US1775405A - Art of paper making - Google Patents
Art of paper making Download PDFInfo
- Publication number
- US1775405A US1775405A US230689A US23068927A US1775405A US 1775405 A US1775405 A US 1775405A US 230689 A US230689 A US 230689A US 23068927 A US23068927 A US 23068927A US 1775405 A US1775405 A US 1775405A
- Authority
- US
- United States
- Prior art keywords
- soda
- wood
- pieces
- chemicals
- boiling
- 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
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 31
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 26
- 239000000463 material Substances 0.000 description 23
- 238000000034 method Methods 0.000 description 23
- 239000000126 substance Substances 0.000 description 15
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 13
- 239000000377 silicon dioxide Substances 0.000 description 13
- 239000002023 wood Substances 0.000 description 12
- 229920001131 Pulp (paper) Polymers 0.000 description 11
- 235000011118 potassium hydroxide Nutrition 0.000 description 11
- 238000009835 boiling Methods 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 7
- 235000013311 vegetables Nutrition 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 5
- 229920002678 cellulose Polymers 0.000 description 5
- 239000001913 cellulose Substances 0.000 description 5
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical class [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 5
- 239000000835 fiber Substances 0.000 description 4
- 239000000344 soap Substances 0.000 description 4
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 3
- 239000010902 straw Substances 0.000 description 3
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 2
- 235000017491 Bambusa tulda Nutrition 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- 244000082204 Phyllostachys viridis Species 0.000 description 2
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 2
- 241000209504 Poaceae Species 0.000 description 2
- 241000209140 Triticum Species 0.000 description 2
- 235000021307 Triticum Nutrition 0.000 description 2
- 239000011425 bamboo Substances 0.000 description 2
- 239000013043 chemical agent Substances 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 229920002955 Art silk Polymers 0.000 description 1
- 244000075850 Avena orientalis Species 0.000 description 1
- 235000007319 Avena orientalis Nutrition 0.000 description 1
- 244000025254 Cannabis sativa Species 0.000 description 1
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 description 1
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 235000004431 Linum usitatissimum Nutrition 0.000 description 1
- 240000006240 Linum usitatissimum Species 0.000 description 1
- 241000722288 Sabal Species 0.000 description 1
- 240000000111 Saccharum officinarum Species 0.000 description 1
- 235000007201 Saccharum officinarum Nutrition 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 235000009120 camo Nutrition 0.000 description 1
- 235000005607 chanvre indien Nutrition 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000011487 hemp Substances 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C3/00—Pulping cellulose-containing materials
- D21C3/02—Pulping cellulose-containing materials with inorganic bases or alkaline reacting compounds, e.g. sulfate processes
Definitions
- The'invent-ion relates to the art of paper makingand more particularly to a process and chemical agent for freeing and. separating the fibre or cellulose of wood, straw, bamboo, and other vegetable tissues from glutinuous, resinous, albuminous, siliceous and other intercellular and incrusting matters, to form paper pulp.
- paper pulp of the type which results from the use of chemicals has been made by crushing, chipping or cutting the vegetable tissues and then subjecting the product to a comparatively strong chemical whereby the cellulose is separated or freed from all foreign substances.
- two methods have been used, known respectively asthe soda or alkaline process and the sulphide or acid process.
- soda or alkaline process the wood after being reduced to chips or shavings is boiled from two to eight hours in a solution of soda which under normal conditions consists of approximately one sixteenth percent of Na O estimated on the barked and clean Wood. The boiling is done under a pressure which varies from ninety to as much as one hundred and fifty pounds per square inch.
- the prepared Wood is boiled in a solution of sulphurous acid (H 303) combined with a certain amount of base either magnesia or lime.
- H 303 sulphurous acid
- Similar processes are used to eliminate the foreign substances depending lar ely upon the character of the material. 11 any case, or instance, regardless of the specific process used, the chemicals heretofore employed have been of such strength and character that a comparatively large portion of the fibres, especially the weaker fibres in the central part of the tissues has been dissolved. As a result,
- One object of the present invention is to provide a process and chemical agent for re- Serial No. 230,689. Renewed. February 8, 1980.
- a further object of this invention is to provide a process or treatment of this character which renders the fibres or cellulose suitable for use in making high grade paper and artificial silk, requires less time than processes previously used and does not require the attention and careful performance which heretofore has been necessary.
- a further object of the invention is to provide a process for making paper pulp which is of an improved character, is comparatively simple, and reduces the cost of the finished product.
- the improved process or formula is applicable to wood, bamboo, flax, hemp, 1ute,
- banana-stalks sugar cane. corn-stalks, cotton, 1.;
- the process is carried out by first reducingthe material from which the pulp is to be formed to comparatively small pieces.
- the process is applied to wood, the latter is first chipped or shaved by any suitable machinery, or is defibered by mechanism, such for example, as that disclosed in Letters Patent of the United States,No.1,344,-
- the solution operates to separate the fibres and to dissolve the intercellular and incrusting materials or to form, together with the latter, soap.
- a characteristic of using the solution or chemicals specified is that the fibres are not attacked in any way and consesodium sulphide is added to the solution, in
- the material to be made into pulp is first crushed by any suitable machinery so that the natural or normal length of the fibres is not broken.
- This crushin operation serves to break or separate the silica coating and intercellular material so that they are more susceptible to the action of the chemicals which are used in the process.
- the crushed product is boiled in a solution containing silica of soda (33 to 66 Baum) and caustic potash in substantially the same proportions (four parts silica of soda and one part caustic soda) as us d in connection with wood, the amount depending upon the kind and condition of the material.
- the material When the process is applied to grasses, banana-stalks and like vegetable tissues, the material is crushed and boiled in a solution containing sodium sulphide in an amount ranging from two to twenty per cent of the dry weight of the material.
- the boiling is by methods or processes heretofore practiced.
- That improvement in the manufacture of paper pulp which consists in reducing the material to comparatively small pieces, and then immersing the pieces in a solution containing silica of soda and caustic potash.
- That improvement in the manufacture of paper pulp which consists in reducing the material to comparatively small ieces, and then immersing the pieces in a solution containing silica of soda and caustic potash sub stantially in'theratio specified, and ran g from two to twenty per cent of the dry weight of the pieces.
- That improvement in the manufacture of paper pulp which consists in reducing the material to comparatively small pieces, and then immersing the pieces in a solution containing silica of soda, caustic potash and sodium sulphide.
- silica of soda, caustic potash and sodium su phide substantially in I the ratio and Signed at'Chicago, Illinois, this 29th day of October, 1927.
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Paper (AREA)
Description
Patented Sept. 9, 1930 f PATENT OFFICE JOHN NEUMANN, OF CHICAGO, ILLINOIS ART OF PAPER MAKING No Drawing. Applieation' filed November 2, 1927,
The'invent-ion relates to the art of paper makingand more particularly to a process and chemical agent for freeing and. separating the fibre or cellulose of wood, straw, bamboo, and other vegetable tissues from glutinuous, resinous, albuminous, siliceous and other intercellular and incrusting matters, to form paper pulp.
Heretofore, paper pulp of the type which results from the use of chemicals has been made by crushing, chipping or cutting the vegetable tissues and then subjecting the product to a comparatively strong chemical whereby the cellulose is separated or freed from all foreign substances. 'In connection with wood, two methods have been used, known respectively asthe soda or alkaline process and the sulphide or acid process. In the soda or alkaline process, the wood after being reduced to chips or shavings is boiled from two to eight hours in a solution of soda which under normal conditions consists of approximately one sixteenth percent of Na O estimated on the barked and clean Wood. The boiling is done under a pressure which varies from ninety to as much as one hundred and fifty pounds per square inch. In the sulphide process, the prepared Wood is boiled in a solution of sulphurous acid (H 303) combined with a certain amount of base either magnesia or lime. In connection with hamboo, grasses and other vegetable tissues, similar processes are used to eliminate the foreign substances depending lar ely upon the character of the material. 11 any case, or instance, regardless of the specific process used, the chemicals heretofore employed have been of such strength and character that a comparatively large portion of the fibres, especially the weaker fibres in the central part of the tissues has been dissolved. As a result,
a portion of the cellulose is lost when the liquor or chemical solution is drained off after the boiling o aeration, and great waste occurs. Additionally great care must be exercised in connection with these processes otherwise the chemicals will attack and destroy a greater percentage of the fibre.
One object of the present invention is to provide a process and chemical agent for re- Serial No. 230,689. Renewed. February 8, 1980.
ducing woodand other vegetable tissues to paper pulp which will effectively dissolve and free all of the intercellular and-incrusting materials without attacking in any way or manner the fibers. As a result, a'material saving is occasioned because practically the entire amount of cellulose is obtained from the tissues.
A further object of this invention is to provide a process or treatment of this character which renders the fibres or cellulose suitable for use in making high grade paper and artificial silk, requires less time than processes previously used and does not require the attention and careful performance which heretofore has been necessary.
A further object of the invention is to provide a process for making paper pulp which is of an improved character, is comparatively simple, and reduces the cost of the finished product.
Other objects will appear hereafter from the detailed description.
The invention consists in the process and chemical a'gent'hereinafter set forth and more particularly defined by the claims at the conclusion hereof,
The improved process or formula is applicable to wood, bamboo, flax, hemp, 1ute,
banana-stalks, sugar cane. corn-stalks, cotton, 1.;
cotton-stalks, straw, palmettos, and rice, wheat and oat-stems, and other various vegetable tissues. The process is carried out by first reducingthe material from which the pulp is to be formed to comparatively small pieces. When the process is applied to wood, the latter is first chipped or shaved by any suitable machinery, or is defibered by mechanism, such for example, as that disclosed in Letters Patent of the United States,No.1,344,-
180, granted to Uel S. McMillan on the22nd day of June, 1920. The wood product is then boiled in a solution containin silica of soda (33 to 66 Baum) and caustic potash. In actual practice, it has been found that the best results are obtainable by using four parts of silica of soda and one part caustic potash, that is by using the chemicals in a ratio of four to one. The chemicals are used in this proportion'i'n amounts ranging from for about two hours.
two to twenty per cent of the dry weight of the wood,- depending mainly upon the kind of wood being treated and the condition thereof. The solution operates to separate the fibres and to dissolve the intercellular and incrusting materials or to form, together with the latter, soap. A characteristic of using the solution or chemicals specified is that the fibres are not attacked in any way and consesodium sulphide is added to the solution, in
an amount ranging from two to twenty per cent of the dry weight of the material, depending of course u on the condition and kind of wood used. enerally an amount is added which is equal to the two chemicals first used. This sodium sulphide accelerates or assists the silica of soda and caustic potash to break down the incrusting and intercellular material or to form soap of same. The boiling is then continued for a period which need not exceed two hours, and under a pressure which may vary from five pounds to one hundred and twenty-five pounds per square-inch. At the conclusion of the boiling, the liquors including any soap resulting from the action of the chemicals upon the resin, fat and other intercellular and incrusting material are drained. The fibre is then washed in the usual way to remove thoroughly the solution and soap and to place it in condition to be bleached.
When the process is applied to corn-stalks, straw or the stems of rice, wheat and oats, the material to be made into pulp is first crushed by any suitable machinery so that the natural or normal length of the fibres is not broken. This crushin operation serves to break or separate the silica coating and intercellular material so that they are more susceptible to the action of the chemicals which are used in the process. The crushed product is boiled in a solution containing silica of soda (33 to 66 Baum) and caustic potash in substantially the same proportions (four parts silica of soda and one part caustic soda) as us d in connection with wood, the amount depending upon the kind and condition of the material. The boiling; is continued Then the liquor is drained and the fibres washed and bleached in any suitable manner. In practice, it has been found that the materials above referred to do not need to have sodium sulphide introduced into the solution during the boiling thereof, and that the fibres freed are in a superior condition and are undissolved.
When the process is applied to grasses, banana-stalks and like vegetable tissues, the material is crushed and boiled in a solution containing sodium sulphide in an amount ranging from two to twenty per cent of the dry weight of the material. The boiling is by methods or processes heretofore practiced.
The process is not to be understood asbeing limited or restricted to the specified proportions and amounts of the chemicals since these may be changed to meet the various kinds of materials and the condition thereof.
Having thus described the invention, what I claim as new and desire to secure by Letters Patent, is:
1. That improvement in the manufacture of paper pulp which consists in reducing the material to comparatively small pieces, and then immersing the pieces in a solution containing silica of soda and caustic potash.
9.. That improvement in the manufacture of paper pulp which consists in reducing the material to comparatively small pieces, and then immersing the pieces in a solution containing silica of soda and caustic potash substantially in the ratio specified.
3. That improvement in the manufacture of paper pulp which consists in reducing the material to comparatively small ieces, and then immersing the pieces in a solution containing silica of soda and caustic potash sub stantially in'theratio specified, and ran g from two to twenty per cent of the dry weight of the pieces.
4. That improvement in the manufacture of paper pulp which consists in reducing the material to comparatively small pieces, and then boiling the pieces in a solution containing silica of soda and caustic potash and until the fibres are entirely free from the intercellular and incrusting material.
5. That improvement in the manufacture of paper pulp which consists in reducing the material to comparatively small pieces, and then immersing the pieces in a solution containing silica of soda, caustic potash and sodium sulphide.
6. 'That improvement in the manufacture of paper pulp which consists in reducing the material to comparatively small pieces, then boiling the pieces in a solution containing silica of soda and caustic potash, and then adding sodium sulphide.
- 7. That improvement in the manufacture of paper pulp which consists in reducing the amounts specified.
material to comparatively small pieces, and then boiling the pieces in a solution containin? silica of soda, caustic potash and sodium su phide substantially in I the ratio and Signed at'Chicago, Illinois, this 29th day of October, 1927.
' JOHN NEUMANN.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US230689A US1775405A (en) | 1927-11-02 | 1927-11-02 | Art of paper making |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US230689A US1775405A (en) | 1927-11-02 | 1927-11-02 | Art of paper making |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1775405A true US1775405A (en) | 1930-09-09 |
Family
ID=22866186
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US230689A Expired - Lifetime US1775405A (en) | 1927-11-02 | 1927-11-02 | Art of paper making |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1775405A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3023140A (en) * | 1958-11-24 | 1962-02-27 | Bauer Bros Co | Pulp bleaching |
| US3147178A (en) * | 1961-05-18 | 1964-09-01 | St Joe Paper Company | Sulphate digestion process |
-
1927
- 1927-11-02 US US230689A patent/US1775405A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3023140A (en) * | 1958-11-24 | 1962-02-27 | Bauer Bros Co | Pulp bleaching |
| US3147178A (en) * | 1961-05-18 | 1964-09-01 | St Joe Paper Company | Sulphate digestion process |
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