USRE4203E - Improvement in the manufacture of paper-pulp from straw - Google Patents
Improvement in the manufacture of paper-pulp from straw Download PDFInfo
- Publication number
- USRE4203E USRE4203E US RE4203 E USRE4203 E US RE4203E
- Authority
- US
- United States
- Prior art keywords
- straw
- pulp
- paper
- manufacture
- improvement
- Prior art date
Links
- 239000010902 straw Substances 0.000 title description 10
- 238000004519 manufacturing process Methods 0.000 title description 5
- 229920001131 Pulp (paper) Polymers 0.000 title description 4
- 239000000126 substance Substances 0.000 description 12
- 239000000463 material Substances 0.000 description 9
- 239000003513 alkali Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 5
- 239000000835 fiber Substances 0.000 description 5
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 4
- 235000012970 cakes Nutrition 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate dianion Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000015450 Tilia cordata Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 210000004080 Milk Anatomy 0.000 description 1
- VWDWKYIASSYTQR-UHFFFAOYSA-N Sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000002956 ash Substances 0.000 description 1
- 238000010009 beating Methods 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium monoxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000003415 peat Substances 0.000 description 1
- 229940072033 potash Drugs 0.000 description 1
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 1
- 235000015320 potassium carbonate Nutrition 0.000 description 1
- 235000011118 potassium hydroxide Nutrition 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 235000013599 spices Nutrition 0.000 description 1
- 239000005418 vegetable material Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Definitions
- My invention consists in reducing the straw or wood or other vegetable material the fiber whereof is suitable for the manufacture of paper to pulp by subjecting said material to the combined action of a chemical and mechani cal agent, the mechanical agent reducing the material to small particles, while at the same time the chemical agent dissolves or separates the fiber from the foreign matter, or that part of the material not suitable for the manufacture of paper; and my invention also consists in recovering a portion of the alkali used as the chemical agent in the process.
- the reduction may be accomplished by any suitable mill provided with grinding or other suitable action, and which will not be attacked by hot alkali.
- the thing is to mechanically reduce or disintegrate the material while it is subjected to the action of the solvent without regard to the kind of machine or mill by which the reduction is accomplished. or the kind of solvent used in the process.
- the large iron mills used for grinding spices answer a very good purpose, though other machines may be devised and used for this purpose more efficiently.
- the mill should be of sufficient size to pass through large quantities in a short time.
- Caustic potash, or,w hat is better, a combination of potash and soda, in the proportion of their chemical equivalents, may be used instead of causticsoda.
- the specific gravity of the alkaline solution may be reduced very considerably by giving more time to the boiling; but the gravity stated gives most satisfactory results whenever the grinding is sufficiently rapid.
- the pulp as it comes from the combined mechanical chemical treatment is thoroughly drained, to save the alkaline liquor, then washed, neutralized, and bleached in the usual manner.
- the advantages resulting from my invention are, first, by an immediate mechanical subdivision of the straw or other vegetablesubstance by grinding itin the incipient stages of the alkaline action the of surface is exposed at once to the chemical action of the solvent, thus saving many hours time, and obviating, Ithink, entirely the necessity of high pressure, or a temperature above the boiling-point of the solution, so that an open tank may be used in the process instead of a tight boiler, though experience may show it to be expedient to use a close vessel with more or less pressure; second, the material being most thoroughly reduced to its ultimate fiber by this process, the pulp may be bleached more readily and at less expense than hitherto; third, the time of treatment is so short and the temperature so not weakened as in other processes; fourth,
Description
- Straw or other Vegetable UNITED STATES PATENT OFFIC ASAHEL K. EATON, OFNEW YORK, N. Y.
IMPROVEMENT IN THE MANUFACTURE OF' PAPER-PULP FROM STRAW, &c.
Specification forming partof Letters Patent No. 41,982, dated March 22, 1864 Reissue No. 41,203. dated December 20, 1870.
To all whom it may concern:
Be it known that I, ASAHE'L K. EATON, of the city, county, and State of New York, have invented certain new andnseful Improvements in the Art of Manufacturing Paper-Pulp from Substance; and I do hereby declarethe following to be a full, clear, and accurate description thereof.
My invention consists in reducing the straw or wood or other vegetable material the fiber whereof is suitable for the manufacture of paper to pulp by subjecting said material to the combined action of a chemical and mechani cal agent, the mechanical agent reducing the material to small particles, while at the same time the chemical agent dissolves or separates the fiber from the foreign matter, or that part of the material not suitable for the manufacture of paper; and my invention also consists in recovering a portion of the alkali used as the chemical agent in the process.
In the practice of my invention I proceed as follows: I first introduce the straw, either cut, ground, or whole, into a tank or boiler containing a boiling solution of caustic soda having a specific gravity of about 1.06, and immel l l 1 l l,
but the reduction may be accomplished by any suitable mill provided with grinding or other suitable action, and which will not be attacked by hot alkali. The thing is to mechanically reduce or disintegrate the material while it is subjected to the action of the solvent without regard to the kind of machine or mill by which the reduction is accomplished. or the kind of solvent used in the process. The large iron mills used for grinding spices answer a very good purpose, though other machines may be devised and used for this purpose more efficiently. The mill should be of sufficient size to pass through large quantities in a short time. Caustic potash, or,w hat is better, a combination of potash and soda, in the proportion of their chemical equivalents, may be used instead of causticsoda. The specific gravity of the alkaline solution may be reduced very considerably by giving more time to the boiling; but the gravity stated gives most satisfactory results whenever the grinding is sufficiently rapid. The pulp as it comes from the combined mechanical chemical treatment is thoroughly drained, to save the alkaline liquor, then washed, neutralized, and bleached in the usual manner.
diatel subject it to the action of a suitable ma- The spent alkali resulting from this treatment chine or agent for reducing the material to small particles-such as cutting, beating, rubbing, or grinding surfacesfor the purpose of separating longitudinally the fiber of the straw or other material undergoing treatment. It is essential that this mechanicalaction should begin in the incipient stages of the chemical ac tion of the alkali, and strength of fiber by exposing the greatest possible amount of surface to the solvent, and the process should be continued until the material is sufficiently reduced, or n ntil the pulp is finished. If it is not convenient to grind within the tank, I first boil the straw for fifteen minutes, then transfer to the'mill and grind it,
and then boil it again for from fifteen to thirty minutes, following this by grinding again, &c. Two or, at most, three successive alternations of this chemical and mechanical.treatment aresufiicient.
It is immaterial what kind of a machine is used for the mechanical reduction of the material. A grinding action is,
I think, the best;
in order to economize time I liquor.
is a dark-colored liquid holding in solution the silica and other soluble matters of the straw, together with the soda of the originalsolution. This soda I reproduce in the following manner: The refuse liquor I first raise to the boilingpoint,with milk of limeadded in the proportion of two ounces of lime to one gallon of the This solution I boil for about thirty minutes, and then pass it through a filter consisting of alternate layers of caustic lime and coarse charcoal powder. This will purify the liquor sufiiciently for further use; but the gradual accumulation of wholly removed by this treatment makes it necessary finally to adopt a more thorough method of purification. This I accomplish by evaporating the liquor to one-fifthits original. bulk, adding about one per cent. of carbonate of lime, one-fourth of one per-cent. of nitrate of soda, and twenty-five per cent. of sawdust, charcoal powder,peat, or other matter that will act as fuel. This mixture I make up into cakes, which are dried and burned. The resulting impurities which are not ashes consist, principally, of carbonate of soda, which is rendered caustic in the usual manner. The cakes above referred to may be used as I fuel to evaporate other portionsof the liquor.
The advantages resulting from my invention are, first, by an immediate mechanical subdivision of the straw or other vegetablesubstance by grinding itin the incipient stages of the alkaline action the of surface is exposed at once to the chemical action of the solvent, thus saving many hours time, and obviating, Ithink, entirely the necessity of high pressure, or a temperature above the boiling-point of the solution, so that an open tank may be used in the process instead of a tight boiler, though experience may show it to be expedient to use a close vessel with more or less pressure; second, the material being most thoroughly reduced to its ultimate fiber by this process, the pulp may be bleached more readily and at less expense than hitherto; third, the time of treatment is so short and the temperature so not weakened as in other processes; fourth,
greatest possible amount low that the cellulose is 4 all the alkali, except avery small percentage,
is saved, thus economizing what has hitherto been mostly a. waste material.
Having now described the manner of making, applying, and practicing my invention, I claim and desire to secure by Letters Patent- 1. Preparing paper-pulp from straw or other substances by subjecting it to a mechanical reduction, as described, commencing with the early stages of the treatment with the chemical solvent, and continuing the said mechanical reduction in connection with the chemical solvent, in the manner and for the purpose described.
2. Purifying the alkali held in solution in the refuse liquor by passing it through afilter, constructed substantially as above described,
sufficiently to enable me to use it again, and
completely reproducing it, when necessary, by making it into combustible cakes, as set forth.
ASAHEL K. EATON. WVitn esses AMos BRQADNAX, V. R. HoLBRooK.
Family
ID=
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| GB1582479A (en) | Process for the production of xylan | |
| USRE4203E (en) | Improvement in the manufacture of paper-pulp from straw | |
| CN110669153B (en) | Method for extracting agar from gracilaria | |
| JPS6036329A (en) | Processing method for liquid used in the causticizing cycle of the Kraft process | |
| US1876522A (en) | Becoveby of by-products of sugab extraction | |
| CN114645478B (en) | Preparation method of refined cotton and cellulose ether | |
| US430516A (en) | Hermann endemann | |
| US41982A (en) | Improvement in the manufacture of paper-pulp from straw | |
| US1052675A (en) | Process of making cellulose. | |
| US2082656A (en) | Process of purification of sugar solutions | |
| US967001A (en) | Process of manufacturing cellulose. | |
| JP3467754B2 (en) | Pulp fiber manufacturing method | |
| US1670156A (en) | Method for cooking wood to form chemical paper stock | |
| US1581671A (en) | Production of pulp and other products from wood | |
| US1780750A (en) | Method of preparing cellulose pulp | |
| US1630147A (en) | Process for extracting the pure cellulose from the bagasse of sugar cane | |
| US1936806A (en) | Process of making strontium carbonate | |
| US1213545A (en) | Method of extracting and modifying proteins or albuminous matter. | |
| SU416384A1 (en) | ||
| US695474A (en) | Process of extracting oil from cotton-seed. | |
| US108487A (en) | Improvement in the manufacture of paper-stock | |
| US1298481A (en) | Process for the treatment of waste soda liquors. | |
| US2031239A (en) | Process for the utilization of sugarcane bagasse | |
| US1792202A (en) | Process for treating the bagasse of sugar cane | |
| US1778199A (en) | Manufacture of pulp |