PL397087A1 - Method for drying of the wood biomass in the belt dryer - Google Patents

Method for drying of the wood biomass in the belt dryer

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Publication number
PL397087A1
PL397087A1 PL397087A PL39708711A PL397087A1 PL 397087 A1 PL397087 A1 PL 397087A1 PL 397087 A PL397087 A PL 397087A PL 39708711 A PL39708711 A PL 39708711A PL 397087 A1 PL397087 A1 PL 397087A1
Authority
PL
Poland
Prior art keywords
biomass
heated
wood biomass
drying chamber
air
Prior art date
Application number
PL397087A
Other languages
Polish (pl)
Other versions
PL217485B1 (en
Inventor
Dominika Bienkowska
Original Assignee
Stel-Investment Spólka Z Ograniczona Odpowiedzialnoscia, Spólka Komandytowo-Akcyjna
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 Stel-Investment Spólka Z Ograniczona Odpowiedzialnoscia, Spólka Komandytowo-Akcyjna filed Critical Stel-Investment Spólka Z Ograniczona Odpowiedzialnoscia, Spólka Komandytowo-Akcyjna
Priority to PL397087A priority Critical patent/PL217485B1/en
Publication of PL397087A1 publication Critical patent/PL397087A1/en
Publication of PL217485B1 publication Critical patent/PL217485B1/en

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  • Drying Of Solid Materials (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

Wynalazek dotyczy sposobu suszenia biomasy drzewnej w suszarni tasmowej, w którym zassane z otoczenia przez wentylatory powietrze ogrzewa sie w zainstalowanych nad komora suszenia wymiennikach ciepla zasilanych energia cieplna wytwarzana w biomasowej kotlowni, wilgotna biomase drzewna dostarcza sie w sposób ciagly do komory suszenia, w której w trakcie przesuwania warstwy biomasy drzewnej na perforowanym tasmowym przenosniku miesza sie ja i suszy ogrzanym powietrzem przechodzacym przez warstwe biomasy drzewnej od góry do dolu. Sposób charakteryzuje sie tym, ze powietrze z otoczenia zassane przez wentylatory (5) usytuowane na obudowie (4) komory suszenia (2) ponizej tasmowego przenosnika (3) ogrzewa sie wstepnie w zaleznosci od jego temperatury o 10°C do 20°C w pierwszej grupie wymienników ciepla (8) zasilanych energia cieplna odzyskiwana przez instalacje odzysku ciepla (9) z gazów spalinowych wytworzonych w procesie spalania w biomasowej kotlowni (7), a nastepnie ogrzane powietrze przepuszcza sie przez odpowiadajaca liczbowo pierwszej grupie wymienników ciepla (8) i polaczona z nia druga grupe wymienników ciepla (10) zasilanych energia cieplna wytwarzana bezposrednio w biomasowej kotlowni (7) doprowadzana do tych wymienników (10) w postaci podgrzanej mieszaniny wodno-glikolowej, w których przy temperaturze mieszaniny wodno-glikolowej na wejsciu wynoszacej od 65°C do 75°C, a na wyjsciu od 45°C do 55°C ogrzewa sie powietrze do temperatury od 55°C do 64°C, po czym powietrzem tym w komorze suszenia (2) suszy sie od góry do dolu przemieszczajaca sie na tasmowym przenosniku (3) warstwe biomasy drzewnej o wysokosci 10 cm, która po przemieszaniu wyrównuje sie ponownie do wysokosci 10 cm za pomoca dwóch przeciwbieznych srubowych przenosników (14) zamontowanych nad tasmowym przenosnikiem (3) za urzadzeniami mieszajacymi biomase.The invention relates to a method of drying wood biomass in a belt dryer, in which the air sucked in from the environment by fans is heated in heat exchangers installed above the drying chamber fed with heat energy generated in the biomass boiler room, moist wood biomass is continuously supplied to the drying chamber, in which while moving the wood biomass layer on the perforated belt conveyor, it is mixed and dried by heated air passing through the wood biomass layer from top to bottom. The method is characterized by the fact that the ambient air sucked in by the fans (5) located on the housing (4) of the drying chamber (2) below the belt conveyor (3) is preheated, depending on its temperature, by 10 ° C to 20 ° C in the first a group of heat exchangers (8) supplied with heat energy recovered by heat recovery installations (9) from flue gases produced in the combustion process in a biomass boiler room (7), and then the heated air is passed through the number 1 heat exchangers corresponding to the first group (8) and connected to there is a second group of heat exchangers (10) supplied with heat energy generated directly in the biomass boiler room (7) fed to these exchangers (10) in the form of a heated water-glycol mixture, in which at the water-glycol inlet temperature from 65 ° C to 75 ° C, and the output from 45 ° C to 55 ° C, the air is heated to a temperature from 55 ° C to 64 ° C, then the air in the drying chamber a (2) is dried from top to bottom moving on the conveyor belt (3) 10 cm high layer of wood biomass, which after mixing again equalizes to a height of 10 cm with the help of two opposing screw conveyors (14) mounted above the belt conveyor ( 3) behind biomase mixing devices.

PL397087A 2011-11-23 2011-11-23 Method for drying of the wood biomass in the belt dryer PL217485B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL397087A PL217485B1 (en) 2011-11-23 2011-11-23 Method for drying of the wood biomass in the belt dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PL397087A PL217485B1 (en) 2011-11-23 2011-11-23 Method for drying of the wood biomass in the belt dryer

Publications (2)

Publication Number Publication Date
PL397087A1 true PL397087A1 (en) 2013-05-27
PL217485B1 PL217485B1 (en) 2014-07-31

Family

ID=48522752

Family Applications (1)

Application Number Title Priority Date Filing Date
PL397087A PL217485B1 (en) 2011-11-23 2011-11-23 Method for drying of the wood biomass in the belt dryer

Country Status (1)

Country Link
PL (1) PL217485B1 (en)

Also Published As

Publication number Publication date
PL217485B1 (en) 2014-07-31

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