel. The device for autothermal valorization of biomass or organic waste has a reactor (1) with a chamber (2), inside there are upper (14) and lower (17) scraper conveyors for carrying the torrefied mixture (44), the interior of which (16, 17) and the upper belts (15, 18) are heated by the combustion gases from torrefaction in the cyclone chamber (21) with the burner (22) in its bottom (23) and the exhaust ports (24, 25), through the mating channels, upper (36) and lower (37) and, respectively, through inlets (6, 7) in the side wall (5) of the chamber (2), having walls: upper (3) with an inlet (4), cooperating with a cell feeder (34) connected by a screw conveyor (33) with a waste loading bunker (32), the lower (12) with the torrefied (45) outlet (13), discharged through the screw conveyor (35) to the container (43) and the rear (10) with the torrefied gas outlet (11) the mixture through the duct (31) to the cyclone chamber (21) supplied with air from the fans, the main (27) and the auxiliary (29) via a channel (28), a channel (30) and an inlet (26), respectively, where the exhaust gas outlets (8, 9) in the side wall (5) are connected respectively through the channels (38, 40) and their outlets (39, 41) with the chimney (52), and the pump (42) is connected to the screw feeder (33) of the torrefaction, while the cyclone chamber, the reactor (1) chamber (2) and the flue gas ducts, the chimney (52) and the torrefaction conveyor (35) are adequately equipped with thermocouples T1 (46), T2 (47), T3 (48), T4 (49) and T5 (50), as well as with an automatic exhaust gas analyzer A (51) discharged to the chimney (52).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL404458A PL227979B1 (en) | 2013-06-26 | 2013-06-26 | A method of autothermal valorization of biomass or organic waste and a device for autothermal valorization of biomass or organic waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL404458A PL227979B1 (en) | 2013-06-26 | 2013-06-26 | A method of autothermal valorization of biomass or organic waste and a device for autothermal valorization of biomass or organic waste |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| PL404458A1 true PL404458A1 (en) | 2015-01-05 |
| PL227979B1 PL227979B1 (en) | 2018-02-28 |
Family
ID=52126332
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PL404458A PL227979B1 (en) | 2013-06-26 | 2013-06-26 | A method of autothermal valorization of biomass or organic waste and a device for autothermal valorization of biomass or organic waste |
Country Status (1)
| Country | Link |
|---|---|
| PL (1) | PL227979B1 (en) |
-
2013
- 2013-06-26 PL PL404458A patent/PL227979B1/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| PL227979B1 (en) | 2018-02-28 |
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