US150111A - Improvement in processes of reducing wood to paper-pulp - Google Patents
Improvement in processes of reducing wood to paper-pulp Download PDFInfo
- Publication number
- US150111A US150111A US150111DA US150111A US 150111 A US150111 A US 150111A US 150111D A US150111D A US 150111DA US 150111 A US150111 A US 150111A
- Authority
- US
- United States
- Prior art keywords
- wood
- steaming
- steam
- vessel
- 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
- 239000002023 wood Substances 0.000 title description 68
- 229920001131 Pulp (paper) Polymers 0.000 title description 12
- 238000000034 method Methods 0.000 title description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 84
- 235000011121 sodium hydroxide Nutrition 0.000 description 36
- 238000010025 steaming Methods 0.000 description 36
- 239000002253 acid Substances 0.000 description 12
- 238000000227 grinding Methods 0.000 description 12
- 239000000126 substance Substances 0.000 description 12
- 238000004519 manufacturing process Methods 0.000 description 8
- 239000000463 material Substances 0.000 description 8
- 239000007844 bleaching agent Substances 0.000 description 6
- 229920002678 cellulose Polymers 0.000 description 6
- 239000001913 cellulose Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000007788 liquid Substances 0.000 description 6
- 239000011148 porous material Substances 0.000 description 6
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- 239000002351 wastewater Substances 0.000 description 6
- 239000003513 alkali Substances 0.000 description 4
- 229910052801 chlorine Inorganic materials 0.000 description 4
- 239000000460 chlorine Substances 0.000 description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 4
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- RTZKZFJDLAIYFH-UHFFFAOYSA-N diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000009423 ventilation Methods 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- AXCZMVOFGPJBDE-UHFFFAOYSA-L Calcium hydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 2
- 210000001035 Gastrointestinal Tract Anatomy 0.000 description 2
- 206010022114 Injury Diseases 0.000 description 2
- 241000779819 Syncarpia glomulifera Species 0.000 description 2
- 229940036248 Turpentine Drugs 0.000 description 2
- 201000011452 adrenoleukodystrophy Diseases 0.000 description 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 235000011116 calcium hydroxide Nutrition 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000003518 caustics Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000000875 corresponding Effects 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000009950 felting Methods 0.000 description 2
- 239000002657 fibrous material Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000014509 gene expression Effects 0.000 description 2
- 230000005443 grand unified theory Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 230000000149 penetrating Effects 0.000 description 2
- 239000001739 pinus spp. Substances 0.000 description 2
- 235000011118 potassium hydroxide Nutrition 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
- 235000015096 spirit Nutrition 0.000 description 2
- UCKMPCXJQFINFW-UHFFFAOYSA-N sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 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
- D21C1/00—Pretreatment of the finely-divided materials before digesting
- D21C1/02—Pretreatment of the finely-divided materials before digesting with water or steam
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S162/00—Paper making and fiber liberation
- Y10S162/02—Chip soaking
Definitions
- HEINRICH VOELTER OF HEIDENHEIM ON THE BRENZ, AND OS'WALD MEYH, OF ZWIGKAU, GERMANY.
- the vessel for steaming can be made of any convenient shape and size. It must, however, be of sufficient strength to stand the necessary pressure of steam. It may also be fitted on a suitable part of it with one or more man-holes, for the purpose of fillin g and emptying it of the material to be treated; and it may be fitted on some convenient place of it with a pipe connecting it with the steam generating apparatus or steamboiler, from which, by means of a cock fitted to this pipe, the necessary steam can be passed into it or shut off, as required. It may be joined, if possible, on its lowest place, with another pipe provided with a cock to enable a person to draw the waste-water off, which results from the condensation of the steam inside the vessel during the steaming operation.
- This water will be found to contain extractive substances; and, lastly, if the steaming-vessel is of weaker construction than the steam-generating vessel, it should be fitted with a steamgage and safety-valve. In some cases it will be necessary to fit a so called false perforated bottom into the steaming-vessel, above the waste-water pipe. Should the materials to be steamed be in small pieces this must be done.
- the steaming-vessel fitted up with the generally well-known mountings enumerated before, can be made of any convenient shape, and of any capacity, as may be required for working, but it must be constructed of sufficient strength to stand the pressure of steam. It may be made (to use the expressions in vogue among steam-boiler makers) horizontal or vertical, or generally like a rag-boiler heated by steam, as they are used in various forms in paper manufactories.
- the boiler may or may not be made to rotate during the steaming operation, as required. In some cases rotation will be found to act injuriously on the material to be steamed, on account of its preventing the extractive matter from being blown off when necessary.
- the steaming vessel and the steam-generating vessel may be constructed, so to speak, of one piece.
- the steaming-vessel has to be sufficiently high, and fitted with an intermediate bottom about twenty inches above the intended highest water-level; also, fitted with a false bottom at some distance above the other bottom, both compartments to communicate by a pipe through which the steam is admitted to the steaming-compartment.
- the admission of steam should be regulated by a cock placed outside the vessel and fitted to this pipe.
- apertures of larger or smaller size ought to be constructed on opposite sides of the vessel, such apertures being shut tight during the steaming operation, but opened afterward for the purpose of creating a draft of air to carry the acid vapors ofl'.
- the caustic-soda lye For the purpose of increasing the dissolving powers of the caustic-soda lye, or other similar liquids, they may be heated by the admission of steam under a pressure of several atmospheres. After the wood has been thus left in contact with the hot lye sufiicient time, the steam is to be shut off.
- the lye which can be used repeatedly again for the same purpose, is run out, and by ventilation of the steaming-vessel, as described before, by means of a draft of air, the remaining vapors contained in the steaming-vessel are removed.
- the wood will be found new to be thoroughly impregnated with lye, and as it is heated above 100, according to the steam-pressure employed, the ventilation effects a considerable concentration of the lye still adhering to it, which is of great advantage, as therebythe lyeing operation can be carried out from the beginning with very diluted lyes and with a smaller quantity of caustic soda.
- the pieces of wood saturated, as they are, with caustic soda-lye, or other kinds of lye used, are now either to be removed out of the vessel, to be converted into wood pulp by the grinding machineryand simultaneous washing, or else they are to be steamed again, as described before.
- the washing of the wood is effected of itself, and the resulting produce is a brown-colored cellulose, which can now be bleached by chlorine, &c.
- the wood which has been thus freed of its incrustating substances, may be exposed in large or small pieces to the action of bleaching-agents, which can be applied either as vapors or gases by charging high-pressed steam with chlorine or in the liquid form as solution of bleaching-powder.
- bleaching-agents which can be applied either as vapors or gases by charging high-pressed steam with chlorine or in the liquid form as solution of bleaching-powder.
Landscapes
- Chemical And Physical Treatments For Wood And The Like (AREA)
- Paper (AREA)
Description
UNITED STATES PATENT QFFICE.
HEINRICH VOELTER, OF HEIDENHEIM ON THE BRENZ, AND OS'WALD MEYH, OF ZWIGKAU, GERMANY.
IMPROVEMENT IN PROCESSES OF REDUCING WOOD TO PAPER-PULP.
Specification forming part of Letters Patent No. 150,111, dated April 21, 1674; application filed October 31, 1873.
To all whom it may concern:
Be it known that we, HEINRICH VoELrER, of Heidenheim on the Brenz, Kingdom of WViirtemburg, Germany, and OSW'ALD MEYH, of Zwickau, Kingdom of Saxony, Germany, paper manufacturers, do hereby declare that we have made an invention of a new method of or process for preparing wood, or Various other fibrous materials of like nature, so as to render such useful in the manufacture of paper-pulp, or for various other purposes, of which the following is a specification:
The main features of our process are described as follows: We take pieces of wood of the same shape, size, and condition in which they. are fed into the grinding apparatus in the well-known so-called wood-grinding mills, and expose them in a close vessel made of suitable material and strength, during one or many hours, to the action of saturated steam of a tension of forty-five to sixty pounds per square inch pressure, and to the action of the temperatures corresponding to these pressures. After such treatment and renewal of the acid by alkaline matter or matters, as hereinafter described, we grind the pieces of wood into pulp, as is usually done.
By the steam penetrating through all the pores of the wood, many of those substances contained in it, which are generally called i11- crustating substances, are dissolved, whereby it gets opened out, and a considerable loosening of its structure is effected, so much so that, after grinding it and passing the ground stuff through a good refiner and sorting apparatus, a surprisingly tough, but rather more or less brownish-looking, paper-pulp is obtained, of great felting capability, out of which, particu larly when fir-wood has been used, paper of good quality, and boards, can be manufactured without the addition of any rag-pulp. For the production of this pulp very much less driving-power is required than for the production of an equal quantity of pulp from wood which has not passed the preliminary steaming operation. The vessel for steaming can be made of any convenient shape and size. It must, however, be of sufficient strength to stand the necessary pressure of steam. It may also be fitted on a suitable part of it with one or more man-holes, for the purpose of fillin g and emptying it of the material to be treated; and it may be fitted on some convenient place of it with a pipe connecting it with the steam generating apparatus or steamboiler, from which, by means of a cock fitted to this pipe, the necessary steam can be passed into it or shut off, as required. It may be joined, if possible, on its lowest place, with another pipe provided with a cock to enable a person to draw the waste-water off, which results from the condensation of the steam inside the vessel during the steaming operation. This water will be found to contain extractive substances; and, lastly, if the steaming-vessel is of weaker construction than the steam-generating vessel, it should be fitted with a steamgage and safety-valve. In some cases it will be necessary to fit a so called false perforated bottom into the steaming-vessel, above the waste-water pipe. Should the materials to be steamed be in small pieces this must be done.
As mentioned above, the steaming-vessel, fitted up with the generally well-known mountings enumerated before, can be made of any convenient shape, and of any capacity, as may be required for working, but it must be constructed of sufficient strength to stand the pressure of steam. It may be made (to use the expressions in vogue among steam-boiler makers) horizontal or vertical, or generally like a rag-boiler heated by steam, as they are used in various forms in paper manufactories. In case a rotating steam-boiler is used as steaming-vessel, or a so-called Donkin rag-boiler, which is fitted inside with a perforated rotating drum, into which the wood to be steamed is put, and where the outside shell is stationary during the rotations of the drum, the boiler may or may not be made to rotate during the steaming operation, as required. In some cases rotation will be found to act injuriously on the material to be steamed, on account of its preventing the extractive matter from being blown off when necessary.
Should it be desirable to do so, the steaming vessel and the steam-generating vessel may be constructed, so to speak, of one piece.
In this case the steaming-vessel has to be sufficiently high, and fitted with an intermediate bottom about twenty inches above the intended highest water-level; also, fitted with a false bottom at some distance above the other bottom, both compartments to communicate by a pipe through which the steam is admitted to the steaming-compartment. The admission of steam should be regulated by a cock placed outside the vessel and fitted to this pipe. After blowing off the steam, on the steaming operation being finished, either into another vessel or into the atmosphere, it will be found to be necessary to carry off the acid vapors left in the steaming-vessel, which have been generated during the steaming operation, as these would condense on the cooling, but still hot, sides of the vessel, and, as it is generally made of iron, would corrode it, and color or do injury to the wood. Furthermore, by getting rid of the acid vapors less alkali will be subsequently required in the process.
For this purpose apertures of larger or smaller size, as may be required, ought to be constructed on opposite sides of the vessel, such apertures being shut tight during the steaming operation, but opened afterward for the purpose of creating a draft of air to carry the acid vapors ofl'.
After a great part of the incrustations of the wood have been thus dissolved by the vigorous action of the steam, we next subject the steamed wood in the vessel to the action of one or more weak solutions of caustic soda or caustic potash, or only milk of lime, which exercise an important influence on the incrustations still remaining on the cellulose of the wood. These lyes act by imparting to the wood in a heightened degree those qualities which have been mentioned before as being essential to a good paper-pulp. By this further treatment a superior pulp is obtained from wood than is obtained by steaming alone, although it is more costly to produce.
lVe will further mention here that, according to our experience, wood, be it in large or. small pieces, after its structure has been loosened by the steaming operation, can be converted easily, .by subsequent treatment with other dissolving agents, into bleachable cellulose. The manner of effecting this is de scribed in the following paragraph. It can also be applied to wood which it is not re quired to bleach.
The effect of steaming the wood with highpressure steam is not only to loosen its structure to a considerable degree, but also to expel the air contained in the steaming-vessel and in the pores of the wood. This state of absence of air can be used to bring the dissolving-liquid-ibr instance, caustic-soda lye of proper construction-in unfailing contact with the innermost portions of the wood. This is done by shutting, after the steaming operation is finished, the steam-admission cock and the waste-water cock; then opening a third cock, which, by a pipe, communicates with a vessel of somewhat larger cubic contents than the steaming apparatus is, and
which is filled with hot or cold caustic-soda lye. As the outward atmosphere is gradually cooling the steamingvessel, the volume of the steam inside of itis reduced, and in consequence of this the caustic-soda lye flows over into the steaming-vessel, where it efl'ects the condensation of the steam and produces a vacuum, which is filled up as soon as formed by more lye flowing over. Directly the temperature of the soda-lye sinks below the boiling-point, the remaining steam becomes totally condensed, and through the vacuum obtained thereby the liquid is drawn into the innermost pores of the wood, which, by steaming,had been very much loosened in structure beforehand. For the purpose of increasing the dissolving powers of the caustic-soda lye, or other similar liquids, they may be heated by the admission of steam under a pressure of several atmospheres. After the wood has been thus left in contact with the hot lye sufiicient time, the steam is to be shut off. The lye, which can be used repeatedly again for the same purpose, is run out, and by ventilation of the steaming-vessel, as described before, by means of a draft of air, the remaining vapors contained in the steaming-vessel are removed. The wood will be found new to be thoroughly impregnated with lye, and as it is heated above 100, according to the steam-pressure employed, the ventilation effects a considerable concentration of the lye still adhering to it, which is of great advantage, as therebythe lyeing operation can be carried out from the beginning with very diluted lyes and with a smaller quantity of caustic soda. The pieces of wood saturated, as they are, with caustic soda-lye, or other kinds of lye used, are now either to be removed out of the vessel, to be converted into wood pulp by the grinding machineryand simultaneous washing, or else they are to be steamed again, as described before. By steaming intermittingly the washing of the wood is effected of itself, and the resulting produce is a brown-colored cellulose, which can now be bleached by chlorine, &c.
The wood, which has been thus freed of its incrustating substances, may be exposed in large or small pieces to the action of bleaching-agents, which can be applied either as vapors or gases by charging high-pressed steam with chlorine or in the liquid form as solution of bleaching-powder. Should it be chiefly required to free the wood from these substances which impart to the Wood p'ulp the property to darken after in light, we re commend that it should be treated (without previous steaming,by which more particularly wood from coniferous trees is rendered of a brown color) with the vapors of alcohol, ether, sulphide of carbon, benzine, spirits of turpen tine, &c., whereby those substances are extracted, and a pulp of the original natural color of the wood is produced.
Having now described and particularly as='- certained the nature, utility, and peculiarity of the said inventiomandthe manner inwhich eration, and next treating the steamed wood the same is or may be used, or carried into with alkali, and finally grinding or reducing practical effect, we would remark, in concluthe wood, all as set forth. 7
sion, that we do .not claim simply subjecting wood to the action of steam or steaming it before grinding it but What we claim as our invention is- Witnesses to signature of HEINR.VOELTER: The process, substantially as described, it GUSTAV SGHOLL,
consisting in subjectingthe wood to the action HEINR. GUT.
of steam, as explained, and next separating I Witnesses to signature of OSWALD MEYH: from it, and the Vessel containing it, the acid ABBOTT L. SEELIGMAN, or acid vapors generated by the steaming op- LUDWIG MI'JLLER.
Publications (1)
Publication Number | Publication Date |
---|---|
US150111A true US150111A (en) | 1874-04-21 |
Family
ID=2219524
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US150111D Expired - Lifetime US150111A (en) | Improvement in processes of reducing wood to paper-pulp |
Country Status (1)
Country | Link |
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US (1) | US150111A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2538457A (en) * | 1946-11-02 | 1951-01-16 | Monie S Hudson | Treating wood |
US2583994A (en) * | 1946-06-21 | 1952-01-29 | Rayonier Inc | Wood pulp digestion |
US3013933A (en) * | 1953-01-28 | 1961-12-19 | Rayonier Inc | Method for preparation of wood cellulose |
-
0
- US US150111D patent/US150111A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2583994A (en) * | 1946-06-21 | 1952-01-29 | Rayonier Inc | Wood pulp digestion |
US2538457A (en) * | 1946-11-02 | 1951-01-16 | Monie S Hudson | Treating wood |
US3013933A (en) * | 1953-01-28 | 1961-12-19 | Rayonier Inc | Method for preparation of wood cellulose |
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