US3455779A - Process of forming moisture resistant hardboard containing tall oil - Google Patents

Process of forming moisture resistant hardboard containing tall oil Download PDF

Info

Publication number
US3455779A
US3455779A US537931A US3455779DA US3455779A US 3455779 A US3455779 A US 3455779A US 537931 A US537931 A US 537931A US 3455779D A US3455779D A US 3455779DA US 3455779 A US3455779 A US 3455779A
Authority
US
United States
Prior art keywords
tall oil
hardboard
slurry
alum
water
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
Application number
US537931A
Inventor
Merle J Showalter
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Armstrong World Industries Inc
Original Assignee
Armstrong Cork Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Armstrong Cork Co filed Critical Armstrong Cork Co
Application granted granted Critical
Publication of US3455779A publication Critical patent/US3455779A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21JFIBREBOARD; MANUFACTURE OF ARTICLES FROM CELLULOSIC FIBROUS SUSPENSIONS OR FROM PAPIER-MACHE
    • D21J1/00Fibreboard
    • D21J1/16Special fibreboard
    • D21J1/18Hardboard
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L97/00Compositions of lignin-containing materials
    • C08L97/02Lignocellulosic material, e.g. wood, straw or bagasse

Definitions

  • the alum solution will be added with stirring, and once the alum solution has been thoroughly distributed throughout the wood fiber slurry, the tall oil salts may be added.
  • the salts of tall oil are readily made by reacting a solution of alkali metal hydroxide with the tall oil.
  • This invention relates generally to fiberboard and more particularly to a wood fiber hardboard. Still more particularly, the invention relates to a process of imparting moisture resistance to a pressure consolidated wood fiber hardboard.
  • the making of a hardboard normally involves reducing wood logs or billets to chips.
  • the chips are thenisubjected to a treatment with steam at pressure in the range of 90 to 175 pounds per square inch.
  • the time of treatment normally runs 1 to 10 minutes.
  • the chips are reduced to fibers by attrition processes such as disk refiners followed by further mechanical'refining as in a heater, Jordan engine or the like.
  • increasingly high steam pressures up to 1200 p.s'li. on the chips may be used, followed by quick depressur'i'zation to disintegrate the chips.
  • the fibers are formed into a slurry of suitable consistency and the slurry is passed to a drainage wire or form in order to produce a wet matQThe wet mat is partially dried and is subsequently consolidated under heat and pressure to form an excellent hardboard.
  • the invention contemplates imparting water resistance to hardboard by adding alum to the slurry of the wood fibers prior to mat formation. There is then added to the alum-treated slurry the watersoluble, alkali metal salt of tall oil.
  • the addition of alum to the wood fiber slurry is necessary to bring about the reaction of the subsequently added tall oil salts with the wood fibers.
  • the alum will preferably be added in the form of a water solution of papermakers alum.
  • the amount of alum to be added will be in the range of about 1% to 5% by dry weight paperat the upper end of this range, although the resulting hardboard may have a density higher than that normally desired.
  • a preferred range of amount of the tall oil is about 3% to 6% by weight tall oil based on the dry weight of the wood fibers.
  • the water solution of tall oil salt is simply added to the alum-treated slurry with stirring. After the tall oil solution has been thoroughly distributed throughout the slurry, it will be found that the tall oil salts have all reacted with the wood fibers.
  • the resulting tall-oil-reacted wood fibers may then be used to form hardboard in accordance with the known methods.
  • the mat will be formed generally in the range of thickness of l to 2 inches by passing the slurry to moving screens or molds.
  • the mat will normally be partially dried after draining to reduce the water content further.
  • One usable drying cycle involves drying the mat to a constant weight at 200 F. before pressing. Higher temperatures can be used for shorter times.
  • the mat before pressing will generally have a moisture content in the range of about 3% to 8% by weight.
  • the partially dried mat will then be pressed at elevated temperatures.
  • the pressures to be used will be in the range of 800 to 1500 pounds per square inch and the temperatures will be in the range of 300 F. to 500 F., with 400 F. being a good workable average. The higher temperatures are preferred.
  • a succession of high temperature rollers may be used.
  • the resulting hardboard having normal thicknesses in the range of 0.22 to 0.27 inch, will be found to have substantially improved water resistance as compared to hardboard which has not had the tall oil treatment.
  • the tall-oil-reacted hardboards have an improved modulus of rupture.
  • EXAMPLE 1 A solution of tall oil was prepared by mixing 795 parts water, 25 parts KOH, and parts tall oil. The resulting solution oftall oil salts was used as described below.
  • a slurry was prepared of 1% consistency containing 577 parts steam cooked refined aspen wood pulp. With stirring, there was added to this slurry parts 10% papermakers alum solution. After distribution of the alum solution throughout the slurry, there was then added parts of the tall oil solution prepared as described above. Agitation continued.
  • the slurry was then drained and pressed into a mat measuring 1 inch in thickness.
  • the mat was dried in an air-circulating oven maintained at 200 F. to a constant weight. It was then hot pressed for 15 minutes at 400 F. and a pressure of 1250 p.s.i. After pressing, the board was put in an oven at 300? F. and aged for 5 hours at that temperature.
  • the board containing 3% by weight tall oil, had the following properties: density, 62.4 pounds per cubic foot; modulus of rupture, 7415 pounds per square inch; linear expansion, 0.13%; water absorption, 8.9%, by change of weight.
  • the improved process of imparting water resistance to said hardboard comprising adding alum to said slurry, and adding to said alum- 5QThe"process accordingto claim 1 wherein said'alum 10 is added to 'said slurry in thetorm of a'water solution.

Description

July 15, 1969 WATER M. J. SHOWALTER 3,455,779
means 0! FORMING MOISTURE RESISTANT HARDBOARD CONTAINING TALL OIL Filed March 28. 1966 LOGS CH'PPING WATER AQUEOUS DIGESTION FIBER SLURRY FORMATION ALUM PRETREATMENT ALKALI METAL SALT OF TALL OH; TALL OIL REACTION MAT FORMATION HEAT PRESSURE PRODUCT INVENTOR MERLE J- SHOWALTER ATTORNEY United States Patent 3,455,779 PROCESS OF FORMING MOISTURE RESISTANT HARDBOARD CONTAINING TALL OIL Merle J. Showalter, Lancaster, Pa., assignor to Armstrong Cork Company, Lancaster, Pa., a corporation of Pennsylvania Filed Mar. 28, 1966, Ser. No. 537,931
Int. Cl. D21j 1/18; D21h 3/08 US. Cl. 162-179 6 Claims ABSTRACT OF THE DISCLOSURE A process, and product, of improving the water resistance of wood fiber hardboard. To a slurry of wood fibers is added alum to pretreat the fibers. There is then added to the alum-treated slurry an additive consisting essentially of the water-soluble, alkali metal salts of. tall oil. The hardboard is then formed in the usual manner..
"ice
makers alum based on the dry weight of the wood fibers. The alum solution will be added with stirring, and once the alum solution has been thoroughly distributed throughout the wood fiber slurry, the tall oil salts may be added.
The salts of tall oil are readily made by reacting a solution of alkali metal hydroxide with the tall oil. The
' of the wood fibers. Increased water resistance is obtained This invention relates generally to fiberboard and more particularly to a wood fiber hardboard. Still more particularly, the invention relates to a process of imparting moisture resistance to a pressure consolidated wood fiber hardboard. 1
The making of a hardboard normally involves reducing wood logs or billets to chips. The chips are thenisubjected to a treatment with steam at pressure in the range of 90 to 175 pounds per square inch. The time of treatment normally runs 1 to 10 minutes. After the steam treatment, the chips are reduced to fibers by attrition processes such as disk refiners followed by further mechanical'refining as in a heater, Jordan engine or the like. Alternatively, increasingly high steam pressures up to 1200 p.s'li. on the chips may be used, followed by quick depressur'i'zation to disintegrate the chips. The fibers are formed into a slurry of suitable consistency and the slurry is passed to a drainage wire or form in order to produce a wet matQThe wet mat is partially dried and is subsequently consolidated under heat and pressure to form an excellent hardboard.
The resulting hardboard, while possessing many excellent properties, has in the past suffered from water takeup. These hardboards will absorb water which reduces the strength of the board, and more important, causes appreciable dimensional change in the board. The attendant swelling and shrinkage causes destruction of the boards at their edges and also allows them to work loose. Accordingly, there is a need for an inexpensive but efiective process of rendering these hardboards more resistant to water absorption.
It is a primary object of the present inventionto supply this need. It is a further object of the present invention to supply a process of making a hardboard which will have enhanced water resistance and which at the same. time will possess increased strength and reduced linear expansion on water take-up. I
These objects are achieved in a strikingly effective and straight-forward manner. The invention contemplates imparting water resistance to hardboard by adding alum to the slurry of the wood fibers prior to mat formation. There is then added to the alum-treated slurry the watersoluble, alkali metal salt of tall oil.
The accompanying drawing is a simplified flow diagram of the process of the present invention.
The addition of alum to the wood fiber slurry is necessary to bring about the reaction of the subsequently added tall oil salts with the wood fibers. The alum will preferably be added in the form of a water solution of papermakers alum. The amount of alum to be added will be in the range of about 1% to 5% by dry weight paperat the upper end of this range, although the resulting hardboard may have a density higher than that normally desired. A preferred range of amount of the tall oil is about 3% to 6% by weight tall oil based on the dry weight of the wood fibers.
The water solution of tall oil salt is simply added to the alum-treated slurry with stirring. After the tall oil solution has been thoroughly distributed throughout the slurry, it will be found that the tall oil salts have all reacted with the wood fibers. The resulting tall-oil-reacted wood fibers may then be used to form hardboard in accordance with the known methods. The mat will be formed generally in the range of thickness of l to 2 inches by passing the slurry to moving screens or molds. The mat will normally be partially dried after draining to reduce the water content further. One usable drying cycle involves drying the mat to a constant weight at 200 F. before pressing. Higher temperatures can be used for shorter times. The mat before pressing will generally have a moisture content in the range of about 3% to 8% by weight.
The partially dried mat will then be pressed at elevated temperatures. The pressures to be used will be in the range of 800 to 1500 pounds per square inch and the temperatures will be in the range of 300 F. to 500 F., with 400 F. being a good workable average. The higher temperatures are preferred. Although it is preferred that the hardboard be pressed in fixed bed presses, a succession of high temperature rollers may be used.
The resulting hardboard, having normal thicknesses in the range of 0.22 to 0.27 inch, will be found to have substantially improved water resistance as compared to hardboard which has not had the tall oil treatment. As an additional advantage, the tall-oil-reacted hardboards have an improved modulus of rupture.
The following examples illustrate several embodiments of the invention. All parts are by weight unless otherwise stated.
EXAMPLE 1 A solution of tall oil was prepared by mixing 795 parts water, 25 parts KOH, and parts tall oil. The resulting solution oftall oil salts was used as described below.
A slurry was prepared of 1% consistency containing 577 parts steam cooked refined aspen wood pulp. With stirring, there was added to this slurry parts 10% papermakers alum solution. After distribution of the alum solution throughout the slurry, there was then added parts of the tall oil solution prepared as described above. Agitation continued.
The slurry was then drained and pressed into a mat measuring 1 inch in thickness. The mat was dried in an air-circulating oven maintained at 200 F. to a constant weight. It was then hot pressed for 15 minutes at 400 F. and a pressure of 1250 p.s.i. After pressing, the board was put in an oven at 300? F. and aged for 5 hours at that temperature.
The board, containing 3% by weight tall oil, had the following properties: density, 62.4 pounds per cubic foot; modulus of rupture, 7415 pounds per square inch; linear expansion, 0.13%; water absorption, 8.9%, by change of weight.
In contrast, a board prepared in the same manner bu' without the tall oil had a linear expansion of 0.23% and a water absorption of 15.9% by change of weight.
EXAMPLE 2 Boards were made as in Example 1, but containing different amounts of tall oil. Following are the results:
I claim:
-1. In the process of making a wood fiber hardboard by reducing wood to chips, subjecting the chips to an aqueous digestion, forming fibers from the resulting chips, forming said fibers into an aqueous slurry, and forming a hardboard from the slurry, the improved process of imparting water resistance to said hardboard comprising adding alum to said slurry, and adding to said alum- 5QThe"process accordingto claim 1 wherein said'alum 10 is added to 'said slurry in thetorm of a'water solution.
6. The productof claim l 1 References Cited UNITED "STATES" PATENTS 5 s. LEON BASHORE, Primary Examiner CI;'X.R.
US537931A 1966-03-28 1966-03-28 Process of forming moisture resistant hardboard containing tall oil Expired - Lifetime US3455779A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US53793166A 1966-03-28 1966-03-28

Publications (1)

Publication Number Publication Date
US3455779A true US3455779A (en) 1969-07-15

Family

ID=24144723

Family Applications (1)

Application Number Title Priority Date Filing Date
US537931A Expired - Lifetime US3455779A (en) 1966-03-28 1966-03-28 Process of forming moisture resistant hardboard containing tall oil

Country Status (1)

Country Link
US (1) US3455779A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3954555A (en) * 1972-09-29 1976-05-04 National Gypsum Company Fiber reinforced plastic articles and method of preparation
US5866641A (en) * 1996-06-22 1999-02-02 Wood Composite Technologies Inc Process for the production of lightweight cellular composites of wood waste and thermoplastic polymers
US5981631A (en) * 1996-07-09 1999-11-09 Wood Composite Technologies Inc. Process for the production of composites of co-mingled thermoset resin bonded wood waste blended with thermoplastic polymers

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2143831A (en) * 1932-01-02 1939-01-10 Insulite Co Synthetic products and process for making them
US2215244A (en) * 1935-07-03 1940-09-17 United States Gypsum Co Process of making pressed board products
GB842820A (en) * 1958-10-16 1960-07-27 Statens Skogsind Ab Improvements in and relating to hardening oils for hardboard
US3009820A (en) * 1959-12-04 1961-11-21 Hercules Powder Co Ltd Sizing composition
US3022527A (en) * 1959-01-22 1962-02-27 United Shoe Machinery Corp Machines for shaping uppers over lasts
US3306812A (en) * 1964-02-10 1967-02-28 Ca Nat Research Council Process of sizing shaped fibrous articles with powdered fatty acids of 18 to 24 c atoms

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2143831A (en) * 1932-01-02 1939-01-10 Insulite Co Synthetic products and process for making them
US2215244A (en) * 1935-07-03 1940-09-17 United States Gypsum Co Process of making pressed board products
GB842820A (en) * 1958-10-16 1960-07-27 Statens Skogsind Ab Improvements in and relating to hardening oils for hardboard
US3022527A (en) * 1959-01-22 1962-02-27 United Shoe Machinery Corp Machines for shaping uppers over lasts
US3009820A (en) * 1959-12-04 1961-11-21 Hercules Powder Co Ltd Sizing composition
US3306812A (en) * 1964-02-10 1967-02-28 Ca Nat Research Council Process of sizing shaped fibrous articles with powdered fatty acids of 18 to 24 c atoms

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3954555A (en) * 1972-09-29 1976-05-04 National Gypsum Company Fiber reinforced plastic articles and method of preparation
US5866641A (en) * 1996-06-22 1999-02-02 Wood Composite Technologies Inc Process for the production of lightweight cellular composites of wood waste and thermoplastic polymers
US5981631A (en) * 1996-07-09 1999-11-09 Wood Composite Technologies Inc. Process for the production of composites of co-mingled thermoset resin bonded wood waste blended with thermoplastic polymers

Similar Documents

Publication Publication Date Title
US4077833A (en) Fire resistant, bauxite-containing, wood composition board
US3707436A (en) Exploding of ammonia impregnated wood chips
US2120137A (en) Process of making ligno-cellulose fiber products
US2234188A (en) Process of making light-colored ligno-cellulose fiber
US2080077A (en) Molded products and process of making same
SE8202868L (en) PROCEDURE FOR PREPARING CHEAP CELLULOSAMASSA
US2068926A (en) Method of making artificial lumber
US2317394A (en) Process for making hardboard
US2047170A (en) Treatment of fibrous material
US3056718A (en) Process of treating hardboard surfaces
US3367828A (en) Hot, wet pressing technique of forming fiberboard
US3455779A (en) Process of forming moisture resistant hardboard containing tall oil
US2116544A (en) Method of enhancing the wetstrength of papers
US3305435A (en) Method of making paper stiffened with waste pulp liquor solids
US2208511A (en) Method of making dense wall panels
US2388487A (en) Process of making compressed fiber products
US2538742A (en) Digesting lignocellulose with a rosin soap
US2454534A (en) Process for defibering lignocellulose while subjected to steam and alkali-metal hydroxide
US4173248A (en) Medium density, high strength lignocellulose composition board including exhaustively hydrated cellulosic gel binder
US2044213A (en) Process of manufacturing hard board
US3386879A (en) Process for forming board containing cellulosic fibers, thermosetting binder and pinewood resin
US4227965A (en) Production of hardboard
US2571986A (en) Dry process for making composite products with ph control
US2490078A (en) Manufacture of plastic products from wood
US3262839A (en) Neutral to weakly alkaline sulfite process for the extraction of cellulose from cellulosic material