Search Images Maps Play YouTube News Gmail Drive More »
Sign in
Screen reader users: click this link for accessible mode. Accessible mode has the same essential features but works better with your reader.

Patents

  1. Advanced Patent Search
Publication numberUS2668110 A
Publication typeGrant
Publication dateFeb 2, 1954
Filing dateJun 18, 1948
Priority dateJun 18, 1948
Publication numberUS 2668110 A, US 2668110A, US-A-2668110, US2668110 A, US2668110A
InventorsAbner Jacobson, Karl Sixt, Spencer Arthur M
Original AssigneeJacobson, Spencer
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Method for fiber liberation in cotton stalks and the pulp
US 2668110 A
Images(2)
Previous page
Next page
Description  (OCR text may contain errors)

Feb. 2, 1954 2,668,110

METHOD FOR FIBER LIBERATION IN COTTON STALKS AND THE PULP Filed June 18, 1948 A. M. SPENCER ETAL 2 Sheets-Sheet l I I I a 3mm ARTHUR M. SPENCER. ABNER JAcoBsoN; KARL SIXT.

Clrforneys.

Feb. 2, 1954 A. M. SPENCER :=:r AL

METHOD FOR FIBER LIBERATION IN COTTON STALKS AND THE PULP Filed June 18, 1948 .2 Sheets-Sheet 2 3mm ARIHUR M. SPENCER. ABNER 'JACOBSON. KARL SlxT. gfi

Patented Feb. 2, 1954 METHOD FOR FIBER LIBERATIQN IN COT- TION STALKS AND THE PULP Arthur M. Spencer, Santa Fe, N. M ex., and Abner Jacobson, Cleveland, and Karl Sixt,S-East Cleveland, Ohio; said 'Sixt assignor to said Spencer and said Jacobson Application June 18, 1948, Serial No. 33,696

4 Elaims. l

The present invention relates to fiber liberation, particularly the treatment of cotton stalk for continuous rapid liberation with minimum breaking of the fiber thereof into useful products, the effective impregnation of the fiber with organic resinous, bituminous or asphaltic materials to the products in free fiber or matted state, and to apparatus for carrying out the process to form such products.

One of the objects of the present invention is to provide an improved process of digestion of the fiber, particularly cotton stalk fiber, whereby the lignin is rapidly and continuously softened and partially removed and/or softened with .a Wetting agent containing a minimum of alkaline chemical tending to degrade the fiber.

Another object is to provide an improved rapid digestive process for softening without degradation of the fiber.

Another object is to provide, improved fiber liberation, without destruction of the .fiber by cutting, tearing and abrasion, by beating of the digested stalks in a whipping type beater to separate fiber bundles into individual fibers.

Another object .is to treat the pulp with emulsified organic materials such as resins, waxes, bitumen and asphalt to obtain by coagulation of the emulsion in situ .on the fiber a homogeneous distribution and coating thereof.

Another object is to produce improved impreghated moistureproofed matted fibrous products of cotton stalk fiber.

Another object is to provide improved apparatus to carry out the process herein and form th improved products.

Other objects will be inherent in the following description of the invention.

Cotton stalk fiber has not been successfully marketed as commercial mat-ted fiber products, such as wall board, insulation, roofing paper, felt, boxboard, rug liners and other paper type products because prior processes applied thereto, similar to treatment of wood tended to degrade the fiber both chemically and mechanically in treatments too {drastic for the requirements of this fiber and too expensive to compete with other fiber sources.

. The present process at merely softening the lignin without complete removal thereof and without degradation of the cellulose, and separation of the long fiber from the stalk bundles without mechanical destruction or breakingfzinto slmrt fibers in a rapid, continuous and economi,

caimanner,

to thepresentzinveution, cotton stalk fiber is digestively softened in the presence of a wetting agent in water primarily adapted to penetrate and loosen the fiber from a normal coating of natural waxes, gums and some of the lignin. The water may also contain a small guantity of alkali which effects some chemical hydrolysis of the naturalfiber, but it is preferred to omit alkali and to effect digestive softening with only aqueous wetting agent. Without 'alkaii, some hydration of the cellulose may take place during the digestive softening; however, the present processing of the fiber in total'treate ment is effected relatively rapidly, so that the final character of the fiber appears to indicate that the primary action of the treatment a softening of the natural fiber binder and relate tively lesser degrees of hydration and, in the presence of dilute alkali, hydrolysis occurs in the treatment. It will be understood that the term digestive softening" used herein is intended to indicate such primary softening action and par tial removal of natural binder substance with secondary, if any, hydration or hydrolysis effects on the fiber. I

As wetting agent, we prefer products which have high surface activity as well as good solvent and dispersing action upon the water insoluble natural waxes, gums and lignins associated with the cotton stalk. In general, the wetting agents are fatty derivatives. Secondary, fatty alcohol sulfonation products, esters of fatty alcohols with dibasic acids, and 'alkyl derivatives of aryl sul fonates and condensates of fatty acids and alcohols with alkyilene oxides, are preferred types. Such wetting agents commonly available as Tergitol, Taxad and sodium lauryl vsulfonate .are suitable. Other common wetting .egents, prefer.- ably. sulfonated types, such as sodium, potassium, ammonium, triethanol amine, piperidine or morpholine salts ,of sulfated ,octyl, decyl, dodecyl, tetradecyl, hexadecyl and octadecyl, primary or secondary alcohols, may be used For specific description .of the process and apparatus, reference is made to the drawings herein, wherein:

Figure 1 shows a general layout of apparatus elements; I

Figure 2 is a vertical sectional view of the digester;

Figure 3 is a side elevational view of the digester with parts broken away to show'in-ternal construction taken on the line 3-3 of Figure .2;

Figure 4 is a horizontal sectional view of the digester on the line 4-- |"-o;f Figure 2, locking the direction of the arrows.

Cotton stalk with or without bolls but without roots and generally without leaves, partially dried from field or other storage, is chopped into suitable lengths and conveyed, preferably in an air conveyor (or other type of conveyor), through duct ill into the suction of blower ll. Water containing .1 to 5% of wetting agent, such as 'I'ergitol, is drawn from a storage tank (not shown) and passed through pipe 12 with flow controlled at a rate set by valve [3 and sprayed onto the dry chopped cotton stalks emitted from the blower II. The wetted mass passes into the atmospherically open top of mixing tank H1. The tank I4 is maintained at a fixed level of fluid and stalks by a conventional type float 15 having an arm l6 attached to the float and actuated by the liquid level to throttle the fluid inlet valve I3 through a connecting rod IT. The tank (4 has a double conical bottom, in one cone 18 of which fluid and stalk is picked up by the suction of a pump 19 and recycled to the top of the tank I4 through pipe 20 to secure complete agitation and wetting of the stalk, as well as considerable release of entrapped air bubbles, and in the other cone 2! the preliminary wet and deaerated stalk and fluid is withdrawn by the suction of a pump 22 for passage to the next step of the process. 4A bailie 23 is placed in the tank 14 slanting above the outlet cone 2| to divert the incoming and recycle stalk suspension towards recycle outlet cone !8 so that most of the stalk is recycled for thorough wetting and the stalk and fluid which passes into outlet cone 2! has been thoroughly wet by having most of the outlet material recycled and wet by ultimately passing beneath the baffle 23.

It is to be noted that the wetting liquid described here is wetting agent and water. If alkali is to be used, then the wetting liquid, as made up, may further include up to 3%, usually less than 1% of alkali, such as caustic soda or soda ash. The alkali may, of course, be added at any subsequent point up to the digester.

Preliminarily, wet stalk and fluid are passed from pump 22 to a deaerating tank 24 by way of pipe 25 and subjected to a vacuum maintained on tank 24 by a vacuum pump 26 through pipe 21. The tank 24 has a conical discharge bottom and a part of the stalk and fluid is picked up and recirculated by pump 28 and recycle line 29 to the top of the tank 24 to aid in the deaeration. The stalk suspension is regulated to a preselected height in the tank 24, as observed through a. sight glass 39 by control of the rate of passage through the tank of the fluid in order to keep the level in the tank below the vacuum outlet into pipe 2'! and facilitate gas separation by falling and breaking of the fluid in dropping from both lines 25 and as through the top of the tank. The rate of flow may be controlled by throttlingvalve 3!. To enhance deaeration and initiate penetration and digestive softening of the stalk by the wetting agent, the tank 24 may be heated by conventional jacketing or coils for steam or other heat transfer fluid.

The thorough deaeration of the fluid is particularly desirable herein to avoid oxidation and degradation of the fiber since no reducing chemical, such as sulfite, is generally present which would inherently remove oxygen.

--The deaeration described is thorough and takes only a fraction up to a minute or two whereby the stalk is thoroughly wetted, deaerated and, with the application of heat, penetration and digestive softening will have begun.

The preliminarily treated suspension then passes through pipe 32 to a slush pump 33 capable of moving the fluid suspension continuously against the high pressures developed during further digestive softening and against the suction of the vacuum in tank 24.

A line 34 is shown dotted with a control valve 35 which may be used as a lay-pass if the vacuum treatment is to be dispensed with in such operations where alkali is used, where the operation is to be speeded up, or where the character 01 the product desired renders this feasible.

The preliminarily treated suspension of stalk in fluidis passed by high pressure pump 33 into the top of digester 31 by way of pipe 36. In the digester 31, the fluid suspension is passed in continuous flow through a tortuous path over the surface of several heated platens defining heating stages wherein the temperature of the fluid is continuously raised, reaching an ultimate digestive temperature of 250 to 350 F., preferably about 300 to 330 F., developing a pressure of 25 to pounds per square inch. The fluid suspension is passed rapidly through digester 31 so that the fiber is under digestive softening treatment of 5 to 15 minutes, preferably about 10 minutes; more rapid or slower passage through the digester is possible with considerable sacrifice of either economy of operation or the quality of the product for many uses.

The digester 31 is shown in detail in Figures 2, 3 and 4 and generally consists of a ruggedly constructed rectangular tank capable of withstanding the pressures mentioned. lhe interior of th digester 3'! has mounted therein a series of vertically disposed horizontal platens 3t, each defining a shelf with alternately disposed openings at opposite sides whereby, after passing over one platen 38, the fluid may descend to the next, passing over each for suitable heat treatment and then passing out at the bottom through outlet 39.

Ihe space defined between each platen is further subdivided by vertical parallel division plates 49 into a set of parallel alleys, alternately open at the end of each alley so that each may communicate with the adjacent alley. Thus, on the surface of a paten 38, the suspension will pass from side to side of a single platen up and back through the communicating alleys and finally drop through an opening 48' in the platen to the next lower platen, thus following a tortuous path in each space between platens, repeating on the next lower platen space. Each platen 38 is internally heated by super-heated steam or other heat transfer fluid supplied thereto and withdrawn by pipes M on opposite sides of the digester from large leads and return heater pipes 42 supplied with heating fluid from any suitable source, such as a steam boiler (not shown).

As thus described, the material passed through the digester in a continuous stream is subjected to indirect heat whereby high temperature and pressure is developed in the fluid adequate to soften the cotton stalk fiber bundles for ultimate separation into individual fibers.

The suspension of softened fiber bundles passes under the high pressure and temperature of the digester through pipe 39 to a rapidly rotating beater 43 for ultimate separation of fibers.

The heater 43 forms the subject matter of copending application, Serial No. 33,697, filed June 18, 1948, now Patent No. 2,592,481, issued April 3, 1952, and is specifically designed to separate fiber by beating with rubber whips cooperating with baffle type walls in a soft impact separation, without macerating, tearing or abrading action, to distinguish from such usual beater eifects.

While more detailed construction is described in the copending application, for purposes herein, it is pointed out that the beater comprises an elongated tank of irregular polyhedral straight sides 44, for example, hexagonal or octagonal or eccentric, such as heart-shaped.

The beater tank has mounted for rotation therein an inner shaft-like duct 45 carrying, internally and externally fastened to the wall of said rotating duct, spirally or axially mounted rubber whips 46 for rotation therewith. One end of the-rotating duct 45 communicates with pipe 38 to receive digestively softened fiber suspension-and pass the same through the interior of the duct 45, rotativ'ely beating the fiber by the flailing action of the rubber whips 4'6 extending into the duct 45. The duct is open at the end 41 of the tank so that the partially'beaten fiber flows out from the rotating duct into the body of the tank, reverses its direction of flow, and passes back over the outside of the duct 45 and continues to be beaten by whips extending from the outside of duct 45 and is thrown against the straight side or eccentric walls 44 of the tank. The passage of the pulp further is baffled by a series of spiral vanes 48 mounted from the walls of the tank. These vanes cooperate with the whips and the throwing effect on the fiber suspension -.thereby against such bafiling to enhance the gentle non-abrasive or non-cutting separation of the fiber bundles into individual fiber. Thus it is to be noted that no abrasive teeth or cutting action, other than flexible whipping and irregular baiiiing, to stop short the rapidly thrown fibers, is present in the construction described. The duct .45 is rapidly rotated through a pulley 49 driven by a belt from a motor (not shown). The whips used herein are commonly rubber hose and, as these are flexed in opposite rotative effects a at various angles, fluid is alternately drawn into the hose and expelled, thus adding to the turbulent movement of the fiber in suspension to aid the ultimate fiber separation.

.Quring the beating, as described, the fluid is still maintained under the heat and pressure of the digester.

It is to be noted that the duct 45 may be rotated either direction. When the whips are spirally disposed, as well as the baffle vanes, the rotation may be in a direction to give a helical thrust eifect, either to aid the normal passage through the beater, or to oppose such passage to give a greater force effect.

The fluid pulp passes out of the beater through a pipe 50 and through a pressure reducing valve This valve is automatically operated by the pressure developed in the beater so as to regulate the-flow to maintain the pressure in the beater and digester substantially constant, the pressure control to the valve being communicated through duct52 with a pilot exhaust of pressure control fluid through duct 53.

The separated fiber now passes at atmospheric pressure through duct 54 into emulsion treating tank 55, conventionally fitted with an agitator 56 for mixing emulsion with the pulp.

For certain purposes the pulp may be otherwise treated, such as by washing and drying.

For purposes of producing water resistant organic emulsion treated pulp, emulsion such as emulsified wax, tar, pitch, resin or asphalt suspended in water in an oil in water type of emul sion with acid, alkaline or salt type of dispersing agents is added and homogeneously mixed with the pulp. Thus a 1 to 5% suspension of 50 penetration asphalt, 70% chlorinated wax, or low temperature coal tar are suitable materials to be applied as emulsions. Various suspending agents such as caustic soda, triethanol amine, petroleum sulfonic acid, sodium lauryl sulfate, are used in forming the emulsion. After thorough mixing of the emulsion and fiber, the emulsion is broken in situ by adding to the tank alkali such as caustic soda, mineral acid such as sulfuric acid, hydrochloric acid, or phosphoric acid or salts, such as sodium chloride or aluminum sulfate, depending on the character of the emulsifying agent, to neutralize or coagulate the same and thus break the emulsion precipitating the organic material in situ on the individual fibers to give fine surface coating thereof.

The following examples illustrate the practice of this invention:

Example I.A 3% aqueous suspension .of 50 penetration petroleum asphalt using sodium lauryl sulfonate as the dispersing agent is added to an individual long undegraded fiber suspensionin water of cotton stalk fiber as emitted from the beater described above and stirred to homogeneity. To this mixture of emulsified asphalt and fiber suspension is added dilute sulfuric acid to a pH of 6.5 and the emulsion will break and the asphaltic particles will homogeneously coat the fiber in suspension. The coated filaments are then separated from the water and dried on a Fourdrinier machine or other fiber matting equipment to be formed into such products as water repellent boxboard, Wall board, felt, shingles, roofing paper, and other common paper products. Other known alkaline and alkali salt dispersing agents including lime, caustic soda or trisodium phosphate may be used to disperse the asphalt and other mineral acids may be used to neutralize the same to effect coagulation.

Example IL-The method of Example I is repeated, using an acid dispersing agent for the asphalt, i. e., petroleum sulfonic acid and the acid is coagulated by neutralizing with caustic soda or ammonia. Other acids, such as sulfuric, or phosphoric or organic acids such as stearic, or alkyl suionic' acids may be used ,as acid dis persing medium.

Example III .-The method of Examples I and II are repeated, using a 3% dispersion of 70% chlorinated parafii-n wax to give a water repellent r and termite proofed wall board or other build ing materials or paper products.

Example IV.--The method of Example III is repeated, using phosphoric acid .as dispersing agent for the-chlorinated wax, and the phosphoric acid is utimately neutralized to thus precipitate the wax in situ with sodium arsenite to form a salt of the phosphoric acid containin arsenic. The homogeneously coated filaments hereof are waterproof as well as flameproof and thus are an improved building material. The method of this example may be repeated, omitting the chlorinated wax to impart fireproofing salt coating without the water repel-lancy. Moreover, various fireproofing salt combinations, suchas arsenic and other metal salts with carbonic acid, may be substituted.

The treated pulp of the several examples is ultimately matted into the several products on a Fourdrinier machine into shingles, wall board,

roofing paper, insulation, etc., with or without further lamination.

Various modifications will occur to those skilled in the art and it is intended that the foregoing description be regarded as exemplary and not limiting, except as defined in the claims.

What we claim as new is:

1. Method of liberating the fiber of cotton stalk inits natural undegraded long fiber form comprising suspending chopped cotton stalk in a fluid slurry consisting of water containing as the active digestive component 0.1 to 5.0 per cent of a Wetting agent, continuously heating the fiber bundles in said aqueous solution to a temperature in the range of about 250 to 350 F. under substantially the pressure developed at said temperature for a period of about 5 to 15 minutes, and then non-abrasively beating the fiber under the same heat and pressure to gently separate the digestively softened bundles into substantially individual fibers.

2. Method of liberating cotton stalk fiber into their naturally undegraded long fiber as contained in cotton stalk without substantial chemical degradation comprising forming a suspension of small cotton stalk sections in a fluid slurry consisting of water containing as the active digestive component 0.1 to 5.0 per cent of a wetting agent, de-aerating said suspension of the cotton stalk in said liquid, rapidly heating the Q suspension under the pressure naturally developed to a temperature in the range of 250 to 350 F. for a period of time of about 5 to 15 minutes sufiicient to merely soften the fiber and its natural coating of lignin, waxes and resins without substantial chemical attack thereon, and then separating the softened fiber bundles into substantially individual fibers still containing their natural lignin, wax and resin coating by nonabrasively beating the fiber under the same heat and pressure.

3. Method of liberating cotton stalk fiber into their naturally undegraded long fiber as contained in cotton stalk without substantial chemical degradation comprising forming a suspension of small cotton stalk sections in a fiuid slurry consisting of water containing as the active digestive component 0.1 to 5.0 per cent of a Wetting agent, de-aerating said suspension of the cotton stalk in said liquid, rapidly heating the suspension under the pressure naturally developed to a temperature in the range of 250 to 350 F. for a period of about 5 to 15 minutes sufficient to merely soften the fiber and its natural coating of lignin, waxes and resins without substantial chemical attack thereon, then separating the softened fiber bundles into substantially individual fibers still containing their natural lignin, wax and resin coating by non-abrasively beating the same under the same heat and pressure, and finally homogeneously mixing the fiber suspension with a water resistant binder substance compatible with the natural coating upon. the fibers and then separating the binder coated fiber from the liquid suspending medium and forming the same into firmly bonded fibrous sheets.

4. A matted and firmly bonded product in sheet-like form, consisting essentially of natural undegraded long cotton stalk fiber, each fiber being coated with its naturally occurring coating of resinous, waxy and lignin coating substances and further coated with a water-repellent binder substance to securely adhere the fibers into the sheet-like product, said product being formed by digestively softening chopped lengths of cotton stalk suspended in a fiuid slurry consisting of water containing as the active digestive component 0.1 to 5.0 per cent of a wetting agent, heating said suspension to a temperature in the range of 250 to 350 F. for approximately 5 to 15 minutes and under a pressure developed at said temperature, non-abrasively beating said softened fiber bundles to separate the same into substantially individual fibers while suspended in said aqueous medium under the same temperature and pressure at which they were softened, and then adding the water-repellent binder substance to said individual fiber suspension and separating the said binder coated fibers from the aqueous suspending medium and forming the same into firmly bonded sheets.

ARTHUR M. SPENCER.

ABNER JACOBSON.

KARL SIXT.

References Cited in the file of this patent UNITED STATES PATENTS Number Name Date Re. 18,200 Haglund Sept. 22, 1931 143,940 Sturdevant Oct. 21, 1873 480,334 Maste Aug. 9, 1892 1,633,733 Fish June 28, 1927 1,663,503 Mason Mar. 20, 1928 1,590,954 Spencer Nov. 6, 1928 1,894,577 Wells Jan. 17, 1933 1,991,769 Palmer Feb. 19, 1935 2,008,892 Asplund July 23, 1935 2,011,799 De la Rosa Aug. 20, 1935 2,041,745 Dreyfus May 26, 1936 2,042,465 Hines June 2, 1936 2,057,167 Sherman Oct. 13, 1936 2,116,511 Earle May 10, 1938 2,145,851 Asplund Feb. 7, 1939 2,159,258 De La Rosa May 23, 1939 2,178,266 Pomilio Oct. 31, 1939 2,263,903 Pomilio Nov. 25, 1941 2,323,194 Beveridge et al. June 29, 1943 2,359,543 Branzell et al. Oct. 3, 1944 2,388,592 Asplund Nov. 6, 1945 2,396,587 Lowgren et al. Mar. 12,.1946 2,402,160 Heritage June 18, 1946 2,422,522 Beveridge et al. June 17, 1947 2,470,764 Dunbar May 24, 1949 2,473,190 Baskin et al. June 14, 1949 2,544,887 Leonard Mar. 13, 1951 FOREIGN PATENTS Number Country Date 279,583 Great Britain Nov. 3, 1927 526,109 Great Britain 1940 OTHER REFERENCES Chemistry of Pulp and Paper Making, by Sutermeister, 3rd ed., pp. 303, 306, 307, 309, 310 (1941),

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US143940 *Jan 30, 1873Oct 21, 1873 Improvement in the manufacture of paper-stock
US480334 *Jul 13, 1891Aug 9, 1892 Hermann xdelbert alfred
US1633733 *Jul 14, 1925Jun 28, 1927Jr Frederick K FishProcess and apparatus for manufacturing ground-wood pulp
US1668503 *Sep 20, 1926May 1, 1928Hall Mary EMassage and cleansing cream and method of preparing the same
US1690954 *Feb 10, 1928Nov 6, 1928Edmondson SpencerProcess for the extraction of cellulose or paper pulp from fibrous vegetable matter containing the same
US1894577 *Sep 17, 1927Jan 17, 1933Mine & Smelter Supply CompanyProduction of fiber
US1991769 *May 27, 1933Feb 19, 1935Palmer Gideon HowardUntilization of cotton plant
US2008892 *Sep 19, 1934Jul 23, 1935Defibrator AbMethod of manufacture of pulp
US2011799 *Oct 8, 1934Aug 20, 1935Roza Corp DeDigesting apparatus
US2041745 *Feb 11, 1933May 26, 1936 Manufacture of cellulosic prod
US2042465 *Sep 30, 1935Jun 2, 1936Hines Pierre RProcess for deinking paper printed with oxidizable inks
US2057167 *Jan 11, 1933Oct 13, 1936Brown CoManufacture of impregnated sheet products
US2116511 *Dec 22, 1934May 10, 1938Theodore EarlePaper stock deinking method
US2145851 *Sep 19, 1934Feb 7, 1939Defibrator AbApparatus for manufacture of pulp
US2159258 *May 28, 1934May 23, 1939Joaquin Julio De La Roza SrMethod and apparatus for digesting fibrous or cellular material
US2178266 *Jul 16, 1937Oct 31, 1939Pomilio Corp LtdContinuous process for the manufacture of semipulp
US2263903 *Jul 16, 1937Nov 25, 1941Pomilio Corp LtdApparatus for the extraction of cellulosic fibers from vegetable material
US2323194 *Aug 7, 1940Jun 29, 1943Brookes Beveridge JamesApparatus for the production of pulp from cellulosic material
US2359543 *Sep 23, 1941Oct 3, 1944Kamyr AbApparatus for continuous digestion of fibrous material
US2388592 *Sep 26, 1940Nov 6, 1945Defibrator AbProcess of making ligno-cellulose pulps from straw
US2396587 *Mar 20, 1941Mar 12, 1946American DefibratorApparatus for producing pulp
US2402160 *May 13, 1940Jun 18, 1946Wood Conversion CoManufacture of bituminous fiber and fiber products
US2422522 *Apr 24, 1943Jun 17, 1947Paper And Ind Appliances IncMethod for the production of pulp from cellulosic material
US2470764 *Sep 23, 1943May 24, 1949Leonidas Dunbar ThomasMethod of treating waste sulfite liquor
US2473190 *Jul 1, 1944Jun 14, 1949Standard Oil Dev CoMethod of producing fibrous building compositions
US2544887 *May 18, 1946Mar 13, 1951Leonard Jr Arthur GManufacture of waterproof paper
USRE18200 *Mar 1, 1930Sep 22, 1931Patejxtaxtiebolagetof stockholm
GB279583A * Title not available
GB526109A * Title not available
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2794738 *May 10, 1951Jun 4, 1957Fibre Corp Of America IncFibrous board and sheet for insulation and other purposes of matted long cotton stalk fiber
US2807989 *Jul 9, 1953Oct 1, 1957Lamort E & MBeater apparatus
US2835574 *Jul 13, 1954May 20, 1958Aronovsky Samuel IModified mechano-chemical pulping
US2999784 *Jul 7, 1958Sep 12, 1961Escher Wyss GmbhProcess and apparatus for the treatment of fibrous materials in the production of cellulose or semi-cellulose
US3188267 *Sep 11, 1961Jun 8, 1965Lummus CoApparatus for continuously pulping cellulose matter
US3215587 *Jan 21, 1963Nov 2, 1965Lummus CoContinuous process and apparatus for delignification of cellulosic material
US3951732 *Nov 5, 1973Apr 20, 1976A. Ahlstrom OsakeyhtioDelignification and bleaching of wood pulp with oxygen in the presence of triethanolamine
US4045280 *Feb 17, 1976Aug 30, 1977Macmillan Bloedel LimitedEthanolamine or methylamine, copper or nickel nitrate
US4067768 *Jun 15, 1977Jan 10, 1978Macmillan Bloedel LimitedAlkaline pulping of lignocellulosic material with amine and sulfate pretreatment
US4091749 *Oct 20, 1976May 30, 1978Macmillan Bloedel LimitedAlkaline pulping of lignocellulosic material with amine pretreatment
US4347100 *May 21, 1981Aug 31, 1982The Chemithon CorporationStrength of paper from mechanical or thermomechanical pulp
Classifications
U.S. Classification162/11, 162/76, 162/159, 162/17, 162/99, 162/72, 162/75, 241/28
International ClassificationD21C3/00
Cooperative ClassificationD21C3/003
European ClassificationD21C3/00B