US2473190A - Method of producing fibrous building compositions - Google Patents
Method of producing fibrous building compositions Download PDFInfo
- Publication number
- US2473190A US2473190A US543196A US54319644A US2473190A US 2473190 A US2473190 A US 2473190A US 543196 A US543196 A US 543196A US 54319644 A US54319644 A US 54319644A US 2473190 A US2473190 A US 2473190A
- Authority
- US
- United States
- Prior art keywords
- asphalt
- paper
- fibrous material
- flux oil
- pulp
- 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
- 239000000203 mixture Substances 0.000 title description 36
- 238000000034 method Methods 0.000 title description 26
- 239000010426 asphalt Substances 0.000 description 47
- 239000003921 oil Substances 0.000 description 44
- 230000004907 flux Effects 0.000 description 40
- 239000002657 fibrous material Substances 0.000 description 33
- 239000000123 paper Substances 0.000 description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 14
- 235000011941 Tilia x europaea Nutrition 0.000 description 14
- 239000004571 lime Substances 0.000 description 14
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- 239000000463 material Substances 0.000 description 11
- 239000011087 paperboard Substances 0.000 description 11
- 239000000835 fiber Substances 0.000 description 10
- 150000003839 salts Chemical class 0.000 description 9
- 239000002002 slurry Substances 0.000 description 9
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- 241000609240 Ambelania acida Species 0.000 description 6
- 239000010905 bagasse Substances 0.000 description 6
- 239000004927 clay Substances 0.000 description 6
- 229940120693 copper naphthenate Drugs 0.000 description 6
- SEVNKWFHTNVOLD-UHFFFAOYSA-L copper;3-(4-ethylcyclohexyl)propanoate;3-(3-ethylcyclopentyl)propanoate Chemical compound [Cu+2].CCC1CCC(CCC([O-])=O)C1.CCC1CCC(CCC([O-])=O)CC1 SEVNKWFHTNVOLD-UHFFFAOYSA-L 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 229920001131 Pulp (paper) Polymers 0.000 description 5
- 229910052782 aluminium Inorganic materials 0.000 description 5
- 150000007524 organic acids Chemical class 0.000 description 5
- HNNQYHFROJDYHQ-UHFFFAOYSA-N 3-(4-ethylcyclohexyl)propanoic acid 3-(3-ethylcyclopentyl)propanoic acid Chemical compound CCC1CCC(CCC(O)=O)C1.CCC1CCC(CCC(O)=O)CC1 HNNQYHFROJDYHQ-UHFFFAOYSA-N 0.000 description 4
- 239000012670 alkaline solution Substances 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 235000005985 organic acids Nutrition 0.000 description 4
- 235000011121 sodium hydroxide Nutrition 0.000 description 4
- 239000004575 stone Substances 0.000 description 4
- 238000004078 waterproofing Methods 0.000 description 4
- -1 aluminum naphthenate Chemical class 0.000 description 3
- 239000004568 cement Substances 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000012764 mineral filler Substances 0.000 description 2
- 241000896693 Disa Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000007900 aqueous suspension Substances 0.000 description 1
- 239000011111 cardboard Substances 0.000 description 1
- 238000004182 chemical digestion Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 125000005609 naphthenate group Chemical group 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/61—Bitumen
-
- 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
- D21J1/08—Impregnated or coated fibreboard
Definitions
- This invention relates to improvements in the bituminous materials used for waterproofing and methods of manufacturing paper, paper felt, and cementing.
- a method of preparing a composition of fibre board which comprises breaking up a fibrous material .into a state of fine subdivision, im-
Landscapes
- Paper (AREA)
Description
June 14,1949 2,473,19
. l 2 This invention relates to improvements in the bituminous materials used for waterproofing and methods of manufacturing paper, paper felt, and cementing.
' paper boards, and particularly in the manufac- Other objects of this invention will be more ture of paper, paper felt, and paper boards that readily understood after reading the following are impervious to moisture and water, and capable 5 description. of high resistance to damage under handling and According to this invention, bagasse or other other stresses, even when subjected to extreme fibrous material was broken up or pulverized in a temperature changes. hammer mill and mixed with flux oil up to an Fibrous pulp is produced principally by meamount of about part of flux oil to 1 part of METHOD OF PRODUCING FIBROUS v BUILDING COMPOSITIONS Charles M. Baskin, Toronto, Ontario, and Norman W. McLeod, Sarnia, Ontario, Canada, assignors to Standard Oil Development Company, a corporation of Delaware No Drawing. Application July 1, 1944, Serial No. 543,196. In Canada July 19, 1943 13 Claims. (Cl. 92-21) UNITED STATES PATENT OFFICE chanical grinding whereby the wood or other fibre. This mixture was then charged intoa stapulp-forming material such as bagasse from tionary pressure cooker and digested with a 1.5 wa t sugar e, lt ha t is disintegrated r Be. solution of caustic soda at 100 lbs. pressure for pulverized by rough tones rotating against the 2'hours. The digested mass was beaten and regrain, by hammer mills or other disintegrators duced to a fairly fine pulp, during which process and by chemical digestion. In either case, the 15 e p lverized asphalt and additional flux oil was pulp before it is processed and converted into added to give an overall total of fl il equal t paper, cardboard or building board, is always dia u /12 Pa t fl x Oil t 1 part of fibre. A uni- ]uted t water, Pulp as produced is really a form dispersion of the pulverized asphalt and flux suspension of small quantities of fibre in large oil in the digested mass was then obtained and quantities of water. In the process of producing there Was o o ty With a p dhering to roofing paper, the pulp is first mad i t a paper the screens while removing water by means of or as it is commonly known in the roofing in- I pressure. The sheets 02' pads thereby obtained dustiy, felt. This felt is then transported to the contained about 60 to QLZI ll and were roofing plant and treated by saturating with flux p s ed through a drier at a temperature of about oil, asphalt, or a mixture of flux oil and asphalt, and then repressed While hot herethen coated with a higher melting point asphalt, Sultant Sheet r b a a o t e verage, which coating is imbedded with various types of e at ro f than s andard satu at d asphalt mineral covering material and the sheet is then ofing. The proportions of asphalt to fibre in made up in rolls or cut into shingleg In the prothe fibrous board were 121 by weight whereas the a ti of r fi t paper sheet or f lt, 30 standard asphalt saturated sheet contains at tains as a, rule, very little mechanical wood pulp least of asphalt to 1 of fi e. but is largely disintegrated and pulped rags, and Alternate]! it Was f und hat if the mechanisome chemically digested long-fibre wood pulp. Cally broken p S ar Cane or other fibrous mabje t of thisinventionis t provide ametl'h terial is mixed with the fiux oil and allowed to od whereby bitumen impregnated paper, paper stand for 1 to 2 weeks, very definite and material felt, or paper boards, are turned out directly from improvement is obtainedv not o y n he disa paper making or paper board making machine, persion of the flux oil and powdered asphalt and and the necessity for the present process of satufiller during the eat process but particularly rating with a bituminous material is eliminated. in the Water-proofing o t e final product. It Another object of this invention is to provide 0 was found that the l r the mixture of mea method for turning out waterproof or moisture chanically d s n egrated bagasse and flux 11 i proof paper, paper felt, or paper board directly allowed to remain in the stock pile before cooking from a paper making or paper board making or digesting, the better is the subsequent dischine, in which the bituminous material is conpersion in the beater d e mo e Waterproof tained in the inner portion of the paper sheet, the finished P paper felt, or paper board, but does not show on Lime may be W in the digestion and it is th outside layers This is an improvement over preferred in that it is relatively inexpensive and existing methods, and eliminates the necessity for available in all localities. the present process of laminating two or more Another desirable feature in using lime is that sheets of paper using bituminous cements. the lime soaps or any combination of lime with A further object of this invention is to modify lignous material are invariably insoluble in water, the characteristics of the waterproofed paper, whereas the products of reaction of lignous matpaper felt, or paper board. by incorporating heavy ter with caustic soda or soda sulflte or sulfate are metal salts of organic acids, such as aluminum all exceedingly water-soluble. When lime is used, naphthenate, copper naphthenate, etc.. into the it was found preferable that mechanically dismixed with a clay-water-asphalt slurry,
integrated bagasse and flux oil be premixed and allowed to soak for several days, and preferably for two weeks or longer.
It is not necessary that the asphalt be used in powdered form as it was found that high softening point low temperature susceptibility asphalt, for example having a softening point of about 140 to 240 F., may be used. As these particular high softening point-low susceptibility asphalts can not be pulverized in that they may be rubbery and tacky, they may be dispersed in stone dust or clay-water slurries to obtain an asphalt-clay-water paste wherein the asphalt is dispersed in extremely fine particles, in fact, considerably finer than current asphalt powders. The use of clay was found to be preferable over the use of stone dust as dry clay can be pulverized in a hammer mill and then plasticized with water at a lower cost than reducing lime stone or the like to a fineness below 200 mesh. Clay when properly plasticized makes a much finer filler than stone dust. fillers with high softening point-low temperature susceptibility asphalt, a more pliable final product is obtained.
For example, mechanically disintegrated bagasse is mixed with flux oil and stored for one or two weeks and then digested with a lime solution of about concentration for about 2 hours at about 100 lbs. per square inch steam pressure. This mass of digested disintegrated fibrous material and flux oil is next mixed with a clay-waterasphalt slurry, then dispersed as a pulp, and finally picked up by the continuous blanket of the wet machine. If a waterproof paper is being produced, the paper felt is removed from the blanket and passed through steam heated rolls for drying. If a waterproof board is being produced, the thick paper felt after being removed from the blanket is carried by a conveyor through a long hot air tunnel where it is dried.
Alternatively, asphalt cement, or a combination of asphalt cement with a heavy metal salt of an organic acid, such as aluminum naphthenate, copper naphthenate, etc., is dispersed in a mixture of clay and water to form an asphaltclay-water paste. After this paste is formed, it can be reduced to a slurry of any desired consistency by incorporating additional water.
For example, mechanically disintegrated bagasse is mixed with flux oil and stored for one or two weeks or longer, and then digested with a lime solution of about 10% concentration for about 2 hours at about 100 pounds per square inch steam pressure. This mass of digested disintegrated fibrous material and flux oil is next (in which up to 75% of heavy metal salts of organic acids such as aluminum naphthenate, copper naphthenate, etc., may be incorporated in the bitumen) then dispersed as a pulp, and finally picked up by the continuous blanket of the wet machine. If a waterproof paper or paper felt is being produced, the thin felted layer is removed from the blanket and passed through steam heated rolls, or through a long hot air tunnel, for drying. If a waterproof paper board is being produced, the
By using clay or stone dust thick felted layer, after being removed from the blanket, is carried by a conveyor through a long hot air tunnel where it is dried.
It is sometimes desirable to introduce the waterproof material between layers of paper so that the waterproofing material would be contained in the inner portion of the sheet and would not show on the outside layers. This may be readily done by forming one or more layers of paper felt introducing asphalt-clay-water suspension into one or more succeeding layers of paper felt, and finally covering with one or more layers of the paper felt, all of these operations being carried out as the layers of paper felt are being built up on the continuous blanket of the wet machine. This may be accomplished by either one or both of the following two methods:
1. In a paper machine consisting of several compartments, the clay-water-asphalt paste or slurry can be dispersed with the pulp in one or more of the central compartments, but not in the end compartments. In this way the blanket picks up a layer of paper pulp from the wet cylinder in the first one or more compartments, followed by a layer of paper pulp containing the claywater-asphalt dispersion, from the wet cylinder in each of one or more of the central compartments, and finally picks up a layer of paper pulp alone from the wet cylinder in each of one or more compartments in the end of the machine. By this procedure, a waterproofed paper sheet or paper board is obtained, which consists of central layers of pulp fibre impregnated with asphalt, contained within an envelope of outer layers of pulp fibre which do not contain asphalt.
2. This method is similar to (1) with the exception that in one or more of the central compartments of the wet machine, where the inner layers of the paper sheet or board are formed, the asphalt-clay-water slurry or paste is introduced into the pulp just as the fibre is being picked up by the wet cylinder, by spraying, etc.
In all cases, it should be clearly understood that the bituminous material used in the above processes for waterproofing and cementing purposes, may contain up to about 75% of metal salts of organic acids, such as aluminum naphthenate, copper naphthenate, etc. These compounds may be dissolved in the hard asphalt, in the flux oil, or both. They may also be added separately at some stage in the process, where they will combine with the bitumen, fibre, and mineral filler. These metal salts of organic acids modify the rigidity or pliability and other characteristics of the waterproofed paper sheet, paper felt, or paper board.
We claim:
1. A method of preparing a building composition which comprises breaking up a fibrous material into a state of fine subdivision, adding about part of a flux oil to about 1 part of the divided fibrous material, adding an alkaline solution to the mixture of fibrous material and flux oil, digesting at lbs. per square inch steam pressure for two hours the fibrous material, flux oil and alkaline solution to form a fibrous pulp, dispersing in the fibrous pulp an asphalt and flux oil, picking up the mixture of fibrous material, flux oil and asphalt in layers on a continuous blanket to form sheets, and submitting the said sheets of fibrous material, asphalt and flux oil to pressure and heat to remove water.
2. A method of preparing a building composition which comprises breaking up a fibrous material into a state of fine subdivision, adding about /2 part of a flux oil to about 1 part of the divided fibrous material, adding caustic soda to the fibrous material and flux oil, digesting at 100 lbs. per square inch steam pressure for two hours the fibrous material, flux oil and caustic soda to form a fibrous pulp. dispersing in the fibrous pulp an asphalt and flux oil, picking up the mixture of the fibrous material, flux oil and asphalt in lay-v ers on a continuous blanket to form sheets, and submitting the said sheets of fibrous material, flux oil and asphalt to pressure and heat to remove water.
3. A method of preparing a building composition which comprises breaking up a fibrous ma? terial into a state of fine subdivision, adding about t part of a fiux oil to about 1 part of the divided fibrous material, adding a solution of lime to the fibrous material, digesting at 100 lbs. per square inch steam pressure for two hours the fibrous material, flux oil and solution of lime to form a fibrous pulp, dispersing in the fibrous pulp an asphalt and flux oil, picking up the mixtureof fibrous pulp, asphalt, flux oil and lime in layers on a continuous blanket to form sheets, and submitting the'said sheets to pressure and heat to remove water.
4. A method of which comprises preparing a composition board mechanically subdividing a fibrous material, adding a flux oil to the finely divided fibrous material, allowing the mixture of finely divided fibrous material and flux oil to stand for at least seven days, adding a lime solution oi. about concentration to the mixture of fibrous material and flux oil, digesting the mixture for about two hours at 100 pounds per square inch steam pressure, dispersing asphalt and flux oil in the mixture, picking up the mixture of fibrous material, flux oil, asphalt and lime in layers on a continuous blanket to form sheets, and submitting the said sheets to pressure and heat to obtain a composition board.
5. A method of preparing a composition board according to claim 4 in which asphalt is dispersed as a clay asphalt slurry containing copper naphthenate.
6. A method of preparing a composition board according to claim 4 in which the asphalt is displaced as a clay-water-asphalt slurry.
7. A method of preparing a composition board according to claim 4 in which asphalt is dispersed as a clay-asphalt slurry containing a metal salt of naphthenic acid.
8. A method of preparing a composition of fibre board which comprises breaking up a fibrous material .into a state of fine subdivision, im-
the finely divided material with about 95 part of a flux oil, allowing the mixture to stand for at least seven days, adding lime to the mixture, digesting at 100 lbs. per square inch steam pressure for two hours the mixture to form a fibrous pulp, dispersing asphalt with the fibrous pulp, picking up the mixture of fibrous'pulp, flux oil, asphaltand lime in layers on a'continuous blanket to form sheets, and submitting' the said sheets to pressure and heat to tion. which comprises breaking up a fibrous material into a state of fine subdivision, impregnating about 1' part of the finely divided fibrous material with about part of a fiux oil, allowing the mixture of fibrous material and flux oil to stand for at least several days, adding an alkaline solution to the mixture of finely divided fibrous material and flux oil, digesting at 'lbs'. per square inch steam pressure for two hours the mixture of finely divided fibrous material, alkaline solution and flux oil, dispersing asphalt and a metal salt of naph thenic acid in the fibrous material mixture, picking up the mixture of fibrous material, flux oil and asphalt in layers on a continuous blanket to form sheets, and submitting the sheets. to pressure and heat to form a building composition containing 1 part by weight of asphalt to 1 part by weight of the fibrous material.
11. A method of preparing a building composition according to claim 10 in which the metal salt of naphthenic acid is aluminum naphthenate. 12. A method of preparing a building composition according to claim 10 in which the metal salt of naphthenic acid is copper naphthenate.
- 13. A method of preparing a building composition according to claim 10 in which 1 part of the fibrous material, 1 part of the asphalt and 1 part of a mineral filler are used.
' CHARLES M. BASKIN.
NORMAN W. MCLEOD.
REFERENCES CITED The following references are of record in .the'
Oct. 1, 1940
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA2473190X | 1943-07-19 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2473190A true US2473190A (en) | 1949-06-14 |
Family
ID=4176146
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US543196A Expired - Lifetime US2473190A (en) | 1943-07-19 | 1944-07-01 | Method of producing fibrous building compositions |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2473190A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2668110A (en) * | 1948-06-18 | 1954-02-02 | Spencer | Method for fiber liberation in cotton stalks and the pulp |
| US2676885A (en) * | 1946-09-19 | 1954-04-27 | Syntics Ltd | Manufacture of articles such as boards and sheets from fibrous vegetable materials |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1657585A (en) * | 1920-08-20 | 1928-01-31 | Barrett Co | Construction material |
| US1754343A (en) * | 1929-01-16 | 1930-04-15 | Multibestos Company | Process of making friction facings |
| US1812515A (en) * | 1929-07-11 | 1931-06-30 | Corcoran Mfg Company | Automobile radiator core |
| US2072686A (en) * | 1935-12-16 | 1937-03-02 | Lancaster Processes Inc | Composition of matter and method of making the same |
| US2132607A (en) * | 1934-05-28 | 1938-10-11 | Standard Oil Co California | Bituminous emulsions and method of producing same |
| US2216311A (en) * | 1934-05-28 | 1940-10-01 | Standard Oil Co California | Bituminous emulsions and method of producing same |
-
1944
- 1944-07-01 US US543196A patent/US2473190A/en not_active Expired - Lifetime
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1657585A (en) * | 1920-08-20 | 1928-01-31 | Barrett Co | Construction material |
| US1754343A (en) * | 1929-01-16 | 1930-04-15 | Multibestos Company | Process of making friction facings |
| US1812515A (en) * | 1929-07-11 | 1931-06-30 | Corcoran Mfg Company | Automobile radiator core |
| US2132607A (en) * | 1934-05-28 | 1938-10-11 | Standard Oil Co California | Bituminous emulsions and method of producing same |
| US2216311A (en) * | 1934-05-28 | 1940-10-01 | Standard Oil Co California | Bituminous emulsions and method of producing same |
| US2072686A (en) * | 1935-12-16 | 1937-03-02 | Lancaster Processes Inc | Composition of matter and method of making the same |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2676885A (en) * | 1946-09-19 | 1954-04-27 | Syntics Ltd | Manufacture of articles such as boards and sheets from fibrous vegetable materials |
| US2668110A (en) * | 1948-06-18 | 1954-02-02 | Spencer | Method for fiber liberation in cotton stalks and the pulp |
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