US348165A - And frank a - Google Patents
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- Publication number
- US348165A US348165A US348165DA US348165A US 348165 A US348165 A US 348165A US 348165D A US348165D A US 348165DA US 348165 A US348165 A US 348165A
- Authority
- US
- United States
- Prior art keywords
- fibers
- chlorine
- bleaching
- pulp
- wood 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
- 239000000835 fiber Substances 0.000 description 58
- 238000000034 method Methods 0.000 description 48
- 229920001131 Pulp (paper) Polymers 0.000 description 34
- 238000004061 bleaching Methods 0.000 description 28
- 239000000460 chlorine Substances 0.000 description 28
- 229910052801 chlorine Inorganic materials 0.000 description 28
- ZAMOUSCENKQFHK-UHFFFAOYSA-N chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 24
- 239000000839 emulsion Substances 0.000 description 22
- 239000000243 solution Substances 0.000 description 20
- 235000013311 vegetables Nutrition 0.000 description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 18
- 239000007844 bleaching agent Substances 0.000 description 16
- ZKQDCIXGCQPQNV-UHFFFAOYSA-N Calcium hypochlorite Chemical compound [Ca+2].Cl[O-].Cl[O-] ZKQDCIXGCQPQNV-UHFFFAOYSA-N 0.000 description 14
- 239000007800 oxidant agent Substances 0.000 description 14
- 239000002253 acid Substances 0.000 description 12
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 10
- 150000001447 alkali salts Chemical class 0.000 description 8
- KZBUYRJDOAKODT-UHFFFAOYSA-N chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 8
- 239000004615 ingredient Substances 0.000 description 8
- 239000002480 mineral oil Substances 0.000 description 8
- 235000010446 mineral oil Nutrition 0.000 description 8
- 239000000126 substance Substances 0.000 description 8
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate dianion Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 230000000266 injurious Effects 0.000 description 6
- MUBZPKHOEPUJKR-UHFFFAOYSA-N oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 6
- 239000003208 petroleum Substances 0.000 description 6
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 6
- 239000011780 sodium chloride Substances 0.000 description 6
- 235000002639 sodium chloride Nutrition 0.000 description 6
- HCHKCACWOHOZIP-UHFFFAOYSA-N zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 6
- 239000011701 zinc Substances 0.000 description 6
- 229910052725 zinc Inorganic materials 0.000 description 6
- UIIMBOGNXHQVGW-UHFFFAOYSA-M NaHCO3 Chemical class [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 239000002585 base Substances 0.000 description 4
- 238000009835 boiling Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 230000002349 favourable Effects 0.000 description 4
- 159000000011 group IA salts Chemical class 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000003921 oil Substances 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000002023 wood Substances 0.000 description 4
- -1 5o rags Polymers 0.000 description 2
- 241000019173 Antichloris Species 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000011777 Corchorus aestuans Nutrition 0.000 description 2
- 240000000491 Corchorus aestuans Species 0.000 description 2
- 235000010862 Corchorus capsularis Nutrition 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 2
- WQYVRQLZKVEZGA-UHFFFAOYSA-N Hypochlorite Chemical group Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 2
- 235000004431 Linum usitatissimum Nutrition 0.000 description 2
- 240000006240 Linum usitatissimum Species 0.000 description 2
- 235000015450 Tilia cordata Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 229920002522 Wood fibre Polymers 0.000 description 2
- 240000008042 Zea mays Species 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 230000001476 alcoholic Effects 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium monoxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 150000001805 chlorine compounds Chemical class 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 239000003086 colorant Substances 0.000 description 2
- 235000005822 corn Nutrition 0.000 description 2
- 235000005824 corn Nutrition 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000010348 incorporation Methods 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 230000001264 neutralization Effects 0.000 description 2
- 230000003472 neutralizing Effects 0.000 description 2
- 235000006408 oxalic acid Nutrition 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000001590 oxidative Effects 0.000 description 2
- 159000000001 potassium salts Chemical class 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 235000019345 sodium thiosulphate Nutrition 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-N sulfonic acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000002025 wood fiber Substances 0.000 description 2
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
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/1026—Other features in bleaching processes
- D21C9/1036—Use of compounds accelerating or improving the efficiency of the processes
Definitions
- Our invention consists in an improved pror cess of bleaching wood fibers which have been reduced to pulp by mechanical means, and other raw vegetable fibers, for the purpose of manufacturing paper therefrom. Hitherto these fibers have not been extensively used for this purpose, both because of previous inability to bleach them and on account of their hardness and brittleness.
- our improved process the fibers are quickly and economically bleached without materially injuring the most delicate fibers, and at the same time are rendered soft and pliable.
- chloride of lime or water saturated with chlorine not only refuses to bleach mechanically-separated wood or vegetable fibers, but, on the contrary, produces intense colors; and strong acids turn mechanically-prepared wood pulp or raw vegetable fibers red in the sunlight, and often without sunlight in the presence of moisture, and the slightest trace of iron contained in any of the materials or vehicles employed in the bleaching, as in the water or lime, is sufficient to blacken the entire mass in a very short time.
- the object of our invention is to bleach to a pure white mechanically-prepared wood pulp and other raw vegetable fibers, and to obtain the same in a soft and pliable condition and without the application of heat.
- Ourimproved process achieves this result in a practical, feasible, economical, and efficient man- 7c ner.
- the usual beaterengine of the paper-mill is preferably em 'ployed, and water is introduced into it in sufficient quantity to carry out the processsay enough to fill the engine about half full.
- An emulsion is then introduced into the water in the engine, consisting of a mineral oil and a basic alkali or alkaline salt or solution thereof.
- oxidizing agents preferably oxidizing agents, and may therefore be termed alkaline oxidizing agents.
- the mineral oilemployed is preferably petroleum or other oil obtained from the distillation of coal, and the alkaline oxidizing agent is preferably chloride of lime,or caustic lime and chlorine solution.
- Proper proportions of the ingredients of the emulsion are as follows: Four (4) pounds of petroleum and six (6) pounds of chloride of lime to each one 0 hundred pounds, dry weight, of the wood pulp or other fiber. After the emulsion has been added to the water and diluted thereby the wood pulp or other fiber is then introduced into the engine. The entire mass is then thor- 9 5 oughly agitated until the emulsion is brought into uniform and intimate contact with the fibers throughout.
- the emulsion acts as a favorable 10o solvent of the resinous and gummy materials which incrust the raw fibers in smallquantities, and as the operation advances it distinctly betrays its action on the fibers by as suming a slight but evident alcoholic and acetic odor.
- the wood pulp on becoming saturated by this solution loses its hardness and woody characteristics and becomes soft and pliable equally, as in the'case of chemicallyisolated fibers or rag-stock.
- the coloring-matter existing in the sap substances of the wood stuff is fully brought out, and is then bleached pure white by the following treatment:
- the wood pulp under treatment being now saturated with the emulsion dilute in water, three to four (3 to 4) pounds of corn inon salt (sodium chloride) in solution are added to each one hundred (100) pounds, dry weight, of the pulp or fiber.
- This solution being capable of dissolving a large quantity of chlorine gas,thus prevents any possible escape of the same,which otherwise would expand and escape into the air, it being set free by the warmth which is evolved by the process of bleaching.
- a small quantity of sulphate of zincsay two (2) to three (3) pounds to each one hundred pounds of the pulp may be advantageouslysubstituted as an equivalent thereof.
- the sulphate of zinc acts very energetically to decompose the chlorides, and thus liberate the chlorine, and if the water originally introduced into the engine at the beginning of the process be warm (say from forty (40) to fifty ccntigrade) on the completion of the process the pulp is left in so nearly a neutral state that little or no anti-chlorine is required, since there is at the conclusion little or no excess of chlorine.
- the nextstage in the process consists in the introduction into the mass of chloride of lime, chlorine gas, or water saturated with chlorine gas, together with a natron salt; or a potassium salt may be substituted for the natron salt.
- the carbonate or sulphate of one of these bases is to be preferred.
- the proper proportions of these ingredients to each one hundred pounds of pulp orfiber would be between thirty (30) and forty (40) pounds of the chloride, depending on its strength, and between twelve (12) and fifteen (15) pounds of the alkali carbonate or-sulphate.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Paper (AREA)
Description
UNITED STATES PATENT OFFICE.
JOHN A. JUST, OF NEW YORK, AND FRANK A. FLETCHER AND CALLIE F. GIBBS, OF NVATERTONVN, N. Y.; SAID JUST AND GIBBS ASSIGNORS TO SAID FLETCHER.
PROCESS OF BLEACHING MECHANICAL WOOD PULP AND OTHER RAW VEGETABLE FIBERS FOR THE PURPOSE OF MANUFACTURING PAPER. E
FBPECIPICATION forming part of Letters Patent No. 348,165, dated August 24, 1886.
Application filed October 9, 1885. Serial No. 179,430. No specimens) To all whom it may concern:
Be it known that we, JOHN A. JUST, a citizen of Germany, and a resident of the city, county, and State of New York, and FRANK 5 A. FLETCHER and CALLIE F. GIBBS, both citizens of the United States, and residents of WVatertown, in the county of Jefferson and State of New York, have invented a new and Improved Process of Bleaching Mechanically- Prepared Vood Pulp and other Raw Vegetable Fibers; and we do hereby declare the following to be'a full and exact description thereof.
Our invention consists in an improved pror cess of bleaching wood fibers which have been reduced to pulp by mechanical means, and other raw vegetable fibers, for the purpose of manufacturing paper therefrom. Hitherto these fibers have not been extensively used for this purpose, both because of previous inability to bleach them and on account of their hardness and brittleness. By our improved process the fibers are quickly and economically bleached without materially injuring the most delicate fibers, and at the same time are rendered soft and pliable. In the processes hitherto tried, and in which heating or boiling has been resorted to, chlorine, which is always contained in the bleaching agent, is left 3c insol'ution in the water in such quantities as to render the atmosphere very injurious to the health of the workmen and others who chance to inhale it, on account of the irrespirable character of chlorine .gas. Substances 3 5 containing chlorine are also used in our process; but since it is conducted without any heating or boiling all possible escapeof chlo-' rine is prevented, and no injurious effects result from its practice.
The old and well-known process which has hitherto been used in endeavoring to bleach wood pulp consists in preparing oxygen and applying the same, the oxygen being evolved by heating a metallic oxide in a clear solution of chloride of lime. This process, however,
fails to bleach raw vegetable fibers and mechanically-prepared wood pulp, although it does bleach all chemically-isolated fibers, such as unbleached chemically-prepared wood pulp, 5o rags, cotton, and wastes of the same.
It has long been known that chloride of lime or water saturated with chlorine not only refuses to bleach mechanically-separated wood or vegetable fibers, but, on the contrary, produces intense colors; and strong acids turn mechanically-prepared wood pulp or raw vegetable fibers red in the sunlight, and often without sunlight in the presence of moisture, and the slightest trace of iron contained in any of the materials or vehicles employed in the bleaching, as in the water or lime, is sufficient to blacken the entire mass in a very short time.
The object of our invention is to bleach to a pure white mechanically-prepared wood pulp and other raw vegetable fibers, and to obtain the same in a soft and pliable condition and without the application of heat. Ourimproved process achieves this result in a practical, feasible, economical, and efficient man- 7c ner.
In carrying out our process the usual beaterengine of the paper-mill is preferably em 'ployed, and water is introduced into it in sufficient quantity to carry out the processsay enough to fill the engine about half full. An emulsion is then introduced into the water in the engine, consisting of a mineral oil and a basic alkali or alkaline salt or solution thereof. These latter principles are at the same time preferably oxidizing agents, and may therefore be termed alkaline oxidizing agents. The mineral oilemployed is preferably petroleum or other oil obtained from the distillation of coal, and the alkaline oxidizing agent is preferably chloride of lime,or caustic lime and chlorine solution. Proper proportions of the ingredients of the emulsion are as follows: Four (4) pounds of petroleum and six (6) pounds of chloride of lime to each one 0 hundred pounds, dry weight, of the wood pulp or other fiber. After the emulsion has been added to the water and diluted thereby the wood pulp or other fiber is then introduced into the engine. The entire mass is then thor- 9 5 oughly agitated until the emulsion is brought into uniform and intimate contact with the fibers throughout. The oily nature of the oil having disappeared in the preparation of the emulsion, the emulsion acts as a favorable 10o solvent of the resinous and gummy materials which incrust the raw fibers in smallquantities, and as the operation advances it distinctly betrays its action on the fibers by as suming a slight but evident alcoholic and acetic odor. The wood pulp on becoming saturated by this solution loses its hardness and woody characteristics and becomes soft and pliable equally, as in the'case of chemicallyisolated fibers or rag-stock. With the aid of chlorine or any oxidizing or deoxidizin g agent present at this stage of the process, the coloring-matter existing in the sap substances of the wood stuff is fully brought out, and is then bleached pure white by the following treatment: The wood pulp under treatment being now saturated with the emulsion dilute in water, three to four (3 to 4) pounds of corn inon salt (sodium chloride) in solution are added to each one hundred (100) pounds, dry weight, of the pulp or fiber. This solution being capable of dissolving a large quantity of chlorine gas,thus prevents any possible escape of the same,which otherwise would expand and escape into the air, it being set free by the warmth which is evolved by the process of bleaching. Thus not only is no chlorine lost, but injurious effects to the workmen are avoided, since the chlorine is not mechanically suspended in the mass, but is held dissolved in the dilute salt solution, and from that is abstracted as fast as required, to oxidize in the process of bleaching. To accelerate the process of bleaching, a small quantity of acid, either vegetable or mineral-such as oxalic acid, for examp1emay be added, thus neutralizing alkaline principles favorable to oxidation. In bleaching some fiberssuch as flax and jute, for example-the acid will be found necessary, but with the wood pulp is not absolutely essential, although preferable. The proportion of acid which is properly used is three-quarters of a pound to each one hundred pounds of the fiber.
Instead of using an acid for the purpose of accelerating the process, a small quantity of sulphate of zincsay two (2) to three (3) pounds to each one hundred pounds of the pulpmay be advantageouslysubstituted as an equivalent thereof. The sulphate of zinc acts very energetically to decompose the chlorides, and thus liberate the chlorine, and if the water originally introduced into the engine at the beginning of the process be warm (say from forty (40) to fifty ccntigrade) on the completion of the process the pulp is left in so nearly a neutral state that little or no anti-chlorine is required, since there is at the conclusion little or no excess of chlorine.
The nextstage in the process consists in the introduction into the mass of chloride of lime, chlorine gas, or water saturated with chlorine gas, together with a natron salt; or a potassium salt may be substituted for the natron salt. The carbonate or sulphate of one of these bases is to be preferred. The proper proportions of these ingredients to each one hundred pounds of pulp orfiber would be between thirty (30) and forty (40) pounds of the chloride, depending on its strength, and between twelve (12) and fifteen (15) pounds of the alkali carbonate or-sulphate. Upon the incorporation of these substances with the mass by agitation in the beater'engine the wood pulp or other fiber is bleached permanently and perfectly white, owing to the decomposition of the hypochlorites formed with the above-mentioned bases. After the bleaching is completed any excess of chlorine is removed by an anti-chlorine substancesuch as sodium hyposulphite or sulphurous-acid solution, for example-and the product is washed, and is then ready for being made into paper.
In case sulphate of zinc has been used to ac eelerate the process, there will usually be no necessity for the use of anti-chlori ne, and hence the washing may be dispensed with, since wash' ing is only essential to preveutbrownish tints being given to the pulp by the anti-chlorines.
In carrying out our invention, in practice we employ a beating-engine which will manipulate about five hundred pounds of the pulp or fiber. The steps of the process carried out with the preferred ingredients are then as follows: First, the emulsion composed of petroleum and chloride of lime is introduced; second, common saltis added; third, an acid or sulphate of zinc is introduced; fourth, chloride of lime and carbonate of soda are introduced. After the introduction of each ingredient the entire mass is thoroughly agitated, so as to subject every portion'of the mass to the action of the substances used.
We claim as our inveution-- 1. In the process of bleaching wood pulp and other fibers, treating the pulp or fiber,for the purpose of softening the same, with an emulsion composed of a mineral oil anda basic alkali, or alkaline salt or solution thercofisubstantially as set forth.
2. In the process of bleaching wood pulp and other fibers, treating the pulp or fiber,for the purpose of softening the same, with an emulsion composed of a mineral oil and an alkaline oxidizing agent, substantially as set forth.
3. In the process of bleaching wood pulp and other fibers in which chlorine gas is evolved, introducing a solution of common salt, substantially as set forth, whereby the free chlorine is dissolved and its escape into the air prevented.
4. In the process of bleaching wood pulp and other fibers which have by previous stages been reduced to a soft and pliable condition, treating the same with an oxidizing agent,together with an alkali basic salt, substantially as set forth.
5. The process of bleaching mechanicallyprepared wood pulp and other raw vegetable fibers,consisting of the following steps: First, treating the pulp or fibers with an emulsion composed of a mineral oil and an alkaline oxidizing agent; second, addingasolution of coming product with an oxidizing or bleaching agent, together with a basic alkali salt, or solution thereof, substantially as set forth. I 5
' In testimony whereof we affix our signatures in presence of two witnesses.
JOHN A. JUST. FRANK A. FLETCHER. OALLIE F. GIBBS.
Witnesses:
GEO. H. WALKER, O. L. ADAMS.
Publications (1)
Publication Number | Publication Date |
---|---|
US348165A true US348165A (en) | 1886-08-24 |
Family
ID=2417233
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US348165D Expired - Lifetime US348165A (en) | And frank a |
Country Status (1)
Country | Link |
---|---|
US (1) | US348165A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2474034A (en) * | 1946-12-04 | 1949-06-21 | Paper Patents Co | Bleaching poplar groundwood |
-
0
- US US348165D patent/US348165A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2474034A (en) * | 1946-12-04 | 1949-06-21 | Paper Patents Co | Bleaching poplar groundwood |
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