US3899559A - Method of manufacturing waferboard - Google Patents
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- US3899559A US3899559A US318840A US31884072A US3899559A US 3899559 A US3899559 A US 3899559A US 318840 A US318840 A US 318840A US 31884072 A US31884072 A US 31884072A US 3899559 A US3899559 A US 3899559A
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 13
- 235000012431 wafers Nutrition 0.000 claims abstract description 63
- 239000002023 wood Substances 0.000 claims abstract description 29
- 229920005989 resin Polymers 0.000 claims abstract description 16
- 239000011347 resin Substances 0.000 claims abstract description 16
- 238000005520 cutting process Methods 0.000 claims abstract description 12
- 238000001035 drying Methods 0.000 claims abstract description 5
- 238000002156 mixing Methods 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 5
- 238000012216 screening Methods 0.000 claims description 5
- 238000000151 deposition Methods 0.000 claims description 3
- 238000003825 pressing Methods 0.000 abstract description 7
- 239000011230 binding agent Substances 0.000 abstract description 4
- 238000003860 storage Methods 0.000 description 9
- 230000015556 catabolic process Effects 0.000 description 4
- 238000006731 degradation reaction Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 241000219000 Populus Species 0.000 description 2
- 206010041662 Splinter Diseases 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 210000000569 greater omentum Anatomy 0.000 description 2
- 239000002344 surface layer Substances 0.000 description 2
- 241000219495 Betulaceae Species 0.000 description 1
- 229920000877 Melamine resin Polymers 0.000 description 1
- 241000183024 Populus tremula Species 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000010960 cold rolled steel Substances 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- SLGWESQGEUXWJQ-UHFFFAOYSA-N formaldehyde;phenol Chemical compound O=C.OC1=CC=CC=C1 SLGWESQGEUXWJQ-UHFFFAOYSA-N 0.000 description 1
- 239000011121 hardwood Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 241000894007 species Species 0.000 description 1
Images
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
-
- 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
- B27N3/04—Manufacture of substantially flat articles, e.g. boards, from particles or fibres from fibres
Definitions
- Fritsch Attorney, Agent, or FirmFetherstonhaugh and Company ABS'I RACT A method of manufacturing waferboard comprising cutting thin wafers from wood logs, drying the wafers to lower the moisture content thereof, mixing the wafers with powdered binder resin and wax in molten or emulsified form to coat the wafers with wax and resin, forming mats of uniform density and thickness of the wafers, pressing the mats in a hot press at suitable temperature, pressure and time to form waferboards of predetermined thickness and density.
- waferboard has been manufactured in the past but it has been difficult to produce in an economical manner waferboards that remain dimensionally stable in all climates, and particularly damp climates.
- the present method involves specified steps which result in waferboards that can be used in exterior locations without undue raising of the wafers at the board surfaces or buckling due to excessive expansion in the plane of the panel when subjected to moisture.
- These waferboards can be used in interior locations, and are particularly suitable for use in areas where they are subjected to moisture, such as in laundry rooms and the like.
- Conventional particleboard or waferboard is made from fine wood particles or flakes and urea-aldehyde resins can be used only in interior locations. Prior to this invention, there had been little success in manufacturing these panels for use in exterior locations, and there is a growing demand for a particleboard or flakeboard with high physical strength properties and low linear expansion for use in exterior locations, such as for sheathing, fences or farm buildings.
- This invention relates to production processes incorporating certain variables for the manufacture of a particleboard and flakeboard to meet these conditions. A number of these variables are inter-related, and a change in one variable will affect the resultant product unless compensating changes are made in the other variables.
- the method according to the present invention of manufacturing waferboard and the like comprises cutting thin wafers from wood logs, screening the cut wafers to remove therefrom any fine wood particles, drying the wafers to reduce the moisture content thereof, mixing the wafers with fine powdered binder resin and wax in molten or emulsified form to coat each wafer with wax covered by powdered resin, forming a mat of wafers of uniform density and thickness on supporting plates, pressing the mat on the plates in a hot press for a suitable time and at a suitable temperature and pressure to form waferboards of predetermined thickness and density, and cooling the boards sufiiciently to enable them to be stored in hot stacks without thermal degradation.
- the logs from which the wafers are to be out are cut into suitable lengths such as, for example, two foot lengths.
- the bark is removed by a standard barker before the logs are cut into these lengths.
- the wood logs should be heated. Usually this heating is with hot water at about 100 to 150F. If the logs are frozen, it is preferable to heat them before barking and before they are cut into the desired lengths. If the logs are not thawed out in the winter time, the wafers tend to break up into splinters during the following wafer cutting operation. For best results, the moisture content of the logs should be about 40 to 70% based upon dry weight of the wood.
- the preheating of the logs in water is beneficial in the summer time since moisture is restored to the dried out surface layers of the logs. Without this restoration of moisture, there is a tendency to splinter the wafers during the cutting thereof.
- the logs are cut into wafers by standard cutters, such as disk or drum cutters.
- the cutting blades move downwardly through the wood at the side thereof.
- the cutter blades are substantially parallel with the grain of the wood and move downwardly through the latter.
- the wafers are cut so that the length thereof in the direction of the grain is approximately 40 to times their thickness, and the width which is perpendicular to the grain of the wafers should be in the range of about 5 to 60 times the thickness. It has been found that these wafers can be anywhere from 0.0 l O to 0.060 inch in thickness, and the best average is about 0.025 inch.
- the ideal length in the direction of grain is l to 2.5 inches, and width from about Va to about 1.5 inches.
- the cut wafers are screened to remove therefrom any fine wood particles.
- the screens can be from 2-mesh to 8-mesh, and preferably are about 4-mesh.
- the wafers are dried at surface temperatures not exceeding 240F, but the recommended temperature range is from about 200 to 240F. Temperatures higher than this tend to degrade the cellulose portion of the wood.
- the final moisture content of the wafers is important for the subsequent bonding and pressing operations. The moisture content depends on the thickness of the boards to be manufactured. In general, a moisture content range of about 2 to 10% produces satisfactory panels. However, the preferred moisture content is about 3% for inch panels, increasing to about 6% for A inch panels.
- molten or emulsified wax is applied to the wafers either before the powdered resin addition or immediately afterwards.
- Liquid resins can be used, in which case wax is required only to control the water absorption properties of the finished boards.
- the wax coats the wafers while the powdered resin adheres to the wax coating on the wafers.
- the amount of wax can be from about 1 to 6% by weight based on the dry wood, and the best results are attained with 2 to 4%, and the amount of resin is from about 1.5 to 4% by weight, and preferably 2%.
- the wafers are uniformly deposited on supporting plates over a wide area parallel to the direction of movement of the plates to maintain uniform density in mats formed by these wafers.
- the wafers can be applied at the rate of about 100 pounds per minute, but preferably no more than 50 pounds per minute to maintain a low angle of deposition.
- the wafers are felted into mats of uniform thickness and density on supporting or caul plates which are preferably made of cold rolled steel in order to minimize dimensional changes in the plates during the following pressing operation.
- the plates with the mats thereon are inserted into a standard hot press where they are subjected to heat and pressure for sufficient time to produce waferboards of desired thicknesses.
- the preferred temperature in the press is about 410F although panels can be made at temperatures of from about 390 to 430F.
- the pressure in the press ranges from about 300 to about 500 pounds per square inch, and is controlled to obtain the required density in the finished boards.
- the press time at these temperatures is about 45 seconds per l/ 16 of an inch of panel thickness. Boards can be made with a press time as low as 40 seconds, but these have lower physical strength than those made at the preferred times.
- Press time of over 55 seconds per 1/16 inch can result in thermal degradation of the panels and a very brittle product, with lowered impact strength and discoloration of the surface.
- the press time is controlled so that the press closes in 40 to 60 seconds and is held at a pressure less than 100 psi for the final minute of press time.
- the formed panels are cooled to about 270F and maintained at this temperature for about 3 to 12 hours.
- .Satisfactory panels have been produced with storage temperatures in the range of 210F to 300F. However, storage above this temperature results in lowered impact resistance in the panels and thermal degradation of the surface layers thereof. Temperatures below this will result'in the panels having reduced water absorption properties.
- the storage time is adjusted in accordance with the temperatures ,of the panels in storage. When the panels are held at 300F the storage time should be limited to under 2 hours. At a more normal storage temperature of about 270F, storage times of 3 to 12 hours are generally satisfactory. If the temperature is in the range of 230 to 250F, panels can be held in storage up to one week without affecting the physical properties thereof.
- the panels are trimmed to size for shipment immediately after the pressing operation or after the storage.
- FIG. 1 A production line for carrying out this invention is illustrated in the accompanying FIG. 1.
- logsof a desired length and having a moisture content of about 40 to 70% based on the dry weight of the wood are fed to a waferizer 10 which cuts wafers therefrom having a thickness of about 0.010 to about 0.060 inch, and a length 40 to 100 times this thickness in the direction of the grain thereof, and a'width of to 60 times the thickness across the grain.
- the wafers are passed through screening apparatus 12 to remove the fine particles of wood.
- the wafers are placed in a dryer 14 where the moisture content thereof is reduced to about 2 to based on the dry weight of the wood.
- the wafers are then directed into a blender 16 in which they are coated with wax in molten or emulsified form and covered with fine powdered bonding resin.
- the coated wafers are directed to a felter 18 in which they are felted into mats of uniform thickness and density on caul plates 19. These plates are directed into a standard hot press 22 where they are subjected to sufficient heat andpressure and for sufficient time to pro prise waferboards of desired thicknesses and having desired physical properties. These boards are then cooled in suitable cooling apparatus, after which they are stored in stacks 26 at temperatures from about 210 to 300F. These boards are cut into the desired dimensions after emerging from the hot press, or after they are taken out of the hot stack 26.
- a method of manufacturing waferboard which comprises cutting thin wafers from wood logs having a moisture content of about 40 to about based on dry weight of the wood, screening the cut wafers to remove therefrom any fine wood particles, drying the wafers at surface temperatures ranging from about 200 to about 240F to reduce the moisture content thereof to about 2 to about 10% based on the dry weight of the wood, mixing the wafers with about 1.5% to about 4% by weight fine powdered binder resin and from 1 to 6% by weight wax in molten or emulsified form to coat each wafer with a coat of wax covered by powdered resin, depositing the coated wafers uniformly on supporting plates to form thereon mats of wafers of uniform density and thickness, pressingthe mats of wafers on the plates in a hot press at temperatures ranging from about 390 to about 430F for a suitable time to form waferboards of predetermined thickness and density, and cooling said boards and storing the boards in hot stacks at temperatures from about 210 to about 300F to prevent thermal
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Wood Science & Technology (AREA)
- Forests & Forestry (AREA)
- Dry Formation Of Fiberboard And The Like (AREA)
- Chemical And Physical Treatments For Wood And The Like (AREA)
Abstract
A method of manufacturing waferboard comprising cutting thin wafers from wood logs, drying the wafers to lower the moisture content thereof, mixing the wafers with powdered binder resin and wax in molten or emulsified form to coat the wafers with wax and resin, forming mats of uniform density and thickness of the wafers, pressing the mats in a hot press at suitable temperature, pressure and time to form waferboards of predetermined thickness and density.
Description
United States Patent [191 Johnanson et al.
[451 Aug. 12, 1975 METHOD OF MANUFACTURING WAFERBOARD Inventors:
Assignee:
Filed:
Appl. No.:
Fred E. Johnanson, Vancouver; William L. Watkins, Hudson Bay, both of Canada MacMillan Bloedel Research Limited, Vancouver, Canada Dec. 27, 1972 Foreign Application Priority Data Nov. 24, 1972 Canada 157386 US. Cl. 264/115; 156/622; 156/624; 264/122 Int. Cl B29j 5/02 Field of Search 156/622, 62.4; 161/168,
References Cited UNITED STATES PATENTS Goss 264/ 1 15 2,776,688 1/1957 Clark 144/326 C 2,786,005 3/1957 Clark 144/326 C 2,854,372 9/1958 Yan et a1. 264/109 2,947,654 8/1960 Chapman 264/ 109 3,011,938 12/1961 Chapman... 156/622 3,021,244 2/ 1962 Meiler 264/115 3,243,327 3/1966 Hoppeler... 156/622 3,383,274 5/1968 Craig 156/628 Primary ExaminerDaniel J. Fritsch Attorney, Agent, or FirmFetherstonhaugh and Company ABS'I RACT A method of manufacturing waferboard comprising cutting thin wafers from wood logs, drying the wafers to lower the moisture content thereof, mixing the wafers with powdered binder resin and wax in molten or emulsified form to coat the wafers with wax and resin, forming mats of uniform density and thickness of the wafers, pressing the mats in a hot press at suitable temperature, pressure and time to form waferboards of predetermined thickness and density.
10 Claims, 1 Drawing Figure 1 METHOD OF MANUFACTURING WAFERBOARD This invention relates to methods of manufacturing waferboard from wood wafers.
waferboard has been manufactured in the past but it has been difficult to produce in an economical manner waferboards that remain dimensionally stable in all climates, and particularly damp climates. The present method involves specified steps which result in waferboards that can be used in exterior locations without undue raising of the wafers at the board surfaces or buckling due to excessive expansion in the plane of the panel when subjected to moisture. These waferboards can be used in interior locations, and are particularly suitable for use in areas where they are subjected to moisture, such as in laundry rooms and the like.
Conventional particleboard or waferboard is made from fine wood particles or flakes and urea-aldehyde resins can be used only in interior locations. Prior to this invention, there had been little success in manufacturing these panels for use in exterior locations, and there is a growing demand for a particleboard or flakeboard with high physical strength properties and low linear expansion for use in exterior locations, such as for sheathing, fences or farm buildings.
This invention relates to production processes incorporating certain variables for the manufacture of a particleboard and flakeboard to meet these conditions. A number of these variables are inter-related, and a change in one variable will affect the resultant product unless compensating changes are made in the other variables.
Many factors are of importance in the control of board properties. Any kind of wood can be used, but for economical purposes, low-density hardwoods, such as poplars, cottonwood or alder, are preferred. In particular, aspen poplar is a desirable species for this purpose.
The method according to the present invention of manufacturing waferboard and the like comprises cutting thin wafers from wood logs, screening the cut wafers to remove therefrom any fine wood particles, drying the wafers to reduce the moisture content thereof, mixing the wafers with fine powdered binder resin and wax in molten or emulsified form to coat each wafer with wax covered by powdered resin, forming a mat of wafers of uniform density and thickness on supporting plates, pressing the mat on the plates in a hot press for a suitable time and at a suitable temperature and pressure to form waferboards of predetermined thickness and density, and cooling the boards sufiiciently to enable them to be stored in hot stacks without thermal degradation.
The logs from which the wafers are to be out are cut into suitable lengths such as, for example, two foot lengths. The bark is removed by a standard barker before the logs are cut into these lengths. To produce the optimum wafers with smooth surfaces and with a minimum of fines, the wood logs should be heated. Usually this heating is with hot water at about 100 to 150F. If the logs are frozen, it is preferable to heat them before barking and before they are cut into the desired lengths. If the logs are not thawed out in the winter time, the wafers tend to break up into splinters during the following wafer cutting operation. For best results, the moisture content of the logs should be about 40 to 70% based upon dry weight of the wood. The preheating of the logs in water is beneficial in the summer time since moisture is restored to the dried out surface layers of the logs. Without this restoration of moisture, there is a tendency to splinter the wafers during the cutting thereof.
The logs are cut into wafers by standard cutters, such as disk or drum cutters. The cutting blades move downwardly through the wood at the side thereof. In other words, the cutter blades are substantially parallel with the grain of the wood and move downwardly through the latter. In order to obtain the maximum physical properties, the wafers are cut so that the length thereof in the direction of the grain is approximately 40 to times their thickness, and the width which is perpendicular to the grain of the wafers should be in the range of about 5 to 60 times the thickness. It has been found that these wafers can be anywhere from 0.0 l O to 0.060 inch in thickness, and the best average is about 0.025 inch. The ideal length in the direction of grain is l to 2.5 inches, and width from about Va to about 1.5 inches.
The cut wafers are screened to remove therefrom any fine wood particles. The screens can be from 2-mesh to 8-mesh, and preferably are about 4-mesh.
Following the screening operation, the wafers are dried at surface temperatures not exceeding 240F, but the recommended temperature range is from about 200 to 240F. Temperatures higher than this tend to degrade the cellulose portion of the wood. The final moisture content of the wafers is important for the subsequent bonding and pressing operations. The moisture content depends on the thickness of the boards to be manufactured. In general, a moisture content range of about 2 to 10% produces satisfactory panels. However, the preferred moisture content is about 3% for inch panels, increasing to about 6% for A inch panels.
The use of powdered phenol formaldehyde or melamine formaldehyde resin is preferred for exterior panels, while urea fonnaldehyde can be used for interior panels. To hold the powdered resin on the wafers, molten or emulsified wax is applied to the wafers either before the powdered resin addition or immediately afterwards. Liquid resins can be used, in which case wax is required only to control the water absorption properties of the finished boards. The wax coats the wafers while the powdered resin adheres to the wax coating on the wafers. The amount of wax can be from about 1 to 6% by weight based on the dry wood, and the best results are attained with 2 to 4%, and the amount of resin is from about 1.5 to 4% by weight, and preferably 2%.
The wafers are uniformly deposited on supporting plates over a wide area parallel to the direction of movement of the plates to maintain uniform density in mats formed by these wafers. The wafers can be applied at the rate of about 100 pounds per minute, but preferably no more than 50 pounds per minute to maintain a low angle of deposition.
The wafers are felted into mats of uniform thickness and density on supporting or caul plates which are preferably made of cold rolled steel in order to minimize dimensional changes in the plates during the following pressing operation.
The plates with the mats thereon are inserted into a standard hot press where they are subjected to heat and pressure for sufficient time to produce waferboards of desired thicknesses. The preferred temperature in the press is about 410F although panels can be made at temperatures of from about 390 to 430F. The pressure in the press ranges from about 300 to about 500 pounds per square inch, and is controlled to obtain the required density in the finished boards. The press time at these temperatures is about 45 seconds per l/ 16 of an inch of panel thickness. Boards can be made with a press time as low as 40 seconds, but these have lower physical strength than those made at the preferred times. Press time of over 55 seconds per 1/16 inch can result in thermal degradation of the panels and a very brittle product, with lowered impact strength and discoloration of the surface. The press time is controlled so that the press closes in 40 to 60 seconds and is held at a pressure less than 100 psi for the final minute of press time.
Following the pressing operation, the formed panels are cooled to about 270F and maintained at this temperature for about 3 to 12 hours. .Satisfactory panels have been produced with storage temperatures in the range of 210F to 300F. However, storage above this temperature results in lowered impact resistance in the panels and thermal degradation of the surface layers thereof. Temperatures below this will result'in the panels having reduced water absorption properties. The storage time is adjusted in accordance with the temperatures ,of the panels in storage. When the panels are held at 300F the storage time should be limited to under 2 hours. At a more normal storage temperature of about 270F, storage times of 3 to 12 hours are generally satisfactory. If the temperature is in the range of 230 to 250F, panels can be held in storage up to one week without affecting the physical properties thereof.
The panels are trimmed to size for shipment immediately after the pressing operation or after the storage.
A production line for carrying out this invention is illustrated in the accompanying FIG. 1.
Referring to the drawing, logsof a desired length and having a moisture content of about 40 to 70% based on the dry weight of the wood are fed to a waferizer 10 which cuts wafers therefrom having a thickness of about 0.010 to about 0.060 inch, and a length 40 to 100 times this thickness in the direction of the grain thereof, and a'width of to 60 times the thickness across the grain. The wafers are passed through screening apparatus 12 to remove the fine particles of wood.
- From here the wafers are placed in a dryer 14 where the moisture content thereof is reduced to about 2 to based on the dry weight of the wood. The wafers are then directed into a blender 16 in which they are coated with wax in molten or emulsified form and covered with fine powdered bonding resin.
The coated wafers are directed to a felter 18 in which they are felted into mats of uniform thickness and density on caul plates 19. These plates are directed into a standard hot press 22 where they are subjected to sufficient heat andpressure and for sufficient time to pro duce waferboards of desired thicknesses and having desired physical properties. These boards are then cooled in suitable cooling apparatus, after which they are stored in stacks 26 at temperatures from about 210 to 300F. These boards are cut into the desired dimensions after emerging from the hot press, or after they are taken out of the hot stack 26.
We claim:
1. A method of manufacturing waferboard, which comprises cutting thin wafers from wood logs having a moisture content of about 40 to about based on dry weight of the wood, screening the cut wafers to remove therefrom any fine wood particles, drying the wafers at surface temperatures ranging from about 200 to about 240F to reduce the moisture content thereof to about 2 to about 10% based on the dry weight of the wood, mixing the wafers with about 1.5% to about 4% by weight fine powdered binder resin and from 1 to 6% by weight wax in molten or emulsified form to coat each wafer with a coat of wax covered by powdered resin, depositing the coated wafers uniformly on supporting plates to form thereon mats of wafers of uniform density and thickness, pressingthe mats of wafers on the plates in a hot press at temperatures ranging from about 390 to about 430F for a suitable time to form waferboards of predetermined thickness and density, and cooling said boards and storing the boards in hot stacks at temperatures from about 210 to about 300F to prevent thermal degradation. 1 '2. The method as claimed in claim 1 in which the wood wafers are from about 0.010 to 0.060 inch thick, about 40 to times said thickness in length in direction of the wood grains, to about 5 to 60 times said thickness in width across the grain.
3. The method as claimed in claim 2 in which the time in the press is from about 40 to 55 seconds for each sixteenth inch in waferboard thickness.
4. The method as claimed in claim 2 in which the waferboards from the press are cooled to about 270F, and are stored at temperatures from about 210 to 250F.
5. The method as claimed in claim 2 in which the time in the press is from about 40 to 55 seconds for each sixteenth inch in waferboard thickness, and the waferboards from the press are cooled to about 270F, and are stored at temperatures from about 210 to 250F.
6. The method as claimed in claim 2 in which the logs, prior to the cutting of the wafers, are heated in water at a temperature of from about 100 to F.
7. The method as claimed in claim 1 in which the time in the press is from about 40 to 55 seconds for each sixteenth inch in waferboard thickness.
8. The method as claimed in claim 1 in which the waferboards from the press are cooled to about 270F, and are stored at temperatures from about 2l0 to 250F.
9. The method as claimed in claim 1 in which the time in the press is from about 40 to 55 seconds for each sixteenth inch in waferboard thickness, and the waferboards from the press are cooled to about 270F,
and are stored at temperatures from about 210 to 10. The method as claimed in claim 1 in which the logs, prior to the cutting of the wafers, are heated in water at a temperature of from about 100 to 150F.
Claims (10)
1. A METHOD OF MANUFACTURING WAFERBOARD, WHICH COMPRISES CUTTING THIN WAFERS FROM WOOD LOGS HAVING A MOISTURE CONTENT OF ABOUT 40 TO ABOUT 70% BASED ON DRY WEIGHT OF THE WOOD, SCREENING THE CUT WAFERS TO REMOVE THEREFROM ANY FINE WOOD PARTICLES, DRYING THE WAFERS AT SURFACE TEMPERATURES RANGING FROM ABOUT 200* TO ABOUT 240*F TO REDUCE THE MOISTURE CONTENT THEREOF TO ABOUT 2 TO ABOUT 10% BASED ON THE DRY WEIGHT OF THE WOOD, MIXING THE WAFERS WITH ABOUT 1.5% TO ABOUT 4% BY WEIGHT FINE POWDERED BINDER RESIN AND FROM 1 TO 6% BY WEIGHT WAX IN MOLTEN OR EMULSIFIED FORM TO COAT EACH WAFER WITH A COAT OF WAX COVERED BY POWDERED RESIN, DEPOSITING THE COATED WAFERS UNIFORMLY ON SUPPORTING PLATES TO FORM
2. The method as claimed in claim 1 in which the wood wafers are from about 0.010 to 0.060 inch thick, about 40 to 100 times said thickness in length in direction of the wood grains, to about 5 to 60 times said thickness in width across the grain.
3. The method as claimed in claim 2 in which the time in the press is from about 40 to 55 seconds for each sixteenth inch in waferboard thickness.
4. The method as claimed in claim 2 in which the waferboards from the press are cooled to about 270*F, and are stored at temperatures from about 210* to 250*F.
5. The method as claimed in claim 2 in which the time in the press is from about 40 to 55 seconds for each sixteenth inch in waferboard thickness, and the waferboards from the press are cooled to about 270*F, and are stored at temperatures from about 210* to 250*F.
6. The method as claimed in claim 2 in which the logs, prior to the cutting of the wafers, are heated in water at a temperature of from about 100* to 150*F.
7. The method as claimed in claim 1 in which the time in the press is from about 40 to 55 seconds for each sixteenth inch in waferboard thickness.
8. The method as claimed in claim 1 in which the waferboards from the press are cooled to about 270*F, and are stored at temperatures from about 210* to 250*F.
9. The method as claimed in claim 1 in which the time in the press is from about 40 to 55 seconds for each sixteenth inch in waferboard thickness, and the waferboards from the press are cooled to about 270*F, and are stored at temperatures from about 210* to 250*F.
10. The method as claimed in claim 1 in which the logs, prior to the cutting of the wafers, are heated in water at a temperature of from about 100* to 150*F.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CA157386 | 1972-11-24 |
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US3899559A true US3899559A (en) | 1975-08-12 |
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US318840A Expired - Lifetime US3899559A (en) | 1972-11-24 | 1972-12-27 | Method of manufacturing waferboard |
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Cited By (29)
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FR2526366A1 (en) * | 1982-05-06 | 1983-11-10 | Casco Ab | PROCESS FOR MANUFACTURING AGGLOMERATED PANELS |
US4643860A (en) * | 1985-03-05 | 1987-02-17 | Macmillan Bloedel Limited | Preservative treated composite wood product |
WO1992012836A1 (en) * | 1991-01-23 | 1992-08-06 | Aci Australia Limited | Building substrate and method of manufacturing same |
US5406768A (en) * | 1992-09-01 | 1995-04-18 | Andersen Corporation | Advanced polymer and wood fiber composite structural component |
US5441801A (en) * | 1993-02-12 | 1995-08-15 | Andersen Corporation | Advanced polymer/wood composite pellet process |
US5486553A (en) * | 1992-08-31 | 1996-01-23 | Andersen Corporation | Advanced polymer/wood composite structural member |
US5827607A (en) * | 1992-08-31 | 1998-10-27 | Andersen Corporation | Advanced polymer wood composite |
US5847016A (en) * | 1996-05-16 | 1998-12-08 | Marley Mouldings Inc. | Polymer and wood flour composite extrusion |
US5948524A (en) * | 1996-01-08 | 1999-09-07 | Andersen Corporation | Advanced engineering resin and wood fiber composite |
US6004668A (en) * | 1992-08-31 | 1999-12-21 | Andersen Corporation | Advanced polymer wood composite |
US6180257B1 (en) | 1996-10-29 | 2001-01-30 | Crane Plastics Company Limited Partnership | Compression molding of synthetic wood material |
US6280667B1 (en) | 1999-04-19 | 2001-08-28 | Andersen Corporation | Process for making thermoplastic-biofiber composite materials and articles including a poly(vinylchloride) component |
US6344268B1 (en) | 1998-04-03 | 2002-02-05 | Certainteed Corporation | Foamed polymer-fiber composite |
US6632863B2 (en) | 2001-10-25 | 2003-10-14 | Crane Plastics Company Llc | Cellulose/polyolefin composite pellet |
US6637213B2 (en) | 2001-01-19 | 2003-10-28 | Crane Plastics Company Llc | Cooling of extruded and compression molded materials |
US6662515B2 (en) | 2000-03-31 | 2003-12-16 | Crane Plastics Company Llc | Synthetic wood post cap |
US6685858B2 (en) | 1997-09-05 | 2004-02-03 | Crane Plastics Company Llc | In-line compounding and extrusion system |
US6708504B2 (en) | 2001-01-19 | 2004-03-23 | Crane Plastics Company Llc | Cooling of extruded and compression molded materials |
US6780359B1 (en) | 2002-01-29 | 2004-08-24 | Crane Plastics Company Llc | Synthetic wood composite material and method for molding |
US6958185B1 (en) | 2000-07-31 | 2005-10-25 | Crane Plastics Company Llc | Multilayer synthetic wood component |
US6971211B1 (en) | 1999-05-22 | 2005-12-06 | Crane Plastics Company Llc | Cellulosic/polymer composite material |
US6984676B1 (en) | 1996-10-22 | 2006-01-10 | Crane Plastics Company Llc | Extrusion of synthetic wood material |
US7017352B2 (en) | 2001-01-19 | 2006-03-28 | Crane Plastics Company Llc | Cooling of extruded and compression molded materials |
US7186457B1 (en) | 2002-11-27 | 2007-03-06 | Crane Plastics Company Llc | Cellulosic composite component |
US7743567B1 (en) | 2006-01-20 | 2010-06-29 | The Crane Group Companies Limited | Fiberglass/cellulosic composite and method for molding |
US20110294925A1 (en) * | 2009-11-23 | 2011-12-01 | Shaler Stephen M | Composite from hemicellulose extracted wood with improved performance and reduced emissions |
US8074339B1 (en) | 2004-11-22 | 2011-12-13 | The Crane Group Companies Limited | Methods of manufacturing a lattice having a distressed appearance |
US8167275B1 (en) | 2005-11-30 | 2012-05-01 | The Crane Group Companies Limited | Rail system and method for assembly |
US8460797B1 (en) | 2006-12-29 | 2013-06-11 | Timbertech Limited | Capped component and method for forming |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2581652A (en) * | 1948-01-19 | 1952-01-08 | Us Sheetwood Company | Method of manufacturing sheet wood |
US2776688A (en) * | 1953-03-23 | 1957-01-08 | Changewood Corp | Crosscut fiber and method for its preparation |
US2786005A (en) * | 1954-07-26 | 1957-03-19 | Changewood Corp | Crosscut woody wafers and structures embodying same |
US2854372A (en) * | 1953-09-03 | 1958-09-30 | Abitibi Power & Paper Co | Process for forming wood particle board and product |
US2947654A (en) * | 1956-03-26 | 1960-08-02 | Wood Processes Oregon Ltd | Method of manufacturing a composite board product |
US3011938A (en) * | 1957-11-18 | 1961-12-05 | Wood Processes Oregon Ltd | Process of making board products |
US3021244A (en) * | 1955-12-23 | 1962-02-13 | John G Meiler | Process for producing high density hardboard |
US3243327A (en) * | 1961-05-16 | 1966-03-29 | Hoppeler Walter | Method of making a pressed plate |
US3383274A (en) * | 1965-01-06 | 1968-05-14 | Us Plywood Champ Papers Inc | Flameproofing of construction material |
-
1972
- 1972-12-27 US US318840A patent/US3899559A/en not_active Expired - Lifetime
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2581652A (en) * | 1948-01-19 | 1952-01-08 | Us Sheetwood Company | Method of manufacturing sheet wood |
US2776688A (en) * | 1953-03-23 | 1957-01-08 | Changewood Corp | Crosscut fiber and method for its preparation |
US2854372A (en) * | 1953-09-03 | 1958-09-30 | Abitibi Power & Paper Co | Process for forming wood particle board and product |
US2786005A (en) * | 1954-07-26 | 1957-03-19 | Changewood Corp | Crosscut woody wafers and structures embodying same |
US3021244A (en) * | 1955-12-23 | 1962-02-13 | John G Meiler | Process for producing high density hardboard |
US2947654A (en) * | 1956-03-26 | 1960-08-02 | Wood Processes Oregon Ltd | Method of manufacturing a composite board product |
US3011938A (en) * | 1957-11-18 | 1961-12-05 | Wood Processes Oregon Ltd | Process of making board products |
US3243327A (en) * | 1961-05-16 | 1966-03-29 | Hoppeler Walter | Method of making a pressed plate |
US3383274A (en) * | 1965-01-06 | 1968-05-14 | Us Plywood Champ Papers Inc | Flameproofing of construction material |
Cited By (48)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2526366A1 (en) * | 1982-05-06 | 1983-11-10 | Casco Ab | PROCESS FOR MANUFACTURING AGGLOMERATED PANELS |
GB2119702A (en) * | 1982-05-06 | 1983-11-23 | Casco Ab | Method for the production of particle boards |
US4643860A (en) * | 1985-03-05 | 1987-02-17 | Macmillan Bloedel Limited | Preservative treated composite wood product |
WO1992012836A1 (en) * | 1991-01-23 | 1992-08-06 | Aci Australia Limited | Building substrate and method of manufacturing same |
US6004668A (en) * | 1992-08-31 | 1999-12-21 | Andersen Corporation | Advanced polymer wood composite |
US6015611A (en) * | 1992-08-31 | 2000-01-18 | Andersen Corporation | Advanced polymer wood composite |
US5486553A (en) * | 1992-08-31 | 1996-01-23 | Andersen Corporation | Advanced polymer/wood composite structural member |
US6015612A (en) * | 1992-08-31 | 2000-01-18 | Andersen Corporation | Polymer wood composite |
US5932334A (en) * | 1992-08-31 | 1999-08-03 | Andersen Corporation | Advanced polymer wood composite |
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US5827607A (en) * | 1992-08-31 | 1998-10-27 | Andersen Corporation | Advanced polymer wood composite |
US5406768A (en) * | 1992-09-01 | 1995-04-18 | Andersen Corporation | Advanced polymer and wood fiber composite structural component |
US5497594A (en) * | 1992-09-01 | 1996-03-12 | Andersen Corporation | Advanced polymer and wood fiber composite structural component |
US5441801A (en) * | 1993-02-12 | 1995-08-15 | Andersen Corporation | Advanced polymer/wood composite pellet process |
US5518677A (en) * | 1993-02-12 | 1996-05-21 | Andersen Corporation | Advanced polymer/wood composite pellet process |
US5695874A (en) * | 1993-02-12 | 1997-12-09 | Andersen Corporation | Advanced polymer/wood composite pellet process |
US5948524A (en) * | 1996-01-08 | 1999-09-07 | Andersen Corporation | Advanced engineering resin and wood fiber composite |
US5951927A (en) * | 1996-05-16 | 1999-09-14 | Marley Mouldings Inc. | Method of making a polymer and wood flour composite extrusion |
US6066680A (en) * | 1996-05-16 | 2000-05-23 | Marley Mouldings Inc. | Extrudable composite of polymer and wood flour |
US5847016A (en) * | 1996-05-16 | 1998-12-08 | Marley Mouldings Inc. | Polymer and wood flour composite extrusion |
US6984676B1 (en) | 1996-10-22 | 2006-01-10 | Crane Plastics Company Llc | Extrusion of synthetic wood material |
US6180257B1 (en) | 1996-10-29 | 2001-01-30 | Crane Plastics Company Limited Partnership | Compression molding of synthetic wood material |
US6511757B1 (en) | 1996-10-29 | 2003-01-28 | Crane Plastics Company Llc | Compression molding of synthetic wood material |
US6685858B2 (en) | 1997-09-05 | 2004-02-03 | Crane Plastics Company Llc | In-line compounding and extrusion system |
US6344268B1 (en) | 1998-04-03 | 2002-02-05 | Certainteed Corporation | Foamed polymer-fiber composite |
US6280667B1 (en) | 1999-04-19 | 2001-08-28 | Andersen Corporation | Process for making thermoplastic-biofiber composite materials and articles including a poly(vinylchloride) component |
US6971211B1 (en) | 1999-05-22 | 2005-12-06 | Crane Plastics Company Llc | Cellulosic/polymer composite material |
US6662515B2 (en) | 2000-03-31 | 2003-12-16 | Crane Plastics Company Llc | Synthetic wood post cap |
US6958185B1 (en) | 2000-07-31 | 2005-10-25 | Crane Plastics Company Llc | Multilayer synthetic wood component |
US6637213B2 (en) | 2001-01-19 | 2003-10-28 | Crane Plastics Company Llc | Cooling of extruded and compression molded materials |
US6708504B2 (en) | 2001-01-19 | 2004-03-23 | Crane Plastics Company Llc | Cooling of extruded and compression molded materials |
US7017352B2 (en) | 2001-01-19 | 2006-03-28 | Crane Plastics Company Llc | Cooling of extruded and compression molded materials |
US6632863B2 (en) | 2001-10-25 | 2003-10-14 | Crane Plastics Company Llc | Cellulose/polyolefin composite pellet |
US6780359B1 (en) | 2002-01-29 | 2004-08-24 | Crane Plastics Company Llc | Synthetic wood composite material and method for molding |
US7186457B1 (en) | 2002-11-27 | 2007-03-06 | Crane Plastics Company Llc | Cellulosic composite component |
US8074339B1 (en) | 2004-11-22 | 2011-12-13 | The Crane Group Companies Limited | Methods of manufacturing a lattice having a distressed appearance |
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US8167275B1 (en) | 2005-11-30 | 2012-05-01 | The Crane Group Companies Limited | Rail system and method for assembly |
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USD788329S1 (en) | 2005-11-30 | 2017-05-30 | Cpg International Llc | Post cover |
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US7743567B1 (en) | 2006-01-20 | 2010-06-29 | The Crane Group Companies Limited | Fiberglass/cellulosic composite and method for molding |
US8460797B1 (en) | 2006-12-29 | 2013-06-11 | Timbertech Limited | Capped component and method for forming |
US20110294925A1 (en) * | 2009-11-23 | 2011-12-01 | Shaler Stephen M | Composite from hemicellulose extracted wood with improved performance and reduced emissions |
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