CA1113800A - Process and device for continuously mixing wood chips with binder - Google Patents
Process and device for continuously mixing wood chips with binderInfo
- Publication number
- CA1113800A CA1113800A CA312,422A CA312422A CA1113800A CA 1113800 A CA1113800 A CA 1113800A CA 312422 A CA312422 A CA 312422A CA 1113800 A CA1113800 A CA 1113800A
- Authority
- CA
- Canada
- Prior art keywords
- binder
- drum
- wood chips
- air
- accordance
- 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.)
- Expired
Links
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
- B27N1/00—Pretreatment of moulding material
- B27N1/02—Mixing the material with binding agent
- B27N1/0218—Mixing the material with binding agent in rotating drums
Abstract
ABSTRACT OF THE DISCLOSURE
A process and apparatus for continuously mixing wood chips with a binder finely divided in air, the wood chips falling through a mixing drum in the form of thin layers with the air moving approximately perpendicularly to the direction of falling in a pulsating fashion.
A process and apparatus for continuously mixing wood chips with a binder finely divided in air, the wood chips falling through a mixing drum in the form of thin layers with the air moving approximately perpendicularly to the direction of falling in a pulsating fashion.
Description
~ ~ ~ 38~ ~
PROCESS AND DEVICE FOR CONTINUOUSLY klIXING
WOOD CHIPS WITH BINDER
FIELD OF T~ INVENTION
The invention relates to a process for continuously mixing wood chips with a binder, in particular a binder in powder form, whereby the binder is finely divided in air and the wood chips are moved by this air, and apparatus for carry-ing out this process consisting of a cylindrical mixing drumrotatable about its center lengthwise with an inlet or the wood chips in one end and an outlet for the wood chips coa~ed with binder at the other end, of components built in for lift-ing wood chips from a chip bed located in the mixing drum, and o~ means for dispersing binder in the interior space of the mixing drum.
' : , _ CKGROUND OF THE INVENTION ~-Germ~n Oenlegungsschrit 16 53 181 teaches a device for wetting wood fibers with liquid binder, which device has a mixing drum rotatable about its center lengthwise axis. In a Ci~ed position with respec~ to the mixing drum the device consists o one spiked roller wi~h a cover ptate or two spiked rollers rotating in opposite directions located in the vicinity of the ascending mixing drum wal~ by means of which device wood fibers rising with the mixing drum wall are thrown back at the same speed and in the same direc~ion to the wood fiber bed located in the lower region of the mixing drum. Spray nozzles which spray liquid binder onto the wood fibers as they ~ove by are located immediately above this trajectory. With this device, insuficiently uni~orm distribution of the binder on the wood fibers is unavoidable. The same is true when such a devic is used for coating wood chips with glue. The reason for this is that the binder sprayed directly onto the wood fibers cannot be sub; cted to a distribu~ion process on the surfaces of the fibers.
~' It is already kno~n that po~dered binder can be blown onto the wood chips together with compressed air by means of devices with the same basic design. Here, too, nonuniform distribution of the binder is unavoidable.
Furthenmore, removal of the air int~oduced additionally into the interior space of the mixing drum poses considerable problems.
SUM~RY OF THE INVENTION
An object of the present invention is to create a method and apparatus of the type described in the pre-amble hereof by means of which optimum distribution of the binder on the surace o the wood chips is achieved at a lower cost.
This problem is solved in a process of the type described in the preamble by the chips being moved in the fonm o~ thin descending layers, whereby these layers are alternately moved in the direction of the perpendiculars normal to their surfaces, and whereby the air which keeps the binder in suspension is moved in puls~s approximately per- ;
pendicularly to the direction of falling and at right angles to the perpendiculars to the surface, The tran8verse move-ment of the wood chip layers produced forms continuously ; changing low-pressure and high-pressure areas into which the binder held in suspension by the air penetrates and out of which it flows away, producing continuously pulsating air streams which flow past the large surfaces of the wood chips, whereby the binder suspended in the air in a very fine distribution is deposited on the wood chip surfaces uni~ormly and in a very finely divided state from the air by condensation or like the settling of dust.
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~ The process according to the invention ~s therefore parti-cularly advantageous if only very small binder particles, namely about 2-5% of the wood chips, are to be distributed ' uniformly on the wood chips. Thus in the process according to the invention there is no distribution of glue on the wood chips by means of higher kinetic energy, but by means ' of an additional intimate mixing process which is produced ,~
' by the axially pulsating air streams and the layers of wood chips moved perpendicularly th'ereto.
The problem of the invention is solved by means of an apparatus of the type described in the preamble by providing open pockets in ~he,inside wall of the mixing drum and in its direction o~ rota~ion. These pockets become filled as they pass through the chip bed located in the lower part o the mixing drum and empty as the responding drum wall xises. Since, due to their movement in a circular path, these pockets also execute a movement at right angles to the drum axis, these wood chip layers produced by the pockets move in the manner described.
BRIEF DESCRIPT'lO~ OF THE DP~WINGS
Other advantages and features of the invention,will " emerge rom the subclaims and the description hereinbelow of one embodiment with reference to the drawing. In the drawing Flgure 1 shows schematically a vertical side view of the device according to the inven~ion;
Figure 2 is a cross-sectional view taken along the line II-II in Figure 1, and ' Figure 3 is a partial perspective view of the interior space of the mixing drum.
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DESCRIPrION OF PREFERRED E~IBODIMF.NTS
The device shown in the drawing has a cylindrical mixing drum 1 which has the comparatively large diameter o
PROCESS AND DEVICE FOR CONTINUOUSLY klIXING
WOOD CHIPS WITH BINDER
FIELD OF T~ INVENTION
The invention relates to a process for continuously mixing wood chips with a binder, in particular a binder in powder form, whereby the binder is finely divided in air and the wood chips are moved by this air, and apparatus for carry-ing out this process consisting of a cylindrical mixing drumrotatable about its center lengthwise with an inlet or the wood chips in one end and an outlet for the wood chips coa~ed with binder at the other end, of components built in for lift-ing wood chips from a chip bed located in the mixing drum, and o~ means for dispersing binder in the interior space of the mixing drum.
' : , _ CKGROUND OF THE INVENTION ~-Germ~n Oenlegungsschrit 16 53 181 teaches a device for wetting wood fibers with liquid binder, which device has a mixing drum rotatable about its center lengthwise axis. In a Ci~ed position with respec~ to the mixing drum the device consists o one spiked roller wi~h a cover ptate or two spiked rollers rotating in opposite directions located in the vicinity of the ascending mixing drum wal~ by means of which device wood fibers rising with the mixing drum wall are thrown back at the same speed and in the same direc~ion to the wood fiber bed located in the lower region of the mixing drum. Spray nozzles which spray liquid binder onto the wood fibers as they ~ove by are located immediately above this trajectory. With this device, insuficiently uni~orm distribution of the binder on the wood fibers is unavoidable. The same is true when such a devic is used for coating wood chips with glue. The reason for this is that the binder sprayed directly onto the wood fibers cannot be sub; cted to a distribu~ion process on the surfaces of the fibers.
~' It is already kno~n that po~dered binder can be blown onto the wood chips together with compressed air by means of devices with the same basic design. Here, too, nonuniform distribution of the binder is unavoidable.
Furthenmore, removal of the air int~oduced additionally into the interior space of the mixing drum poses considerable problems.
SUM~RY OF THE INVENTION
An object of the present invention is to create a method and apparatus of the type described in the pre-amble hereof by means of which optimum distribution of the binder on the surace o the wood chips is achieved at a lower cost.
This problem is solved in a process of the type described in the preamble by the chips being moved in the fonm o~ thin descending layers, whereby these layers are alternately moved in the direction of the perpendiculars normal to their surfaces, and whereby the air which keeps the binder in suspension is moved in puls~s approximately per- ;
pendicularly to the direction of falling and at right angles to the perpendiculars to the surface, The tran8verse move-ment of the wood chip layers produced forms continuously ; changing low-pressure and high-pressure areas into which the binder held in suspension by the air penetrates and out of which it flows away, producing continuously pulsating air streams which flow past the large surfaces of the wood chips, whereby the binder suspended in the air in a very fine distribution is deposited on the wood chip surfaces uni~ormly and in a very finely divided state from the air by condensation or like the settling of dust.
.: . . . , " , ' ~ ,:
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~ The process according to the invention ~s therefore parti-cularly advantageous if only very small binder particles, namely about 2-5% of the wood chips, are to be distributed ' uniformly on the wood chips. Thus in the process according to the invention there is no distribution of glue on the wood chips by means of higher kinetic energy, but by means ' of an additional intimate mixing process which is produced ,~
' by the axially pulsating air streams and the layers of wood chips moved perpendicularly th'ereto.
The problem of the invention is solved by means of an apparatus of the type described in the preamble by providing open pockets in ~he,inside wall of the mixing drum and in its direction o~ rota~ion. These pockets become filled as they pass through the chip bed located in the lower part o the mixing drum and empty as the responding drum wall xises. Since, due to their movement in a circular path, these pockets also execute a movement at right angles to the drum axis, these wood chip layers produced by the pockets move in the manner described.
BRIEF DESCRIPT'lO~ OF THE DP~WINGS
Other advantages and features of the invention,will " emerge rom the subclaims and the description hereinbelow of one embodiment with reference to the drawing. In the drawing Flgure 1 shows schematically a vertical side view of the device according to the inven~ion;
Figure 2 is a cross-sectional view taken along the line II-II in Figure 1, and ' Figure 3 is a partial perspective view of the interior space of the mixing drum.
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DESCRIPrION OF PREFERRED E~IBODIMF.NTS
The device shown in the drawing has a cylindrical mixing drum 1 which has the comparatively large diameter o
2 to 3 meters. It is provided around i~s outer periphery with support rings 2 extending all around it, these support rings being associated pairwise with support rollers 3, 4. A support roller pair 3 located in one radial plane and associated with a support ring 2 is provided with guide rings 5 gripping one side of the associa~ed support ring 2, so that mixing drum 1 is nondisplaceably mounted on guide rollers 3, 4 in the direction of its central lengthwise axis 6. Support rollers 3, 4, each of which is on one side, are nonrotatably mounted on a common shaft 7 which in its turn is mounted on pedestals 8, 9~ Pedestals 8, 9 are mounted on a base frame 10. This base frame is mounted 15 at one en~ namely the end adjacent to outlet chute 11 of mixing -~
drum 1 with respect to floor 13 by means of a pivot 12, the swivelin axis 14 o said base frame running horiæontally and perpendicu-larly to central lengthwise axis 6. At its other end adjacent to an inlet chute 15, the base frame is supported on both sides by means of threaded spindles 16 with respect to floor 13, so that the angle of mixing drum 1 to the horizontal can be alteret in such a manner that mixing drum l can be tilted slightly downward from inlet chute 15 to outlet chute 11.
One of the two shafts 7 is provided at one free end with a V-belt pulley 17 drivable by means of V-belt 18 by a fixed drive motor 19 thereby causing mixing drum 1 to rotate.
The end of mixing drum l facing inlet chute 15 is closed off by a circular end wall 20 on which inlet chute lS is mounted, with an associated inlet aperture 21 in said end wall 20 providing a passage into the interior 22 of mixing drum 1. Inlet chute 15 and hence end wall 20 is supported by suppo~ts 23 with respect to base frame 10, namely end wall 20 is fixed with respect to base frame 10 and does not rotate ~ 3~
~ .
with mixing drum 1. If desired, profiled joints 24 are provided on its periphery, which joints provide a sub-stantially dust-proof seal between end wall 20 and mix- ~ -~
ing drum 1.
S An end wall 25 is provided in front of the end wall associated with outlet chute 11, which wall is also supported on base frame 10 andldoes not rotate with the ~-.~. , .
drum and which wall has an outlet aperture 26 providing a passage into outlet chute 11. Outlet chute 11 is firmly mounted on this end wall ~5.
Inlet chute 15 is located upstream of a conveyor type weigher 27, shown schematically in the drawing, which in lts turn is associated wlth a volumetrically dispensing delivery device (not shown) of a hopper. This conveyor type weigher 27 has a gravimetrically operating control device and the volumetrically dispensing delivery device of a hopper located upstream of it, connected to a control circuit so that a continuous stream of wood ships in a precisely preset quantity by weight per unit time is fed in~o mixing drum 1 through inlet chute l5. The a~ore-mentioned dispensing devices are traditional and generally known.
Further~ore, a hopper 28 for powdered binder is provided, which binder is removed from the hopper through a volumetrically operating dispensing unit 29 in the form o a screw conveyor and fed by means of a gravimetrically . .
operating control unit in the form of a conveyor type weigher. Drive 31 o dispensing unit 29 and control unit 30 are also connected in a closed control circuit so that a continuous stream of po~ered binder with a preset quantity by weight per unit time leaves control device 30. This ~' _5_ .~ .
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flow of material is fed into the interior 22 of mixing drum 1 through end wall 20 by means o a screw conveyor driven by drive 32. A swirling device 35 in the form of a propeller is mounted on shaft 34 of screw conveyor 33, at its end located in interior 22, which s~irling device divides the powdered binder leaving screw conveyor 33 and swirls it around.
~-~ The propeller is driven at a correspondingly high speed.
Alternatively to or cumulatively with this feed device for powdered binder, one or more nozzles 36 pro-jecting into interior 22 are provided in end wall 20, whichnozzles are connected via a metering pump 37 to a supply tank 38 for liquid binder, so that liquid binder can be injected into interior 22 in a very finely divided fonm and in specific preset quantities by weigh~ per unit time.
Shovel-like plates 43, 44 are provided on the inner wall 39 of mixing drum 1 in axially consecutive cylinder sections, of which only three cylinder sections 40, 41, 42 are sho~n, which pla~es 43, 44, are distributed equidistantly around the periphery, and are disposed respect~velg in two adjacen~ cylinder sections 40, 41 in such a way that they a~e staggered with respect to each other around the periphery of inner wall 39 by half the distance between two pla~es h3 or 44 in one cylinder section 40 or 41.
Shovel-like plates 43 as viewed from the outside to the in-sid~ are pitched in the rotational direction 45 of the mixingdrum with respect to the corresponding radius, so that a ; pocket 46 is formed between plate 43 and 44 and the associated section of inner wall 39 of mixing drum 1. As the drum moves in rotational direction 45, a specific quantity of wood chips is scooped up from the wood chip bed 47 in the lower part of mixing drum 1 into such a poc~et 46. These wood chips in ' ' - - .
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pocket 46 flow over the inner edge 48 o plate 43, 44 as the drum rotates, in the form of a relatively thin parabolic layer 49, 50 back into wood chip bed 47. As may be seen rom Figure 2, a wood chip layer 49, from the beginning of empty-ing of a pocket 46 former by a plate 43 until completeemptying migrates transversely through the mixing drum 1 so that - between this layer 49 and the part of inner wall 39 turned toward it (on the left in Figure 2) a space Sl is produced which enlarges as the pocket empties, in which space a certain negati~re pressure arises as it steadily increases in size.
As may be seen from Figure 3, because of the staggered arrangement of plates 43, 44 in adjacent cylinder sections 40, 41 or 41, 42, the layers 49, 50 which form are also staggered with respect with one another so that the negative pressure developing in the individual spaces 51 behind layers 49, 50 can be equalizçd by axial air flows in the directions shown by arrows S2, 53. Because, in each cylinder section 40, 41, , , ~ 42, several plates 43, 44 are located on the periphery of ,;!~ 20 in-.cr wall 39 of mixing drum 1, axiall~ pulsating air stseams in the direction of arrows 52, 53 develop, and these cause the powdered or droplet-shaped binder particles suspended in interior 22 to be dra~n with them into space 51, and also to pulsate in the axial direction, hence arriving on the surfaces of the individual wood chips in a very finely dlvided form. Furthermore, when a layer 49 or 50 breaks up when a pocket 46 is completely empty, pressure equali-~ ~ation takes place a~ right angles to the lengthwise axis 6 .' in the direction of arrow 54 in Figure 2, wh ~eby in the region where, shortly before, a space 51 had been undernegative pressure, a slight e~cess pressure now develops.
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This causes an interplay of axially and radially pulsating negative pressure and excess pressure waves, which cause extremely fine division of the binder particles throughout the interior 22 of mixing drum 1 and an extremely fine distribution of the binder particles over the individual ` wood chips.
In order to distribute the suspended binder, both po~dered and liquid, throughout the entire interior 22 of mixing drum 1, screw conveyor 33 on the one hand and nozzies 36 on the other, as shown in Figure 7, tenminate in the vicinity of that part of interior 22 toward which layers 49, 50 do no~ migrate, so that the binder is not sprayed directly onto the wood chips.
As may be seen from Figures 2 and 3, layers 49, 50 are thin by comparison to their width, which corresponds approxi-mately to the axial exten~ of plates 43, 44.
The above-mentioned transverse movement of layers 49, 50 in mixing drum 1 is approximately in the direction of the normals to the surfaces of these layers, which normals extend approximately cppo3ite to the direct~onarro~ 54.
By means of swirling device 35, air streams are also generated in the lengthwise direction of mixing drum 1, which streams reinforce the above-mentioned axially pulsating air streams and, in the same way as these air streams, generate air streams across both large surfaces of layers 49, 50.
! It will be obvious to tho~e skilled in the art that various changes may be made without departing from the scope of the invention and the invention is not to be considered limited to what is shown in the drawings and described in the specification.
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drum 1 with respect to floor 13 by means of a pivot 12, the swivelin axis 14 o said base frame running horiæontally and perpendicu-larly to central lengthwise axis 6. At its other end adjacent to an inlet chute 15, the base frame is supported on both sides by means of threaded spindles 16 with respect to floor 13, so that the angle of mixing drum 1 to the horizontal can be alteret in such a manner that mixing drum l can be tilted slightly downward from inlet chute 15 to outlet chute 11.
One of the two shafts 7 is provided at one free end with a V-belt pulley 17 drivable by means of V-belt 18 by a fixed drive motor 19 thereby causing mixing drum 1 to rotate.
The end of mixing drum l facing inlet chute 15 is closed off by a circular end wall 20 on which inlet chute lS is mounted, with an associated inlet aperture 21 in said end wall 20 providing a passage into the interior 22 of mixing drum 1. Inlet chute 15 and hence end wall 20 is supported by suppo~ts 23 with respect to base frame 10, namely end wall 20 is fixed with respect to base frame 10 and does not rotate ~ 3~
~ .
with mixing drum 1. If desired, profiled joints 24 are provided on its periphery, which joints provide a sub-stantially dust-proof seal between end wall 20 and mix- ~ -~
ing drum 1.
S An end wall 25 is provided in front of the end wall associated with outlet chute 11, which wall is also supported on base frame 10 andldoes not rotate with the ~-.~. , .
drum and which wall has an outlet aperture 26 providing a passage into outlet chute 11. Outlet chute 11 is firmly mounted on this end wall ~5.
Inlet chute 15 is located upstream of a conveyor type weigher 27, shown schematically in the drawing, which in lts turn is associated wlth a volumetrically dispensing delivery device (not shown) of a hopper. This conveyor type weigher 27 has a gravimetrically operating control device and the volumetrically dispensing delivery device of a hopper located upstream of it, connected to a control circuit so that a continuous stream of wood ships in a precisely preset quantity by weight per unit time is fed in~o mixing drum 1 through inlet chute l5. The a~ore-mentioned dispensing devices are traditional and generally known.
Further~ore, a hopper 28 for powdered binder is provided, which binder is removed from the hopper through a volumetrically operating dispensing unit 29 in the form o a screw conveyor and fed by means of a gravimetrically . .
operating control unit in the form of a conveyor type weigher. Drive 31 o dispensing unit 29 and control unit 30 are also connected in a closed control circuit so that a continuous stream of po~ered binder with a preset quantity by weight per unit time leaves control device 30. This ~' _5_ .~ .
.", ~;i 3~
.
flow of material is fed into the interior 22 of mixing drum 1 through end wall 20 by means o a screw conveyor driven by drive 32. A swirling device 35 in the form of a propeller is mounted on shaft 34 of screw conveyor 33, at its end located in interior 22, which s~irling device divides the powdered binder leaving screw conveyor 33 and swirls it around.
~-~ The propeller is driven at a correspondingly high speed.
Alternatively to or cumulatively with this feed device for powdered binder, one or more nozzles 36 pro-jecting into interior 22 are provided in end wall 20, whichnozzles are connected via a metering pump 37 to a supply tank 38 for liquid binder, so that liquid binder can be injected into interior 22 in a very finely divided fonm and in specific preset quantities by weigh~ per unit time.
Shovel-like plates 43, 44 are provided on the inner wall 39 of mixing drum 1 in axially consecutive cylinder sections, of which only three cylinder sections 40, 41, 42 are sho~n, which pla~es 43, 44, are distributed equidistantly around the periphery, and are disposed respect~velg in two adjacen~ cylinder sections 40, 41 in such a way that they a~e staggered with respect to each other around the periphery of inner wall 39 by half the distance between two pla~es h3 or 44 in one cylinder section 40 or 41.
Shovel-like plates 43 as viewed from the outside to the in-sid~ are pitched in the rotational direction 45 of the mixingdrum with respect to the corresponding radius, so that a ; pocket 46 is formed between plate 43 and 44 and the associated section of inner wall 39 of mixing drum 1. As the drum moves in rotational direction 45, a specific quantity of wood chips is scooped up from the wood chip bed 47 in the lower part of mixing drum 1 into such a poc~et 46. These wood chips in ' ' - - .
' . ., ~ , :
.', '~' ~ . ~
pocket 46 flow over the inner edge 48 o plate 43, 44 as the drum rotates, in the form of a relatively thin parabolic layer 49, 50 back into wood chip bed 47. As may be seen rom Figure 2, a wood chip layer 49, from the beginning of empty-ing of a pocket 46 former by a plate 43 until completeemptying migrates transversely through the mixing drum 1 so that - between this layer 49 and the part of inner wall 39 turned toward it (on the left in Figure 2) a space Sl is produced which enlarges as the pocket empties, in which space a certain negati~re pressure arises as it steadily increases in size.
As may be seen from Figure 3, because of the staggered arrangement of plates 43, 44 in adjacent cylinder sections 40, 41 or 41, 42, the layers 49, 50 which form are also staggered with respect with one another so that the negative pressure developing in the individual spaces 51 behind layers 49, 50 can be equalizçd by axial air flows in the directions shown by arrows S2, 53. Because, in each cylinder section 40, 41, , , ~ 42, several plates 43, 44 are located on the periphery of ,;!~ 20 in-.cr wall 39 of mixing drum 1, axiall~ pulsating air stseams in the direction of arrows 52, 53 develop, and these cause the powdered or droplet-shaped binder particles suspended in interior 22 to be dra~n with them into space 51, and also to pulsate in the axial direction, hence arriving on the surfaces of the individual wood chips in a very finely dlvided form. Furthermore, when a layer 49 or 50 breaks up when a pocket 46 is completely empty, pressure equali-~ ~ation takes place a~ right angles to the lengthwise axis 6 .' in the direction of arrow 54 in Figure 2, wh ~eby in the region where, shortly before, a space 51 had been undernegative pressure, a slight e~cess pressure now develops.
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This causes an interplay of axially and radially pulsating negative pressure and excess pressure waves, which cause extremely fine division of the binder particles throughout the interior 22 of mixing drum 1 and an extremely fine distribution of the binder particles over the individual ` wood chips.
In order to distribute the suspended binder, both po~dered and liquid, throughout the entire interior 22 of mixing drum 1, screw conveyor 33 on the one hand and nozzies 36 on the other, as shown in Figure 7, tenminate in the vicinity of that part of interior 22 toward which layers 49, 50 do no~ migrate, so that the binder is not sprayed directly onto the wood chips.
As may be seen from Figures 2 and 3, layers 49, 50 are thin by comparison to their width, which corresponds approxi-mately to the axial exten~ of plates 43, 44.
The above-mentioned transverse movement of layers 49, 50 in mixing drum 1 is approximately in the direction of the normals to the surfaces of these layers, which normals extend approximately cppo3ite to the direct~onarro~ 54.
By means of swirling device 35, air streams are also generated in the lengthwise direction of mixing drum 1, which streams reinforce the above-mentioned axially pulsating air streams and, in the same way as these air streams, generate air streams across both large surfaces of layers 49, 50.
! It will be obvious to tho~e skilled in the art that various changes may be made without departing from the scope of the invention and the invention is not to be considered limited to what is shown in the drawings and described in the specification.
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Claims (14)
OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A process for continuous mixing of wood chips with a binder, comprising moving said wood chips through the binder which is finely divided in air, said chips being moved through the air in the form of thin falling layers wherein said layers are alternately displaced approximately in the direction of the normals of their surfaces; and moving said air, which keeps the binder in a state of suspension, approximately perpendicu-larly to the direction of falling and perpendicularly to the normals to their surfaces in a pulsating fashion.
2. A process in accordance with claim 1 wherein said binder is in powdered form.
3. A process in accordance with claim 1, wherein said binder is in liquid form.
4. A process in accordance with claim 1, wherein said binder is in liquid and powdered form.
5. Apparatus for continuously mixing wood chips with a binder, comprising a cylindrical mixing drum drivable about its central lengthwise axis, said drum having an inlet aperture for the wood chips in one end wall and an outlet aperture for the wood chips coated with binder in the other end wall, built in pockets provided on the inner wall of said drum, said pockets being open in the rotational direction of said drum, to scoop up wood chips from a chip bed located in the bottom of said drum, and means for distributing the binder in the interior of the mixing drum.
6. An apparatus in accordance with claim 5, wherein said binder is in liquid form.
7. An apparatus in accordance with claim 5, wherein said binder is in powdered form.
8. An apparatus in accordance with claim 5, wherein said binder is in liquid and powdered form.
9. Apparatus according to Claim 5, wherein several said pockets are disposed in axially consecutively disposed cylinder sections of said drum, and wherein said pockets provided in adjacent cylinder sections are staggered tangentially with respect to one another.
10. Apparatus according to Claim 5, wherein said pockets are formed by plates provided on the inside wall of said drum.
11. Apparatus according to Claim 5, wherein an air swirling device is provided in the interior of said drum, causing air to swirl in the lengthwise direction thereof.
12. Apparatus according to Claim 5, wherein said means for distributing said binder terminate in the area of the interior of said drum, which is associated with the descending part of said drum wall.
13. Apparatus according to Claim 11, wherein a screw conveyor is provided for introducing said binder, said screw conveyor terminating in the area of said air swirling device in the interior of said mixing drum.
14. Apparatus according to Claim 11, wherein a screw conveyor is provided for introducing said binder, said screw conveyor terminating in the area of said air swirling device, and wherein a propeller coupled with said screw conveyor is provided as the air swirling device.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19772744522 DE2744522A1 (en) | 1977-10-04 | 1977-10-04 | PROCESS AND DEVICE FOR CONTINUOUS MIXING OF WOOD SHADES WITH BINDERS |
| DEP2744522.3 | 1977-10-04 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1113800A true CA1113800A (en) | 1981-12-08 |
Family
ID=6020585
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA312,422A Expired CA1113800A (en) | 1977-10-04 | 1978-09-29 | Process and device for continuously mixing wood chips with binder |
Country Status (3)
| Country | Link |
|---|---|
| US (1) | US4188130A (en) |
| CA (1) | CA1113800A (en) |
| DE (1) | DE2744522A1 (en) |
Families Citing this family (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4378871A (en) * | 1978-02-06 | 1983-04-05 | Clark James D A | Method of producing smooth-uniform streams of semi-pourable fibrous particles |
| DE2837435B2 (en) * | 1978-08-28 | 1981-06-25 | Friedrich Horst 5840 Schwerte Papenmeier | Process and device for processing PVC powder |
| DE3324106A1 (en) * | 1983-07-05 | 1985-01-17 | Draiswerke Gmbh, 6800 Mannheim | METHOD FOR GLUING WOOD CHIPS AND THE LIKE WITH LIQUID GLUE AND DEVICE FOR CARRYING OUT THE METHOD |
| DE3503896A1 (en) * | 1985-02-06 | 1986-08-07 | Draiswerke Gmbh, 6800 Mannheim | LINING FOR A CONTAINER OF A MIXER |
| US5071675A (en) * | 1989-03-20 | 1991-12-10 | Weyerhaeuser Company | Method of applying liquid sizing of alkyl ketene dimer in ethanol to cellulose fibers entrained in a gas stream |
| US5432000A (en) * | 1989-03-20 | 1995-07-11 | Weyerhaeuser Company | Binder coated discontinuous fibers with adhered particulate materials |
| US5498478A (en) * | 1989-03-20 | 1996-03-12 | Weyerhaeuser Company | Polyethylene glycol as a binder material for fibers |
| US5230959A (en) | 1989-03-20 | 1993-07-27 | Weyerhaeuser Company | Coated fiber product with adhered super absorbent particles |
| US5064689A (en) * | 1989-03-20 | 1991-11-12 | Weyerhaeuser Company | Method of treating discontinuous fibers |
| US5057166A (en) * | 1989-03-20 | 1991-10-15 | Weyerhaeuser Corporation | Method of treating discontinuous fibers |
| US5173122A (en) * | 1991-01-04 | 1992-12-22 | Tilby Sydney E | Apparatus for washing sugarcane billets |
| CA2126240A1 (en) * | 1991-12-17 | 1993-06-24 | Paul Gaddis | Hopper blender system and method for coating fibers |
| US6162496A (en) * | 1996-05-20 | 2000-12-19 | Blue; David | Method of mixing |
| US6517232B1 (en) | 1996-05-20 | 2003-02-11 | Becker-Underwood, Inc. | Mixing systems |
| US6193410B1 (en) | 1998-12-16 | 2001-02-27 | Puckett, Ii Robert A. | Method for agitating the liquid contents of paint balls |
| US6551401B1 (en) | 2000-10-19 | 2003-04-22 | Becker-Underwood, Inc. | Machine for coloring landscaping material |
| DE20112599U1 (en) * | 2001-08-01 | 2002-12-19 | Kronospan Tech Co Ltd | MDF board and manufacture |
| US20050230073A1 (en) * | 2004-04-06 | 2005-10-20 | Thi International Llc | Apparatus and method for treating mulch |
| DE202004008213U1 (en) * | 2004-05-18 | 2004-08-05 | Hfhn Wood Engineering Gmbh | gluing device |
| RU2648388C1 (en) * | 2017-07-10 | 2018-03-26 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Поволжский государственный технологический университет" | Device for wood concrete manufacturing |
| CN109529705A (en) * | 2018-11-29 | 2019-03-29 | 黄仕平 | A kind of feed addition mixing arrangement |
| US11833711B2 (en) | 2018-12-23 | 2023-12-05 | Louisiana-Pacific Corp. | Blending apparatus for manufactured wood processing |
| US20230019663A1 (en) * | 2020-01-23 | 2023-01-19 | Hans W. Fechner | Method of glue-coating plant particles |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2761420A (en) * | 1953-07-13 | 1956-09-04 | Long Bell Lumber Company | Apparatus for applying sprayable materials to solid particles |
| US3407511A (en) * | 1967-05-16 | 1968-10-29 | American Hoist & Derrick Co | Rotary dryer for aggregate |
| US3798338A (en) * | 1972-05-30 | 1974-03-19 | Pillsbury Co | Method for applying thermoplastic coatings to food and pharmceutical products |
| US3940120A (en) * | 1974-08-05 | 1976-02-24 | The Boeing Company | Dust free asphalt production method and apparatus |
| US3974307A (en) * | 1975-02-05 | 1976-08-10 | Bowen Michael E | Method for coating wood chips with resinous liquid |
-
1977
- 1977-10-04 DE DE19772744522 patent/DE2744522A1/en not_active Withdrawn
-
1978
- 1978-09-20 US US05/943,983 patent/US4188130A/en not_active Expired - Lifetime
- 1978-09-29 CA CA312,422A patent/CA1113800A/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| DE2744522A1 (en) | 1979-04-12 |
| US4188130A (en) | 1980-02-12 |
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