EP0267516A2 - Méthode et appareil pour la fabrication des panneaux de fibres de bois - Google Patents

Méthode et appareil pour la fabrication des panneaux de fibres de bois Download PDF

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Publication number
EP0267516A2
EP0267516A2 EP87116121A EP87116121A EP0267516A2 EP 0267516 A2 EP0267516 A2 EP 0267516A2 EP 87116121 A EP87116121 A EP 87116121A EP 87116121 A EP87116121 A EP 87116121A EP 0267516 A2 EP0267516 A2 EP 0267516A2
Authority
EP
European Patent Office
Prior art keywords
press
belt
hardener
band
fleece
Prior art date
Legal status (The legal status 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 status listed.)
Granted
Application number
EP87116121A
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German (de)
English (en)
Other versions
EP0267516A3 (en
EP0267516B1 (fr
Inventor
Kurt Held
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Individual
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Individual
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Filing date
Publication date
Priority claimed from DE19863639061 external-priority patent/DE3639061C2/de
Application filed by Individual filed Critical Individual
Publication of EP0267516A2 publication Critical patent/EP0267516A2/fr
Publication of EP0267516A3 publication Critical patent/EP0267516A3/de
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Publication of EP0267516B1 publication Critical patent/EP0267516B1/fr
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
    • B27N—MANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
    • B27N3/00—Manufacture of substantially flat articles, e.g. boards, from particles or fibres
    • B27N3/08—Moulding or pressing
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
    • B27N—MANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
    • B27N3/00—Manufacture of substantially flat articles, e.g. boards, from particles or fibres
    • B27N3/08—Moulding or pressing
    • B27N3/086—Presses with means for extracting or introducing gases or liquids in the mat
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
    • B27N—MANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
    • B27N3/00—Manufacture of substantially flat articles, e.g. boards, from particles or fibres
    • B27N3/08—Moulding or pressing
    • B27N3/24—Moulding or pressing characterised by using continuously acting presses having endless belts or chains moved within the compression zone
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B30—PRESSES
    • B30B—PRESSES IN GENERAL
    • B30B5/00—Presses characterised by the use of pressing means other than those mentioned in the preceding groups
    • B30B5/04—Presses characterised by the use of pressing means other than those mentioned in the preceding groups wherein the pressing means is in the form of an endless band
    • B30B5/06—Presses characterised by the use of pressing means other than those mentioned in the preceding groups wherein the pressing means is in the form of an endless band co-operating with another endless band
    • B30B5/065—Presses characterised by the use of pressing means other than those mentioned in the preceding groups wherein the pressing means is in the form of an endless band co-operating with another endless band using anti-friction means for the pressing band
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T156/00—Adhesive bonding and miscellaneous chemical manufacture
    • Y10T156/17—Surface bonding means and/or assemblymeans with work feeding or handling means
    • Y10T156/1702—For plural parts or plural areas of single part
    • Y10T156/1712—Indefinite or running length work
    • Y10T156/1741—Progressive continuous bonding press [e.g., roll couples]

Definitions

  • the invention relates to a method for producing wood-based panels according to the preamble of patent claim 1 and devices for carrying out this method according to the preamble of patent claims 26, 30 and 87.
  • Such wood-based panels such as chipboard, fiber, OSB or MDF, consist of wood chips, wood fibers, etc., which are glued with a binder.
  • the binders are usually urea, melamine or phenol-formaldehyde resins. These chips are then scattered into a fleece, which is compressed into a compact plate in a press. To accelerate the setting process, heat can be added during pressing and a hardener can be added to the binder solution before the chips are glued.
  • Continuous processes are increasingly being used to produce such wood-based panels in which a continuous double belt press is used instead of the discontinuous deck press.
  • the fleece is exposed to surface pressure and possibly heat during conveyance by the double belt press, so that the wood-based panel is produced as an endless web.
  • DE-OS 34 11 590 also shows a system working with a double belt press for the production of wood-based panels by means of steam curing.
  • distribution and collection channels are arranged on both sides of the press belts in the inlet area of the double belt press, from which nozzle holes extend to the press nip.
  • the overheated water vapor is introduced from the distribution channels through the nozzle holes into the long sides of the fleece.
  • DE-OS 34 14 178 shows a process which works with a discontinuous deck press and in which superheated steam is also fed to the fleece via the pressure plates.
  • the system according to DE-OS 20 58 820 allows a more uniform vaporization over the width of the system and thus also a uniform curing across the width of the material plate, but the structure of the steam supply via the pressure plates and the press belts in the fleece is very expensive .
  • the rollers run in this embodiment in a steam atmosphere in which there is a very high risk of corrosion for the rollers.
  • the lubricant required for the rollers tends in a steam atmosphere usually to decomposition and thus leads to a scuffing of the rollers after a short operating time. Such presses have not proven to be reliable in the past and are therefore rarely used.
  • the invention has for its object to provide a method for the production of wood-based panels, which both greatly reduces the pressing time and reduces the heat input. In a continuous process using a double belt press, the use of shorter double belt presses should be possible.
  • the advantages that can be achieved with the invention are, in particular, that no steam generation or a greatly reduced generation has to take place, so that the related energy costs are at least greatly reduced. Since the pressing time is shortened considerably compared to conventional continuous or discontinuous systems, the production performance of the system increases.
  • the gas or steam atmosphere can be separated from the rollers, so that there is neither the risk of corrosive destruction of the rollers or other components of the double belt press nor the risk of the lubricant decomposing with a simultaneous impairment of its lubricity.
  • the hardening of the wood-based panels can advantageously be controlled in a metered manner with the aid of the concentration of the acidic or basic gas.
  • the method according to the invention can be carried out both with continuously operating plants for producing endless webs of wood-based panels and with discontinuous plants for producing wood-based panels with fixed dimensions.
  • Continuous processes generally work with a double belt press, while discontinuous processes use single or multi-day presses.
  • FIG. 1 Such a plant operating according to the method according to the invention for the continuous production of chipboard is shown in Figure 1.
  • the wood chips are processed in devices arranged in front of the double belt press, pretreated and glued with hardener-free binder. Such devices are known per se and are therefore not shown in the drawing.
  • These glued wood chips are fed to a forming station 3 via a pipeline 2.
  • the forming station 3 is arranged above the end of a conveyor belt 6 on the right in the drawing, which is looped over two deflecting rollers 4 and 5 and moves continuously in the direction of the arrow towards the double belt press 1.
  • the glued wood chips are scattered onto the conveyor belt to form a fleece consisting of a chip cake 7.
  • the scattering can take place in such a way that a multi-layer chip cake is formed, for example a three-layer chip cake, in which the top layer consists of fine chips and the middle layer consists of coarse chips.
  • the chip cake 7 is transported with the conveyor belt 6 in the direction of the arrow to the double belt press 1.
  • further devices known per se and therefore not shown in the drawing can be arranged.
  • Such devices can be, for example, checkweighers with which the basis weight of the chip cake is measured, pre-pressing devices, etc.
  • a transfer plate 8 is arranged, which guides the chip cake 7 from the conveyor belt 6 into the entry zone of the double belt press 1.
  • the chip cake 7 When entering the double belt press 1, the chip cake 7 is continuously compressed to the final thickness of the chipboard under the action of pressure.
  • a hardener for the binder with which the wood chips are glued is in gaseous form or in a binary phase with a gaseous carrier supplied to the surfaces of the chip cake 7 within the double belt press 1. This gas penetrates into the chip cake 7 via the surfaces, since this cake still has a low density during the compression phase.
  • strong inorganic or organic acids act as particularly fast hardeners, which greatly accelerate the hardening reaction of the resin.
  • Such acids are, for example, hydrochloric acid, sulfuric acid, phosphoric acid, formic acid, acetic acid, maleic acid and the like.
  • inorganic bases act as fast hardeners.
  • a basic hardener is, for example, ammonia.
  • a cooling zone associated with the outlet can be present in the double belt press 1, so that the chipboard web is already cooled in the double belt press 1 under the effect of the surface pressure.
  • the chipboard web 9 then leaves the double belt press 1 at a uniform speed and is further processed in the system parts following the double belt press 1. If necessary, the chipboard web 9 can then pass through a further cooling device, not shown in the drawing, for further cooling.
  • the particle board web 9 is then ground to the finished size in a grinding station 10. Then the particle board web 9 is divided in a cross-cutting station 11 into individual particle boards 12 of the desired size, which are stacked in a stacking device 13 for removal on pallets.
  • the entire process sequence in the plant shown in FIG. 1, The spreading of the chip cake 7 in the forming station 3, the specification and keeping constant of the process parameters of the double belt press 1 and the division of the chipboard web 9 into individual plates is controlled by a computer which is arranged in the control cabinet 14.
  • the data terminal 15 serves to enter the parameters by the user.
  • the computer in the control cabinet 14 can also be connected to an external host computer, which is located, for example, in the central EDP, in order to control the production and report back the production data enable further evaluation directly from the head office.
  • the double belt press 1 for the continuous production of chipboard is shown schematically.
  • the double belt press 1 has four guide drums 18, 19, 20, 21 rotatably mounted in bearing bridges 16, 17.
  • Two press belts 22 and 23, each consisting of two press belts, are guided around two of these guide drums 18, 19, which closer is shown in Fig. 3.
  • the direction of rotation of the press belt arrangement 22, 23 is indicated by arrows in the deflection drums 18 and 21.
  • the chip cake 7 is passed between the press belt arrangements 22 and 23 through the double belt press 1.
  • the chip cake 7 is first compressed in a wedge-shaped inlet zone 24, then through a medium-pressure reaction zone 25 with a constant gap width and then through a low-pressure mold holding zone 26, so that finally the chipboard web 9 on the deflection drums 19 and 20 leaves the double belt press 1.
  • the pressure exerted in the individual zones 24, 25 and 26 via pressure plates 27, 28 and 29 can be selected depending on the requirements of the chip cake and the type of resin for glueing the chips.
  • the reaction forces exerted by the chip cake 7 are transmitted via the pressure plates 27, 28, 29 and from support beams 30 connected to them into the press frame, which is only indicated schematically.
  • the design of the press frame is known from DE-OS 32 34 082 and does not need here to be explained in more detail.
  • the structure of the pressure plates 27, 28 can be seen in more detail in FIG. 3.
  • the pressure plate 27 of the deflection drum 18 or 21 is too wedge-shaped and thus adapts to the shape of the wedge-shaped inlet zone 24.
  • the pressure plate 28 for the medium pressure reaction zone 25 has a substantially rectangular cross section.
  • a roller bed is arranged between the pressure plates 27, 28 and the inner belt 31 of the press belt arrangement 22 or 23 consisting of the inner belt 31 and outer belt 32, which transfers the pressure from the pressure plates 27, 28 to the press belt arrangement 22 or 23.
  • the fixedly arranged in the double belt press 1 roller bed consists of staggered rollers 33, which are mounted on shafts 35 by means of bearing needles 34.
  • the shafts 35 are fastened in bearing strips 36, which in turn are fastened on the side facing away from the inner belt 31 in the pressure plate 27 or 28 .
  • the further training of such a roller bed can also be done according to DE-OS 31 23 291 or DE-OS 33 04 754.
  • Transverse holes 37 are made in the pressure plates 27, 28, through which thermal oil can be passed if heating of the pressure plates 27, 28 is desired.
  • a roller bed can also be attached between the pressure plate 29 and the inner band 31.
  • a pressure chamber 38 can also be provided here (see FIG. 4). To the sides, this pressure chamber 38 is delimited by a sliding surface seal 39, which runs around the edge of the pressure chamber 38 without interruption.
  • the sliding surface seal 39 is seated in a groove 40 in the pressure plate 29 and is acted upon from the groove base of the groove 40 with a pressure medium, which acts on an O-ring cord 41 lying against the sliding surface seal 39, so that the sliding surface seal slides firmly onto a surface the inner band 31 rests.
  • a pressurizable fluid pressure medium is introduced, which exerts the pressure on the press belt assembly 22 or 23. Since there is generally no further compression of the chip cake 7 in the medium-pressure reaction zone 25, such a pressure chamber 38 can also be fitted there, if desired, instead of the roller bed between the pressure plate 28 and the inner belt 31.
  • the inner band 31 and the outer band 32 of the press band arrangement 22 and 23 are spaced apart from one another. This distance is kept constant by spacers 42 which are fastened on the outer band 32 and extend across the width of the outer band 32. This creates a cavity between two spacers 42, which is formed by the spacers 42 and the outside of the inner band 31 and the inside of the outer band 32. This cavity extends over the width of the press belt arrangement 22 or 23 and thus forms a transverse channel 43.
  • the spacer 42 can be seen in more detail in FIG. It consists of two strips 44 of L-shaped cross section, which are arranged such that the longer legs of the L are opposite one another and are at a distance from one another.
  • the shorter legs of the L's are connected to the inside of the outer band 32 by a weld seam 48.
  • a slide bar 45 is clamped into the groove formed by the distance between the two longer legs of the L-shaped bars 44. This slide bar 45 touches with its narrow surface in each case the inner band 31 and the outer band 32.
  • the height of the slide bar 45 is chosen just as large as the desired distance between the inner and outer band.
  • the slide bar 45 slides with its narrow surface on the outside of the inner band 31.
  • the slide bar is made of a plastic with good sliding properties.
  • polyimides are suitable.
  • the slide bar there consists of a metal body 46, on the narrow surface of which the inner band 31 is assigned a slide surface 47 is applied.
  • This sliding surface 47 consists of a dry sliding layer, for example of porous sintered tin bronze, the pores of which are filled with polytetrafluoroethylene or graphite. Due to the good metallic thermal conductivity of such dry sliding layers, such an embodiment is particularly suitable when heat transfer from the pressure plate to the inner band, from the inner band to the outer band and from the outer band to the chip cake is desired.
  • additional lubrication of these surfaces can be provided.
  • the L-shaped strips 44 can also be welded to the outside of the inner band 31 so that the slide bar 45 or 47 slides on the inside of the outer band 32.
  • the spacers consist of a single molded part 49, which is connected to the inner band 31.
  • This molded part 49 consists of a metal-rubber compound and is particularly suitable if no heat has to be supplied from the pressure plates 27, 28 via the press belt arrangement 22, 23 to the chip cake 7 for pressing the chip cake.
  • the molded part 49 is fastened on the outside of the inner band 31 and has adjacent webs 50, the height of which is precisely the distance between In nenband 31 and outer band 32 corresponds. Between two webs 50, which run across the width of the press belt arrangement 22, 23, there is a transverse channel 51, which is too open to the inside of the outer belt 32.
  • the webs 50 are connected to one another along the groove base of the channel 51 facing the inner band 31.
  • a support band 78 is arranged between the inner band 31 and the outer band 32 of the press band arrangements 22, 23, which is deformed in a wave-like or approximately sinusoidal manner, so that adjacent elevations 79 and depressions 80, each with the same height, alternate.
  • the support band 78 is loosely guided between the inner band 31 and outer band 32.
  • it can also be attached to the outer band 32 either by means of spot welds 81 on the depressions 80, as shown in FIG. 10, or by means of spot welds on the elevations 79 (not shown in FIG. 10) on the inner band 31.
  • transverse channels 82 and 83 are connected to one another with bores 84.
  • an acidic or basic hardener for the binder with which the chips of the chip cake 7 are glued is in a gaseous phase or in a binary phase with a gaseous one Carrier supplied.
  • a feed part 52 for the hardener is arranged on the left and right on the side of the double belt press 1 along the wedge-shaped inlet zone 24.
  • This feed part 52 can be seen in section in FIG. 7.
  • the feed part 52 can consist of two separate parts 52a and 52b for the upper one and the lower press belt arrangement 22, 23 consist, as shown on the left in FIG. 7, or of a single part 52, as can be seen on the right in FIG. 7.
  • the one-piece feed part 52 has the advantage that the inlet zone 24 is laterally sealed.
  • the feed part 52, 52a, 52b comprises the lateral edge region of the two press belt arrangements 22 and 23, which laterally protrude slightly beyond the rollers 33 of the roller bed.
  • a recess 53 both in the area of the press belt arrangement 22 and of the press belt arrangement 23, the height of which is somewhat larger than the distance of the inner belt 31 from the outer belt 32 and the depth of which is somewhat larger than the protruding part of the press belt arrangement 22, 23.
  • a sealing element 54 is attached, which touches the edges of the inner band 31 and the outer band 32 under light pressure, and covers the edge of the transverse channel 43, 51.
  • the sealing element consists of a metal-rubber element, for example Viton.
  • the dry sliding surfaces 55, 56 are two dry sliding surfaces 55, 56 on the horizontal walls of the recess 53, the dry sliding surface 55 sliding on the projecting edge of the inside of the inner band 31 and the dry sliding surface 56 on the projecting edge of the outside of the outer band 32.
  • the dry sliding surfaces can consist of a copper-metal matrix, in the pores of which graphite is embedded, or of tin-bronze. Due to the dry sliding surfaces 55, 56 and the sealing element 54, the transverse channels 43, 51 arranged between the moving press belt arrangements 22, 23 are dynamically sealed in the wedge-shaped inlet zone 24 against the feed part 52.
  • a collecting line 57 runs in the longitudinal direction, ie in the forward direction of the chip cake 7, from which bores 58 lying one behind the other in the longitudinal direction and in the transverse direction extend in the direction of the press belt arrangement 22, 23.
  • the transverse direction is the one lying in the press belt plane, perpendicular to the forward direction of the chip cake 7 standing direction.
  • These bores 58 pass through the sealing element 54.
  • the acidic or basic hardener in gaseous form or with a gaseous carrier is introduced into the feed part 52 via the collecting line 57. From the manifold 57, the hardener then passes through the bores 58 into the channels 43, 51 as soon as a bore 58 opens into the channel 43, 51 at the moving press belt arrangement.
  • the channels 43, 51 are thus dynamically filled with the gas containing the hardener as long as they are in the wedge-shaped inlet zone 24.
  • Distributed openings 59 are provided in the outer band 32 in the longitudinal and transverse directions, through which the gaseous hardener or the carrier gas transporting the hardener can pass to the surface of the chip cake 7 and penetrate into it. Since the chip cake 7 is not yet completely compressed in the wedge-shaped inlet zone 24, the gas can penetrate to the center of the chip cake 7 and start the reaction of the binder with which the chips are glued and accelerate its hardening.
  • thermosetting resins used for the binder generally allow the curing to be further accelerated by the application of heat.
  • the gas itself can advantageously be used as a carrier for this heat. If the hardener is supplied in the gaseous phase, the hardener gas can be heated before it is introduced into the channels 43, 51. If the hardener is supplied in the binary phase with a gaseous carrier, this gaseous carrier can be heated accordingly.
  • a gaseous carrier medium can be a gas which is neutral with respect to the acidic or basic hardener, ie gas which does not react with it, such as air or an inert gas. Water vapor, which can be overheated, is also suitable as a gaseous carrier.
  • the press belts 31, 32 can be heated so that the chip cake 7 is in contact via heat conduction Outer band 32 heat is transferred to the chip cake 7.
  • a further embodiment for feeding the hardener into the channel 43, 51 is shown in the part of the feed part 52a assigned to the press belt arrangement 22. Bores 60 pass vertically downward through the dry sliding surface 62 from the collecting line 63 for the hardener. In this area of the inner band 31 of the press band arrangement 22 there are inlet openings 61 in the form of slots, so that the hardener can enter the channels 43, 51 dynamically.
  • the openings 59 in the outer belt 32, through which the gaseous hardener or the carrier gas transporting the hardener penetrates from the channels 43, 51 into the chip cake 7, are spaced in the transverse and longitudinal directions at an appropriate distance, which is calculated according to the amount of hardener required per unit of time , arranged.
  • the openings 59 can be designed as bores. Slits running in the longitudinal direction, the width of which in the transverse direction is approximately 0.1 to 0.2 mm, have proven to be particularly advantageous. These slots have a trapezoidal cross section, the taper of which is assigned to the outside of the outer band 32, as shown in FIG. 6 with the reference number 64.
  • the trapezoidal cross-section of the opening 64 acts as a nozzle for the hardener which is directed onto the chip cake 7.
  • Such slots can be made in the outer band 32 with the aid of a laser.
  • These openings 59, 64 slight burrs which consist of erected chips remain on the chipboard after the pressing. These burrs are removed in the grinding station 10 after the chipboard web 9 has left the double belt press 1 with the aid of a grinding belt (see FIG. 1).
  • the openings 59, 64 can become clogged with resin residues from the chip cake 7 over time. To prevent this, the openings 59, 64 in the outer belt 32 of the press belt arrangement 22, 23 after Leave the low-pressure mold holding zone 26 as soon as the particle board web 9 has separated from the press belt arrangement at the outlet.
  • a roller 65 equipped with teeth can serve this purpose (indicated schematically in FIG. 4).
  • the teeth 66 of the roller 65 are arranged at the same distance as the openings 59, 64 on the outer belt 32. The teeth 66 therefore engage in these openings 59, 64 and expel resin residues which are located in these openings 59, 64.
  • the roller 66 Due to the engagement of the teeth 66 in the openings 59, 64, the roller 66 is carried along by the movement of the press belt arrangement 22, 23, so that the roller 65 does not require its own drive.
  • the resin residues which are pushed into the channels 43, 51 by the teeth 66 can be removed therefrom by means of a suction part which is constructed exactly like the feed part 52a, b in FIG. 7.
  • the suction part is attached to the outlet of the double belt press behind the roller 65.
  • the manifold 57, 63 is connected to negative pressure, so that the resin residues are sucked out of the channels 43, 51 via the bores 58, 60 and the manifold 57, 63.
  • the design of the double belt press can be somewhat simplified.
  • the inlet area of such a simplified double belt press can be seen in a longitudinal section in FIG. 11.
  • the upper and lower press belt arrangements each consist of a simple press belt 85, which is provided with openings 86.
  • the pressure plates 27 in the wedge-shaped inlet zone 24 are provided with channels 87 through which the acidic or basic hardener in the gaseous phase or a binary phase with a gaseous carrier medium is fed from the outside into the double belt press.
  • Leads 88 lead from the channels 87, which guide the hardener from the channels 87 to the roller bed, from where the hardener is conducted via the rollers and the openings 86 onto the surfaces of the chip cake. The hardener then penetrates from the surfaces into the chip cake and accelerates the hardening reaction of the binder in the chip cake.
  • a feed part 52 for the hardener, as described above, is not necessary here. Furthermore, in this embodiment, the costs for a second press belt and the spacers are advantageously saved.
  • a double belt press for the continuous production of particle board webs can be seen in a further embodiment in FIG. 8.
  • This double belt press 67 is constructed similarly to that in FIG. 2, but the lower press belt arrangement 68 in the wedge-shaped inlet zone 24 is somewhat preferred over the upper press belt arrangement 69, so that the part of the lower press belt arrangement 68 on the right in the drawing outside the casing 70 of the entire double belt press protrudes.
  • the scattering station 3 Above this protruding part of the lower press belt arrangement 68 is the scattering station 3, in which the hardener-free glued chips are scattered to form a chip cake 7 on the lower press belt arrangement 68.
  • the chip cake 7 is then transported with the continuously advancing lower press belt arrangement into the wedge-shaped inlet zone 24, where the acidic or basic hardener is supplied in gaseous form or in a binary phase with a gaseous carrier during the compression phase according to the inventive method.
  • the wedge-shaped entry zones 24 into the double belt press shown in FIGS. 2 and 8 are symmetrical at the top and bottom, i.e. they each run at the same angle.
  • the top and bottom angles of the run-in wedge can also be different. It is also possible to design only the upper or lower side of the inlet zone in a wedge shape with an angle.
  • the double belt press 89 has six deflecting drums 90, 91, 92, 93, 94, 95, three deflecting drums each being assigned to a press belt arrangement, namely the deflecting drums 90, 91, 92 of the press belt arrangement 96, which is on the left in the drawing Double belt half 103 and the deflection drums 93, 94, 95 of the press belt arrangement 97 of the right double belt half 104.
  • the deflection drums 90, 91, 92 and 93, 94, 95 are arranged essentially at the corner points of a triangle and rotate according to the arrows in the drawing.
  • the press belt arrangements 96 and 97 which run over the deflection drums 90, 91, 92 and 93, 94, 95 and which are tensioned by means of hydraulic cylinders 98 thus have a horizontal section 99 and a vertical section 100 which is the wedge-shaped inlet zone 24, the medium pressure reaction zone 25 and is assigned to the low-pressure mold holding zone 26.
  • One half 102a and 102b of the chip cake is scattered onto the horizontal section 99 of the left double band half 103 and the right double band half 104 by scattering stations 101.
  • Half 102a is transported to the right with the leading press belt arrangement 96 in the horizontal direction and half 102b is moved to the left with the press belt arrangement 97 and is deflected downward in the vertical direction on the deflection drums 92 and 95.
  • the two chip cake halves 102a and 102b meet to form a single chip cake 102, which is then transported in a vertical direction through the wedge-shaped inlet zone 24 with the two press belt arrangements 96, 97.
  • the press belt arrangements 96, 97 each consist of two press belts arranged at a distance from one another by means of spacers 42, namely an inner belt 31 and an outer belt 32 (see FIG. 5).
  • the acidic or basic, gaseous hardener in channels 51 in the wedge shaped inlet zone 24 is introduced, from where it flows through openings 59 in the outer belt 32 onto the surfaces of the chip cake 102 and then penetrates into the chip cake 102.
  • the pressing pressure is transferred from the pressure plate 27 to the inner belt 31 of the pressing belt arrangement 96, 97 via a roller bed 105.
  • the medium-pressure reaction zone 25 and then the low-pressure mold holding zone 26 follow.
  • the pressing pressure from the pressure plates 28, 29 can also be applied to the press belt arrangement via a roller bed 106, 107 96, 97 are transmitted, as shown in FIG. 12 for the left double band half 103.
  • the pressure can also be transferred to the pressure belt arrangement 96, 97 via pressure chambers 108, 109, as can be seen on the right double belt half 104.
  • the press frame, on which the two vertically positioned double belt halves are fastened, is not shown in FIG. 12 for reasons of clarity.
  • the chip cake 102 After the chip cake 102 is transported through the medium pressure reaction zone 25 and the low pressure mold holding zone 26, it leaves the double belt press 89 as a hardened chipboard sheet 110 at the deflection drums 90 and 93. In the vertical direction further down, this chipboard sheet 110 can then be further processed.
  • a compression piston 111 At the deflecting drums 92 and 95 at the beginning of the wedge-shaped inlet zone 24, a compression piston 111, which has the shape of a wedge and extends across the width of the double belt press 89, is attached. This oscillates in the vertical direction in accordance with the double arrow 112 and thus compresses the chip cake 102 directly at the inlet into the wedge-shaped inlet zone 24.
  • the compression piston 111 thus acts like a pre-press, so that this can be saved in the embodiment described.
  • the oscillatory movement of the Compression piston 111 can be generated, for example, by means of two synchronously moved eccentrics 126, the movement of which is transmitted to the compression piston 111 via a crank rod 127.
  • the chip cake 102 can also be sprinkled onto only a horizontal section 99, either that of the left or right double belt half 103 or 104.
  • the feed part 52 for the hardener can be omitted.
  • the compression piston 111 contains in its lower part, which is assigned to the wedge-shaped tip, a sealing element 113 which is continuous in the transverse direction and has continuous nozzle bores 114 arranged next to one another. These nozzle bores 114 open into vertical guide tubes 115, which run in the compression piston 111 and are open at the top. In each guide tube 115 there is a closing needle 116, the upper end of which is connected to a frame 117 fixedly attached to the double belt press 89. The compression piston 111 oscillates in the vertical direction with respect to this frame 117.
  • the closing needles 116 close the nozzle bores 114 (see FIG. 13).
  • the upper opening of the guide tubes 115 is also closed by a thickened extension 118 in the upper part of the closing needles 116.
  • the openings of the nozzle bores 114 are completely released by the closing needles 116, while the upper openings of the guide tubes 115 continue to be closed by the thickened extension 118, as shown in FIG. 14.
  • the acidic or basic hardener is in the gaseous phase or in the binary phase with a gaseous carrier by means of a transverse manifold 120 located in the compression piston 111. From this manifold 120, the guide tubes 115 are supplied with the hardener. During the vertically downward compression movement of the compression piston 111, the openings of the nozzle bores 114 are released and the acidic or basic hardener penetrates into the center of the chip cake 102. When the compression piston 111 subsequently goes up again, the closing needles 116 close the nozzle bores 114 again, so that at this point in time no further hardener can escape into the chip cake 102.
  • the closing needles 116 have tips 121 at their lower ends. When the compression piston 111 moves vertically upward, these tips 121 engage in the nozzle bores 114 and push out resin residues which clog the nozzle bores 114 to the outside. If the acidic or basic hardener is fed to the chip cake 102 only via the compression piston 111, the openings 59 in the outer belt 32 can be omitted. In addition, it is sufficient if the press belt arrangements 22, 23 contain only a single press belt instead of an inner and outer belt.
  • the double belt press 89 can also be equipped with multi-layer belt packs 122.
  • the multi-layer belt packs 122 consist of several, without spacing press belts 123, 124, 125. These press belts 123, 124, 125 have no openings, since the hardener is not fed to the chip cake via the press belts.
  • Such multilayer belt packages 122 advantageously have a higher tensile strength than simple press belts and are also less sensitive to damage caused by foreign bodies running in the chip cake, such as lumps of resin, small metal particles, stones, etc.
  • the number of individual press belts of the multilayer belt package 122 can be selected as required.
  • the remaining configuration of the multi-layer tape packages can be done according to DE-OS 27 35 142.
  • press belt arrangements 22, 23 can not only be used on double belt presses for the production of wood-based panel webs.
  • Such a press belt arrangement 22, 23 can also be used particularly advantageously in double belt presses which are used for pressing web-shaped materials at elevated temperatures.
  • essentially press belt temperatures of up to approx. 220 ° C could be reached.
  • the lubricant for the rollers 33 of the roller bed, if it is a roller-based double belt press decomposes within a very short time.
  • the known materials for the sliding surface seal 39 are likewise only stable up to this temperature, so that temperatures higher than 220 ° C. have not hitherto been able to be reached reliably.
  • thermosetting and thermoplastic materials that require pressing temperatures of 350 ° C and more. Such materials have so far not been able to be produced continuously.
  • the outer belt 32 are heated to the temperature required by the material to be pressed before entering the reaction zone.
  • the inner band 31 is heated to a temperature which is just tolerable by the lubricant or the sliding surface seal 39. Since there is a distance between the outer band 32 and the inner band 31 and there is air in this space, the channels 41, which in turn acts as a thermal insulator, very little heat is transferred from the outer band 32 to the inner band 31.
  • the only places where such a heat flow could occur are the spacers 42. In this case, however, the embodiment for the spacer 42 will preferably be chosen, in which the slide bar 45 consists of a plastic, for example a polyimide.
  • the embodiment for the slide bar can also be selected, in which the slide bar consists of a metal body 46 and a slide surface 47.
  • the slide strips 45 are then equipped with the smallest possible cross section, so that they have a small cross section compared to the entire surface of the press belts and thus only a small heat flow between the outer belt 32 and inner belt 31 can occur, which is practically negligible.
  • the inner band 31 thus remains substantially at a lower temperature which is harmless to the lubricant and the sliding surface seals 39, while the outer band 32 maintains the higher temperature. As a result, the heat flow mainly enters the material to be pressed, as desired.
  • the supply part 52 is omitted.
  • the openings 59, 64 in the outer belt 32 and the inlet openings 61 in the inner belt 31 are then likewise not present. If necessary, the inner band 31 can be additionally cooled.
  • FIG. 9 shows a discontinuously operating device which realizes the method according to the invention.
  • This device consists of a stack press 71.
  • the chips are in turn glued without hardening, scattered to form a chip cake, cut into individual chip cake sections and then transported in cycles to the stack press.
  • Such parts of the plant are known per se and therefore do not need to be described further.
  • the stack press 71 which is shown in a section along the transverse direction in FIG. 9, the chip cake 72 is compressed when the press plates 73, 74 are closed and during the build-up of pressure.
  • the gaseous acidic or basic hardener or the hardener with the gaseous carrier agent is in turn fed via the pressure plates 73, 74 onto the surfaces of the chip cake 72, from where it penetrates into the chip cake 72 and starts the hardening reaction of the binder there .
  • bores 75 are made in the pressure plates 73, 74, which run parallel to the surface of the pressure plates. From these bores 75, vertical openings 76 lying one behind the other in the longitudinal direction, which are shown in the drawing for reasons of illustration with an exaggerated cross-section and spacing from one another, branch off from the press plate surface 77 facing the chip cake 72, via which the hardener opens from the bores 75 the surface of the chip cake 72 emerges. As soon as the compression phase has ended, the supply of the hardener is stopped. The chipboard is then pressed under a holding pressure until the binder has hardened.
  • a plurality of vertical openings 76 which are adjacent to one another in the transverse direction, can also emerge from a bore 75 in each case.
  • additional heat can also be supplied to the chip cake 72 via the gaseous hardener, the gaseous carrier means or by means of heat conduction from the pressure plates 73, 74.
  • the chipboard can also be cooled at the same time during the holding pressure.
  • a one-day press is used.
  • a discontinuous multi-day press can also be used. It is only important in this case that the acidic or basic hardener is supplied in gaseous form or in a binary phase with a gaseous carrier agent over the surfaces of the chip cake during the compression phase of the chip cake.

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Wood Science & Technology (AREA)
  • Forests & Forestry (AREA)
  • Mechanical Engineering (AREA)
  • Dry Formation Of Fiberboard And The Like (AREA)
EP87116121A 1986-11-14 1987-11-03 Méthode et appareil pour la fabrication des panneaux de fibres de bois Expired - Lifetime EP0267516B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19863639061 DE3639061C2 (de) 1986-11-14 1986-11-14 Verfahren und Vorrichtungen zur Herstellung von Holzwerkstoffplatten
DE3639061 1986-11-14

Publications (3)

Publication Number Publication Date
EP0267516A2 true EP0267516A2 (fr) 1988-05-18
EP0267516A3 EP0267516A3 (en) 1989-11-15
EP0267516B1 EP0267516B1 (fr) 1993-01-20

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EP87116121A Expired - Lifetime EP0267516B1 (fr) 1986-11-14 1987-11-03 Méthode et appareil pour la fabrication des panneaux de fibres de bois

Country Status (5)

Country Link
US (3) US4802837A (fr)
EP (1) EP0267516B1 (fr)
JP (1) JPS63212503A (fr)
CN (1) CN1009443B (fr)
RU (1) RU1833305C (fr)

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EP0383572A2 (fr) * 1989-02-14 1990-08-22 Csr Limited Procédé et appareil pour fabriquer des produits en fibres en longueur continue
FR2648744A1 (fr) * 1989-06-26 1990-12-28 Borden Inc Methode pour lier une matiere lignocellulosique en presence d'esters a l'etat gazeux
WO1991004142A1 (fr) * 1989-09-15 1991-04-04 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Procede d'extrusion a plat pour la fabrication de materiaux en bois lies par un produit inorganique ou organique, en particulier les panneaux stratifies
EP0776742A1 (fr) * 1995-11-29 1997-06-04 De Pretto-Escher Wyss s.r.l. Dispositif pour la fabrication de panneaux de particles, panneaux de fibres ou autre
WO1998025744A1 (fr) * 1996-12-11 1998-06-18 Boise Cascade Corporation Dispositif et procede de formation continue de composites comprenant une matiere de charge et une matiere thermosensible, et produits ainsi fabriques
US6605245B1 (en) 1997-12-11 2003-08-12 Boise Cascade Corporation Apparatus and method for continuous formation of composites having filler and thermoactive materials
US6821614B1 (en) 1996-12-11 2004-11-23 Boise Cascade Corporation Apparatus and method for continuous formation of composites having filler and thermoactive materials, and products made by the method
DE10314623B3 (de) * 2003-04-01 2005-01-13 Kronotec Ag Vorrichtung und Verfahren zur Herstellung von Holzwerkstoffplatten
WO2005054600A1 (fr) * 2003-12-04 2005-06-16 Hamberger Industriewerke Gmbh Carreau
CN103158188A (zh) * 2013-03-05 2013-06-19 黑龙江华信家具有限公司 低碳制作环保防变形板材的方法
WO2017118531A1 (fr) * 2016-01-04 2017-07-13 Fritz Egger Gmbh & Co. Og Panneau de fibres à résistance accrue contre toute attaque fongique, et procédé de fabrication
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US6599621B2 (en) * 2001-03-20 2003-07-29 William H. Porter High strength structural insulated panel
WO2003026878A1 (fr) * 2001-09-26 2003-04-03 Hunstman International Llc Systeme de moulage equipe d'un element mobile a liberation automatique
US6989116B2 (en) * 2003-02-18 2006-01-24 Weyerhaeuser Company Compressed composite product formation and transport method
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WO2016160613A1 (fr) * 2015-03-27 2016-10-06 Spitler Charles Douglas Caractéristiques de rigidité de peau, et procédé et système de production de commande de gonflant avec une teneur en humidité variable dans une fibre de verre d'entrée
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Cited By (17)

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Publication number Priority date Publication date Assignee Title
EP0383572A3 (fr) * 1989-02-14 1992-01-22 Csr Limited Procédé et appareil pour fabriquer des produits en fibres en longueur continue
EP0383572A2 (fr) * 1989-02-14 1990-08-22 Csr Limited Procédé et appareil pour fabriquer des produits en fibres en longueur continue
FR2648744A1 (fr) * 1989-06-26 1990-12-28 Borden Inc Methode pour lier une matiere lignocellulosique en presence d'esters a l'etat gazeux
BE1003585A5 (fr) * 1989-06-26 1992-04-28 Borden Inc Procede de liaison de matiere lignocellulosique avec des esters gazeux.
WO1991004142A1 (fr) * 1989-09-15 1991-04-04 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Procede d'extrusion a plat pour la fabrication de materiaux en bois lies par un produit inorganique ou organique, en particulier les panneaux stratifies
EP0776742A1 (fr) * 1995-11-29 1997-06-04 De Pretto-Escher Wyss s.r.l. Dispositif pour la fabrication de panneaux de particles, panneaux de fibres ou autre
US6863512B2 (en) 1996-12-11 2005-03-08 Officemax Incorporated Apparatus and method for continuous formation of composites having filler and thermoactive materials, and products made by the method
WO1998025744A1 (fr) * 1996-12-11 1998-06-18 Boise Cascade Corporation Dispositif et procede de formation continue de composites comprenant une matiere de charge et une matiere thermosensible, et produits ainsi fabriques
US6200682B1 (en) 1996-12-11 2001-03-13 Boise Cascade Corporation Apparatus and method for continuous formation of composites having filler and thermoactive materials and products made by the method
US6821614B1 (en) 1996-12-11 2004-11-23 Boise Cascade Corporation Apparatus and method for continuous formation of composites having filler and thermoactive materials, and products made by the method
US6605245B1 (en) 1997-12-11 2003-08-12 Boise Cascade Corporation Apparatus and method for continuous formation of composites having filler and thermoactive materials
DE10314623B3 (de) * 2003-04-01 2005-01-13 Kronotec Ag Vorrichtung und Verfahren zur Herstellung von Holzwerkstoffplatten
WO2005054600A1 (fr) * 2003-12-04 2005-06-16 Hamberger Industriewerke Gmbh Carreau
CN103158188A (zh) * 2013-03-05 2013-06-19 黑龙江华信家具有限公司 低碳制作环保防变形板材的方法
CN103158188B (zh) * 2013-03-05 2015-01-21 张福贵 低碳制作环保防变形板材的方法
WO2017118531A1 (fr) * 2016-01-04 2017-07-13 Fritz Egger Gmbh & Co. Og Panneau de fibres à résistance accrue contre toute attaque fongique, et procédé de fabrication
WO2019110217A1 (fr) * 2017-12-04 2019-06-13 Siempelkamp Maschinen- Und Anlagenbau Gmbh Barre rotative

Also Published As

Publication number Publication date
EP0267516A3 (en) 1989-11-15
US4923656A (en) 1990-05-08
EP0267516B1 (fr) 1993-01-20
RU1833305C (en) 1993-08-07
US4895508A (en) 1990-01-23
CN87107124A (zh) 1988-05-25
JPS63212503A (ja) 1988-09-05
CN1009443B (zh) 1990-09-05
US4802837A (en) 1989-02-07

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