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 waste

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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
Application number
PL404458A
Other languages
Polish (pl)
Other versions
PL227979B1 (en
Inventor
Halina Pawlak-Kruczek
Artur Brzędkiewicz
Władysław Madaj
Original Assignee
Pawlak-Kruczek Halina Pinwest Technika
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 Pawlak-Kruczek Halina Pinwest Technika filed Critical Pawlak-Kruczek Halina Pinwest Technika
Priority to PL404458A priority Critical patent/PL227979B1/en
Publication of PL404458A1 publication Critical patent/PL404458A1/en
Publication of PL227979B1 publication Critical patent/PL227979B1/en

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Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, 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).

PL404458A 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 PL227979B1 (en)

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)

Also Published As

Publication number Publication date
PL227979B1 (en) 2018-02-28

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