US2161655A - Method of making hard, dense, fibrous, boardlike products - Google Patents
Method of making hard, dense, fibrous, boardlike products Download PDFInfo
- Publication number
- US2161655A US2161655A US108372A US10837236A US2161655A US 2161655 A US2161655 A US 2161655A US 108372 A US108372 A US 108372A US 10837236 A US10837236 A US 10837236A US 2161655 A US2161655 A US 2161655A
- Authority
- US
- United States
- Prior art keywords
- board
- freeness
- dense
- pulp
- boardlike
- 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 - Lifetime
Links
- 238000004519 manufacturing process Methods 0.000 title description 2
- 238000000034 method Methods 0.000 description 13
- 239000002023 wood Substances 0.000 description 11
- 239000000835 fiber Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 229920001131 Pulp (paper) Polymers 0.000 description 5
- 239000005418 vegetable material Substances 0.000 description 5
- 239000007900 aqueous suspension Substances 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 238000000227 grinding Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000007731 hot pressing Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000005018 casein Substances 0.000 description 2
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 2
- 235000021240 caseins Nutrition 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000010924 continuous production Methods 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 229920002522 Wood fibre Polymers 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009950 felting Methods 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000013007 heat curing Methods 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000004078 waterproofing Methods 0.000 description 1
- 239000002025 wood fiber Substances 0.000 description 1
Images
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21J—FIBREBOARD; MANUFACTURE OF ARTICLES FROM CELLULOSIC FIBROUS SUSPENSIONS OR FROM PAPIER-MACHE
- D21J1/00—Fibreboard
Definitions
- This invention relates generally to an apparatus for and the process of making dense, hard, board-like products from wood or woody materials.
- Another object of the invention is the making of board or sheets from vegetable fibers adapted for use in construction of buildings and various other purposes.
- a further object of the invention is to provide an improved process of forming composition boards or sheets from fibrous pulp stock, which comprises forming a sheet, applying heat and pressure to compact and'unite the sheet into a homogeneous body.
- the vegetable material is first comminuted or reduced to pulp by any suitable means.
- any vegetable material which can be reduced to pulp may be used but economically it is .preferred that waste material be used.
- Figure 1 is a view diagrammatically illustrating an apparatus for carrying out the process.
- Figure 2 is a sectional view of a heat controlling damper.
- the apparatus shown comprises a suitable sheet forming machine A, a wet press, B, a hot pressing apparatus, C, a cut-01T means, D, a tipple conveyor E, and heat chamber F.
- the felting or sheet forming apparatus consists of a suitable stock tank I0.
- the pulp is deposited upon the cylinders Ii and I2, and fed upwardly thereby forming a web or sheet.
- the sheet so formed passes to wet press to remove the surplus water.
- This press consists of rolls I3 and I 5 and rotatable belts Il and I6, mounted upon rolls i3 and rolls l5, respectively.
- the sheet after having the surplus water removed, is passed to the hot pressing apparatus.
- the hot pressing apparatus 'I'he hot pressing is enclosed in a suitable housing and consists of large rolls, I1, which carry belts I9.
- the rolls Il and the belts are causedv to rotate by any suitable means (not shown) and a series of upper and lower rolls I8.
- Heat is supplied to the press by any desired means but it is preferred that a furnace 23, discharges hot gas through conduit 24, and branch 25, into the receiving end of the press housing.
- the gas is withdrawn from the housing at or near the discharge end by conduit, 26, and its branches, and returned by the aid of a fan, 2l, to the furnace.
- dampers 20 In the press housing are located dampers 20, which may be opened or closed by a suitable means located outside of the housing. For example, this may be accomplished by means of handle 2
- a spring 22, may be used for holding the dampers 20, in the adjusted position.
- the dampers 20, control the amount of gases discharged to any given part of the press and also create a turbulence of the air adjacent to the rolls i8, so that stratification of the gas is prevented.
- the sheet after being pressed to the desired thickness is discharged from the housing and is divided into the desireddimensions by cut-olf saw, D. 'Ihe sections may then be discharged or subjected to further treatment.
- the sections may be carried by endless conveyor belts, 2B, mounted upon rolls 29, to a heat treating chamber F. In this chamber is located spaced apart and superimposed conveyor, 33. Heat is supplied to the chamber by means of coils 34.
- the sections of the board are delivered to the conveyors 33, by means of a tipple conveyor E, which consists of fixed roll, 30, movable roll, 3
- a tipple conveyor E which consists of fixed roll, 30, movable roll, 3
- the low freeness stock is preferably commingled with the high freeness stock while in a water bath. O1 course the stocks may be commingled at any time prior to formation of the boardlike body.
- the low freeness stock acts as a binder for the product made.
- the board or sheet is formed and the surplus water removed, the extent to which the sheet is dried is not important but from an economical standpoint it is preferred the board contain 40% to 60% of water at -the time it is subjected to simultaneous heat and pressure.
- the temperature in the press must be above 212.
- the temperature is preferably approximately 700 F. at the receiving end and approximately 430 F. on the discharge end.
- the pressure to which the product is subjected may vary from 25# to 75# per lineal inch of 'roll in contact with the product being pressed.
- the product may be completely free from moisture in the press or in a continuous process, the product may be discharged having a predetermined moisture content.
- a belt having a highly polished surface is placed against the surface it is desired to have smooth.
- I'I'he board-like body after being discharged from the pressing apparatus is divided into sections of the desired size. I'he sections may be submitted to a heat curing operation at a temperature of approximately 250 F.
- a synthetic petroleum resin or a'synthetic wood resin which hardens under heat and pressure within the range of from 2% to 15% may be used to obtain higher water-proofing and greater tensile strength.
- the board-like body may be made continuously or intermittently in a suitable hydraulic press.
- a product for instance a board-like body made from stock having the major portion of relatively high freeness and the remainder of relatively low freeness, results in a complete bonding of the fibers under heat and pressure into a homogeneous and water-resisting product.
- the process of making a hard and highly water-resisting board-like body which comprises forming a board-like body from a mixture of 5% to 20% of raw and unbeaten ground wood fibrous material having a freene'ss of from 40 to 80 and 80% to 95% of raw and unbeaten wood fibrous stock having a freeness Within the range of 500 to 700, commingling with the fibers while in a water suspension 1% to 3% of casein, and simultaneously applying heat and pressure to consolidate and, dry the board.
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- Paper (AREA)
Description
BOARDLIKE PRODUCTS .lune 6, 1939. G. H. ELLIS METHOD OF MAKING HARD, DENSE, FIBHOUS,
Filed oct. so, 195e INVENTOR Y 650mb- H. ELL/s BLQLW ATTORNEY Patented June 6, 1939 PATENT OFFICE METHOD F MAKING HARD, DENSE, FI-
" BROUS, BOARDLIKE PRODUCTS George H. Ellis, New Brighton, Minn., assignor to The Insulite Company, Minneapolis, Minn., a corporation of Minnesota Application october so, 193s, serial No. 108,372 7 claims. (ci. :az-21) This invention relates generally to an apparatus for and the process of making dense, hard, board-like products from wood or woody materials.
Another object of the invention is the making of board or sheets from vegetable fibers adapted for use in construction of buildings and various other purposes.
A further object of the invention is to provide an improved process of forming composition boards or sheets from fibrous pulp stock, which comprises forming a sheet, applying heat and pressure to compact and'unite the sheet into a homogeneous body.
In practice the vegetable material is first comminuted or reduced to pulp by any suitable means. Of courseany vegetable material which can be reduced to pulp may be used but economically it is .preferred that waste material be used.
With the foregoing and other objects in view A the invention consists of the novel construction,
combination and arrangement of parts hereinafter more specifically described and illustrated in the accompanying drawing wherein is shown embodiments of the invention and also in the novel steps of the process hereinafter to be more fully described but it is to be understood that changes, variations and modifications may be resorted to which fall within the scope of claims hereunto appended.
In the accompanying drawing which illustrates an embodiment of the invention and forms a part of the specification:
Figure 1 is a view diagrammatically illustrating an apparatus for carrying out the process.
Figure 2 is a sectional view of a heat controlling damper.
In the embodiment of the invention here shown there is illustrated an apparatus for carrying out the process of making board-like bodies. The apparatus shown comprises a suitable sheet forming machine A, a wet press, B, a hot pressing apparatus, C, a cut-01T means, D, a tipple conveyor E, and heat chamber F.
The felting or sheet forming apparatusconsists of a suitable stock tank I0. The pulp is deposited upon the cylinders Ii and I2, and fed upwardly thereby forming a web or sheet. The sheet so formed passes to wet press to remove the surplus water. This press consists of rolls I3 and I 5 and rotatable belts Il and I6, mounted upon rolls i3 and rolls l5, respectively.
The sheet after having the surplus water removed, is passed to the hot pressing apparatus. 'I'he hot pressing is enclosed in a suitable housing and consists of large rolls, I1, which carry belts I9. The rolls Il and the belts are causedv to rotate by any suitable means (not shown) and a series of upper and lower rolls I8.
Heat is supplied to the press by any desired means but it is preferred that a furnace 23, discharges hot gas through conduit 24, and branch 25, into the receiving end of the press housing. The gas is withdrawn from the housing at or near the discharge end by conduit, 26, and its branches, and returned by the aid of a fan, 2l, to the furnace.
In the press housing are located dampers 20, which may be opened or closed by a suitable means located outside of the housing. For example, this may be accomplished by means of handle 2|, secured upon a damper rod. A spring 22, may be used for holding the dampers 20, in the adjusted position. The dampers 20, control the amount of gases discharged to any given part of the press and also create a turbulence of the air adjacent to the rolls i8, so that stratification of the gas is prevented.
The sheet after being pressed to the desired thickness is discharged from the housing and is divided into the desireddimensions by cut-olf saw, D. 'Ihe sections may then be discharged or subjected to further treatment. The sections may be carried by endless conveyor belts, 2B, mounted upon rolls 29, to a heat treating chamber F. In this chamber is located spaced apart and superimposed conveyor, 33. Heat is supplied to the chamber by means of coils 34.
The sections of the board are delivered to the conveyors 33, by means of a tipple conveyor E, which consists of fixed roll, 30, movable roll, 3|, and endless belt 32, rotatably mountedupon rolls and 3l.
To produce a relatively inexpensive, hard, dense, board-like product, having a specific gravity of approximately 1, there is used 80% to 95% of rather coarse, pulped vegetable material, such as ground wood, having a freeness measured by the Canadian standard tester of from 500 to 700, preferably approximately 600. There is commingled with this pulp, 5% to 20% of vegetable material, derived from thel same source as the pulp but having a freeness of from 40 to 80 measured by the same tester, preferably a freeness of approximately 60. The vegetable material ranging from 5% to 20% is usually in the form of pulp (for example ground Wood pulp in its natural state) and if the freeness is to be around 40 the material is treated in a pebble mill or the like to obtain this freeness.
soy
'Ihe low freeness stock ispreferably commingled with the high freeness stock while in a water bath. O1 course the stocks may be commingled at any time prior to formation of the boardlike body. The low freeness stock acts as a binder for the product made.
The board or sheet is formed and the surplus water removed, the extent to which the sheet is dried is not important but from an economical standpoint it is preferred the board contain 40% to 60% of water at -the time it is subjected to simultaneous heat and pressure.
'I'he temperature in the press must be above 212. In a. continuous process the temperature is preferably approximately 700 F. at the receiving end and approximately 430 F. on the discharge end.
The pressure to which the product is subjected may vary from 25# to 75# per lineal inch of 'roll in contact with the product being pressed.
Pressures above this may be used if found desirable.
'I'he product may be completely free from moisture in the press or in a continuous process, the product may be discharged having a predetermined moisture content.
If it is desired that the body have one smooth surface, a belt having a highly polished surface is placed against the surface it is desired to have smooth.
'I'he board-like body after being discharged from the pressing apparatus is divided into sections of the desired size. I'he sections may be submitted to a heat curing operation at a temperature of approximately 250 F.
If it is desired to give the board additional resistance to water absorption and higher stiffness and tensile strength, a material or materials are commingled with the stock prior to forming the product.
If casein within the range of 1% to 3% based upon the dry weight of the pulp is added, this results in a high gloss finish and a high tensile strength.
A synthetic petroleum resin or a'synthetic wood resin which hardens under heat and pressure within the range of from 2% to 15% may be used to obtain higher water-proofing and greater tensile strength.
It is to be understood that the board-like body may be made continuously or intermittently in a suitable hydraulic press.
A product .for instance a board-like body made from stock having the major portion of relatively high freeness and the remainder of relatively low freeness, results in a complete bonding of the fibers under heat and pressure into a homogeneous and water-resisting product.
I claim:
1. The process of making a grainless and high strength board-like body from raw, unbeaten ground wood fibers which comprises commingling fibers having a freeness of 40 to 80 with fibers 'in a water suspension having a freeness of 500 to 700, the fibers having a freeness of 40 to 80 persent within the range of 5% to 20%, forming a board-like body and simultaneously applying heat and pressure to produce a dense and hard board.
2. The process of making a hard and highly water-resisting board-like body which comprises forming a board-like body from a mixture of 5% to 20% of raw and unbeaten ground wood fibrous material having a freene'ss of from 40 to 80 and 80% to 95% of raw and unbeaten wood fibrous stock having a freeness Within the range of 500 to 700, commingling with the fibers while in a water suspension 1% to 3% of casein, and simultaneously applying heat and pressure to consolidate and, dry the board.
3. The process of making high strength, boardlike body comprising mixing 5% to 20% unbeaten ground wood pulp having a freeness of 40 to 80 with 80% to 95% of unbeaten ground wood pulp having a freeness of 500 to 700, forming a board-- like body, simultaneously applying heat and pressure to compress the body into a dense and stiff product.
4. The process of making high strength, boardlike body comprising grinding wood to product pulp having a freeness of 500 to 700, grinding wood to produce pulp having a freeness of 40 to 80, commingling 5% to 20% of the 40 to 80 freeness stock with 80% to 95% of stock having a freeness of 500 to 700, forming a board from the mixture of fibers in a water suspension, and simultaneously applying heat and pressure to the board.
5. The process of making a hard, dense, grainless, board-like body which comprises grinding wood without substantial hydration into a freeness within the range of about 500 to 700, commingling 5% to 20% of raw ground wood having a freeness within the range of 40 to 80 with the disintegrated wood having a freeness of from 500 to 700 while in a water suspension, forming a board-like body, and simultaneously applying heat and pressure.
6. The process of making a hard and dense, board-like body which includes commingling 5 to 20% of unbeaten ground raw wood pulp having a freeness of approximately 60 with 80% to 95% of raw unbeaten Wood pulp in a water bath having a freeness of approximately 600, forming a board-like body, and simultaneously applying heat and pressure to the board-like body.
7. The process of making a hard and highly water-resisting, board-like body which includes grinding wood into raw, unbeaten pulp, 80% to 95% of the pulp having a freeness of about 500 to 700, 5% to 20% of the pulp having a freeness of about 40 to 80, forming a board-like body, and simultaneously applying heat and pressure to the board-like body to consolidate, densify and reduce the thickness of the board-like body.
GEORGE H. ELLIS.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US108372A US2161655A (en) | 1936-10-30 | 1936-10-30 | Method of making hard, dense, fibrous, boardlike products |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US108372A US2161655A (en) | 1936-10-30 | 1936-10-30 | Method of making hard, dense, fibrous, boardlike products |
Publications (1)
Publication Number | Publication Date |
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US2161655A true US2161655A (en) | 1939-06-06 |
Family
ID=22321839
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US108372A Expired - Lifetime US2161655A (en) | 1936-10-30 | 1936-10-30 | Method of making hard, dense, fibrous, boardlike products |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2654296A (en) * | 1948-03-18 | 1953-10-06 | James B Mccorkle | Process of producing primed hardboard |
US2832267A (en) * | 1954-03-29 | 1958-04-29 | Oregon Lumber Co | Method of making a paper covered hardboard |
US2918398A (en) * | 1953-02-19 | 1959-12-22 | Abitibi Corp | Artificial board |
US3113065A (en) * | 1961-06-12 | 1963-12-03 | Building Products Ltd | Resin bonded fibreboard and the process of making the same |
DE1240730B (en) * | 1963-02-08 | 1967-05-18 | Julius Wilisch | Plant for the production of cardboard |
US20080223269A1 (en) * | 2007-03-18 | 2008-09-18 | Paoluccio John A | Method and apparatus for biomass torrefaction using conduction heating |
-
1936
- 1936-10-30 US US108372A patent/US2161655A/en not_active Expired - Lifetime
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2654296A (en) * | 1948-03-18 | 1953-10-06 | James B Mccorkle | Process of producing primed hardboard |
US2918398A (en) * | 1953-02-19 | 1959-12-22 | Abitibi Corp | Artificial board |
US2832267A (en) * | 1954-03-29 | 1958-04-29 | Oregon Lumber Co | Method of making a paper covered hardboard |
US3113065A (en) * | 1961-06-12 | 1963-12-03 | Building Products Ltd | Resin bonded fibreboard and the process of making the same |
DE1240730B (en) * | 1963-02-08 | 1967-05-18 | Julius Wilisch | Plant for the production of cardboard |
US20080223269A1 (en) * | 2007-03-18 | 2008-09-18 | Paoluccio John A | Method and apparatus for biomass torrefaction using conduction heating |
US8449631B2 (en) * | 2007-03-18 | 2013-05-28 | John A. Paoluccio | Method and apparatus for biomass torrefaction using conduction heating |
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