Classifications

• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F26—DRYING
  • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
  • F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
  • F26B21/02—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
  • F26B21/04—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure partly outside the drying enclosure
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F26—DRYING
  • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
  • F26B3/00—Drying solid materials or objects by processes involving the application of heat
  • F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
  • F26B3/10—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour carrying the materials or objects to be dried with it

Definitions

• the present invention relates to a method for drying a particulate material, such as wood fibres for making fibreboards, in which method the material is transported through a two-stage drying plant by means of drying gas, e.g. drying air, the material being supplied, in a first stage, into a first drying conduit where it is dried in a first drying gas flow transporting the material to a first cyclone in which it is separated from the drying gas which is discharged from the first cyclone, and the material separated in the first cyclone being supplied, in a second stage, into a second drying conduit where it is dried in a second drying gas flow transporting the material to a second cyclone in which it is separated from the drying gas which is discharged from the second cyclone.
• drying gas e.g. drying air
• fresh air is blown in as drying air in the first stage, whereupon this air is separated in the first cyclone and emitted from the first stage.
• the used drying gas is emitted into the atmosphere but is previously used to preheat the fresh air which is blown in in the first stage.
• the used drying air is passed through a heat exchanger.
• the heat exchanger is combined with a scrubber for washing the used drying air.
• fresh air is blown in as drying air also in the second stage, whereupon this air is separated in the second cyclone and emitted into the atmosphere.
• the object of the present invention is to provide a method for drying a particulate material, such as wood fibres, in which method the emission of pollutants into the atmosphere is reduced, simultaneously as the drying gas is utilised in an effective manner.
• this object is achieved by a method which is of the type mentioned by way of introduction and characterised in that the major part of the drying gas discharged from the first cyclone is conveyed to a condenser so as to be subsequently recir ⁇ culated in the first stage, that the remainder of the dry ⁇ ing gas discharged from the first cyclone is emitted from the plant, that an amount of the drying gas discharged from the second cyclone, which corresponds to said remain ⁇ der of the drying gas discharged from the first cyclone, is conveyed to the condenser to be circulated in the first stage, that the remainder of the drying gas discharged from the second cyclone is recirculated in the second stage, and that an amount of fresh drying gas, e.g. fresh air, which corresponds to said remainder of the drying gas discharged from the first cyclone, is supplied to the second stage.
• About 80% of the drying air discharged from the first cyclone is preferably conveyed to the condenser.
• the second drying gas flow preferably is about 30% of the first drying gas flow.
• the first drying gas flow preferably has a tempera- ture of 150°C-180°C, while the second drying gas flow pre ⁇ ferably has a temperature of 110°C-135°C.
• the plant shown in the drawing and intended for dry ⁇ ing wood fibres for making fibreboards has two drying stages, viz. a first stage 1 and a second stage 2.
• first fan 3 which blows drying air, which is heated to a temperature of about 160°C in a first heating device 4, through a first drying conduit 5 opening into a first cyclone 6.
• Glue-coated wood fibres which are to be dried are sup ⁇ plied through a first supply conduit 7 into the first dr ing conduit 5 and are transported by the drying air to th first cyclone 6.
• the wood fibres are dried while being transported. They are separated from the drying air in th first cyclone 6 and discharged therefrom by means of a first sluice arrangement 8.
• the drying air is discharged from the first cyclone through a conduit 9.
• the major part, preferably about 80% of the drying air discharged from the first cyclone is passed through a conduit 10 to a condenser 11 in which vapour in the drying air is condensed to be discharged in the form of water containing fibre dust, formaldehyde and hydrocarbons from the condenser 11 to, for example, a water-purifying apparatus (not shown) through a duct 12.
• the drying air is passed from the condenser 11 through a conduit 13 to the first fan 3 to be recirculated in the first stage 1.
• the remainder of the drying air discharged from the first cyclone 6 is emitted from the plant throug a conduit 14 and can be used as e.g. combustion air in a boiler plant.
• a second fan 1 which blows drying air heated in a second heating device 16 through a second drying conduit 17 opening into a second cyclone 18.
• the wood fibres discharged from the sluice arrangement 8 of the first cyclone 6 are supplied through a second supply conduit 19 into the second drying conduit 17 and are transported by the drying air therein to the second cyclone 18. While being transported, the wood fibres are additionally dried.
• the dried wood fibres are separated from the drying air in the second cyclone 1 and are discharged therefrom by means of a second sluice arrangement 20.
• the dried fibres are passed through a con duit 21 on to a storage container (not shown).
• the drying air is discharged from the second cyclone 18 through a conduit 22.
• the remainder of the drying air discharge from the second cyclone 18 is recirculated through a con ⁇ duit 24 connected to the drying conduit 17, so as to be recirculated in the second stage 2.
• An amount of fresh air, which corresponds to the drying air discharged from the first stage 1 through the conduit 14 is supplied to the second stage 2 through a conduit 25 connected to the second heating device 16 in order to replace the drying air transferred from the second stage 2 to the first sta 1 through the conduit 23.
• the flow of drying air in the second stage 2 (by which is meant the flow of drying air in the second dryi conduit 17) preferably constitutes about 30% (0.3 G) of the drying air flow G in the first stage (by which is meant the flow of drying air in the first drying conduit 5).
• the flow of drying a discharged from the plant through the conduit 14 thus co stitutes about 20% of the drying air flow in the conduit 5, i.e. about 0.2 G.
• the drying air flow in the conduit thus also constitutes about 0.2 G, which means that the drying air flow recirculated through the conduit 24 in stage 2 is about 0.1 G, and that the flow of fresh air i the conduit 25 is about 0.2 G.
• the fresh air is heated in the second heating devic 16 to a temperature of about 150°C.
• the fresh air is mix with the drying air recirculated through the conduit 24 and having a temperature of about 60°C, whereby a flow o drying air having a temperature of about 120°C is obtain in the drying conduit 17.

Landscapes

• Engineering & Computer Science (AREA)
• Mechanical Engineering (AREA)
• General Engineering & Computer Science (AREA)
• Life Sciences & Earth Sciences (AREA)
• Microbiology (AREA)
• Drying Of Solid Materials (AREA)
• Dry Formation Of Fiberboard And The Like (AREA)
• Treatment Of Sludge (AREA)
• Processing Of Solid Wastes (AREA)
• Inorganic Compounds Of Heavy Metals (AREA)
• Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Priority Applications (6)

Applications Claiming Priority (2)

Publications (1)

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ID=20380951

Family Applications (1)

Country Status (9)

Cited By (1)

Families Citing this family (9)

Citations (4)

• 1990
  • 1990-11-20 SE SE9003687A patent/SE469353B/sv not_active IP Right Cessation
• 1991
  • 1991-11-14 AT AT91920414T patent/ATE126879T1/de not_active IP Right Cessation
  • 1991-11-14 ES ES91920414T patent/ES2079079T3/es not_active Expired - Lifetime
  • 1991-11-14 US US08/050,339 patent/US5295310A/en not_active Expired - Lifetime
  • 1991-11-14 EP EP91920414A patent/EP0557386B1/en not_active Expired - Lifetime
  • 1991-11-14 AU AU89376/91A patent/AU653975B2/en not_active Ceased
  • 1991-11-14 DE DE0557386T patent/DE557386T1/de active Pending
  • 1991-11-14 WO PCT/SE1991/000774 patent/WO1992008938A1/en active IP Right Grant
  • 1991-11-14 CA CA002096334A patent/CA2096334C/en not_active Expired - Fee Related
  • 1991-11-14 DE DE69112419T patent/DE69112419T2/de not_active Expired - Lifetime

Patent Citations (4)

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