US3427217A - Repulping of wet-strength broke containing wet-strength resin - Google Patents
Repulping of wet-strength broke containing wet-strength resin Download PDFInfo
- Publication number
- US3427217A US3427217A US3427217DA US3427217A US 3427217 A US3427217 A US 3427217A US 3427217D A US3427217D A US 3427217DA US 3427217 A US3427217 A US 3427217A
- Authority
- US
- United States
- Prior art keywords
- wet
- strength
- broke
- resin
- repulping
- 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
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
- D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
- D21C5/02—Working-up waste paper
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/64—Paper recycling
Definitions
- This invention relates to the pulping of wet-strength paper broke.
- Broke is a waste product of the paper industry which, if not recovered and utilized, represents a substantial loss. It is customary, therefore, to repulp the broke and reuse it in the process. This has worked out quite well in the case of broke containing such materials as rosin size, starch, clay and the like since this type of broke can be handled in the usual equipment. In the case of wet-strength broke, however, the resin-fiber bonds are very difficult to break and have generally required the use of high temperatures and low pHs. This necessitate special equipment, thus increasing costs and, in addition, may result in damage to the fibers.
- oxidizing salts which have been found effective for the purpose are sodium hypochlorite, calcium hypochlorite, sodium chlorite, chlorine dioxide, sodium peroxide, sodium hydrosulfite, sodium chlorate, potassium chlorate, ammonium persulfate and similar water-soluble alkali metal and alkali earth metal salts.
- sodium hypochlorite calcium hypochlorite
- sodium chlorite sodium chlorite
- chlorine dioxide sodium peroxide
- sodium hydrosulfite sodium chlorate
- potassium chlorate sodium ammonium persulfate
- water-soluble alkali metal and alkali earth metal salts water-soluble alkali metal and alkali earth metal salts.
- water-soluble metal hypochlorites are preferred.
- the wetstrength broke is treated with a dilute aqueous solution of the oxidizing salt.
- This may be accomplished advantageously by introducing the broke into a dilute aqueous solution of the salt and permitting it to soak until the desired loosening of the fiber-resin-fiber bonds is obtained, i.e., until the fiber-resin-fiber bonds are loosened to the point where the broke can be pulped in conventional pulping equipment.
- the treated broke may then be subjected to mechanical pulping in the usual manner. Stirring is not necessary during treatment of the broke but may be used if desired.
- the time required to obtain the desired loosening of the fiber-resin-fiber bonds will vary depending upon a number of factors such as the type and concentration of salt, temperature of treatment, type of wet-strength resin, extent of defibering desired and so on. In general, times from about 15 minutes to about 90 minutes have been found satisfactory although more or less time may be used, if desired. From about 30 minutes to about 60 minutes is preferred.
- the concentration of the oxidizing salt, based on dry pulp, may be varied from about 0.05% to about but will usually be from about 0.1% to about 1.0%.
- the defibering proceeds somewhat more rapidly if an excess of the oxidizing salt is present at the outset of the treatment, and hence, this is the preferred procedure. Satisfactory loosening of the fibers with a minimum of damage thereto ice takes place at pHs from about 4 to about 10. Since the pH during treatment will normally fall within this range, adjustment of pH is generally not necessary.
- the treatment herein described is most advantageously carried out with a hot oxidizing salt solution at temperatures from about 30 C. to about C. Preferred temperatures are from about 40 C. to about 75 C.
- the process of the invention is useful in connection with the repulping of broke containing any adsorbed wetstrength resin.
- Typical of these are cationic amine-modified urea-formaldehyde resins, melamine-formaldehyde resins, cationic resins prepared by reacting epichlorohydrin with a polyamide of a saturated dicarboxylic acid and a polyalkylene polyamine, cationic resins prepared by reacting epichlorohydrin with a polyalkylene polyamine, and so on.
- the wet-strength broke utilized in the examples was prepared by adding to an aqueous suspension of paper pulp (70% groundwood, 20% unbleached sulfite and 10% semibleached kraft) about 1.0% by weight, based on the weight of pulp, of a cationic amine modified urea-formaldehyde wet-strength resin and then sheeting and drying the pulp in conventional manner.
- the cationic ureaformaldehyde resin was formed by reacting urea, aqueous formaldehyde and triethylenetetramine (technical grade) together first for a short time under alkaline conditions and then under acid conditions until the viscosity of the solution rose to about V-W Gardner-Holdt.
- the reactants were utilized in a ratio of about 21.32 parts of urea, 63.26 parts of 37% formaldehyde, 82.84 parts of triethylenetetramine.
- Example 1 Twenty grams of the wet-strength broke described above was immersed in a solution containing ml. of Dazzle bleach (5.25% NaOCl), 1 g. of sodium hydroxide (98% NaOH) and 300 ml. of water. The mixture was heated to F. and maintained at this temperature during the treatment. Five minutes after charging, the stock was light cream in color and sufficiently tender to be dispersed in water after rolling a piece between the thumb and the forefinger. The condition of the stock 15 minutes after charging was about the same as at 5 minutes. Thirty minutes after charging the stock was white in color and easily dispersed in water. The fiber length was good.
- Dazzle bleach 5.25% NaOCl
- sodium hydroxide 98% NaOH
- Example 2 Twenty grams of the same wet-strength broke treated in Example 1 was immersed in a solution containing 100 ml. of Dazzle bleach (5.25% NaOCl), 0.5 g. of sodium hydroxide (98% NaOH) and 350 ml. of water. The mixture was warmed to F. and placed on a hot water bath.
- Dazzle bleach 5.25% NaOCl
- sodium hydroxide 98% NaOH
- a process for the pulping of paper broke composed of cellulose fibers bonded together by an adsorbed content of at least one wet-strength resin which comprises: slurrying said broke with a dilute aqueous solution of an inorganic oxidizing salt thereby loosening the fiber-resinfiber bonds in said broke, and then subjecting the broke to mechanical pulping.
Description
United States Patent 3,427,217 REPULPING OF WET-STRENGTH BROKE CON- TAINING WET-STRENGTH RESIN Harold R. Miller, Holyoke, Mass., assignor to Hercules Incorporated, a corporation of Delaware No Drawing. Filed Jan. 28, 1960, Ser. No. 5,131 US. Cl. 162-6 3 Claims Int. Cl. D21c 3/04, 3/22, 5/02 ABSTRACT OF THE DISCLOSURE A process of repulping wet-strength broke containing wet-strength resins by slurrying the broke with a dilute aqueous solution of an inorganic oxidizing salt.
This invention relates to the pulping of wet-strength paper broke.
Broke is a waste product of the paper industry which, if not recovered and utilized, represents a substantial loss. It is customary, therefore, to repulp the broke and reuse it in the process. This has worked out quite well in the case of broke containing such materials as rosin size, starch, clay and the like since this type of broke can be handled in the usual equipment. In the case of wet-strength broke, however, the resin-fiber bonds are very difficult to break and have generally required the use of high temperatures and low pHs. This necessitate special equipment, thus increasing costs and, in addition, may result in damage to the fibers.
It has now been found that the pulping of wet-strength broke is greatly facilitated by the action of aqueous solutions of various oxidizing salts. Exemplary of the oxidizing salts which have been found effective for the purpose are sodium hypochlorite, calcium hypochlorite, sodium chlorite, chlorine dioxide, sodium peroxide, sodium hydrosulfite, sodium chlorate, potassium chlorate, ammonium persulfate and similar water-soluble alkali metal and alkali earth metal salts. In fact, it appears that the particular cation associated with the oxidizing anion has no pronounced effect and thus that any water-soluble oxidizing salt may be employed. The water-soluble metal hypochlorites are preferred.
In carrying out the process of the invention, the wetstrength broke is treated with a dilute aqueous solution of the oxidizing salt. This may be accomplished advantageously by introducing the broke into a dilute aqueous solution of the salt and permitting it to soak until the desired loosening of the fiber-resin-fiber bonds is obtained, i.e., until the fiber-resin-fiber bonds are loosened to the point where the broke can be pulped in conventional pulping equipment. The treated broke may then be subjected to mechanical pulping in the usual manner. Stirring is not necessary during treatment of the broke but may be used if desired.
The time required to obtain the desired loosening of the fiber-resin-fiber bonds will vary depending upon a number of factors such as the type and concentration of salt, temperature of treatment, type of wet-strength resin, extent of defibering desired and so on. In general, times from about 15 minutes to about 90 minutes have been found satisfactory although more or less time may be used, if desired. From about 30 minutes to about 60 minutes is preferred.
The concentration of the oxidizing salt, based on dry pulp, may be varied from about 0.05% to about but will usually be from about 0.1% to about 1.0%. The defibering proceeds somewhat more rapidly if an excess of the oxidizing salt is present at the outset of the treatment, and hence, this is the preferred procedure. Satisfactory loosening of the fibers with a minimum of damage thereto ice takes place at pHs from about 4 to about 10. Since the pH during treatment will normally fall within this range, adjustment of pH is generally not necessary.
The treatment herein described is most advantageously carried out with a hot oxidizing salt solution at temperatures from about 30 C. to about C. Preferred temperatures are from about 40 C. to about 75 C.
The process of the invention is useful in connection with the repulping of broke containing any adsorbed wetstrength resin. Typical of these are cationic amine-modified urea-formaldehyde resins, melamine-formaldehyde resins, cationic resins prepared by reacting epichlorohydrin with a polyamide of a saturated dicarboxylic acid and a polyalkylene polyamine, cationic resins prepared by reacting epichlorohydrin with a polyalkylene polyamine, and so on.
The following examples will illustrate the invention. The wet-strength broke utilized in the examples was prepared by adding to an aqueous suspension of paper pulp (70% groundwood, 20% unbleached sulfite and 10% semibleached kraft) about 1.0% by weight, based on the weight of pulp, of a cationic amine modified urea-formaldehyde wet-strength resin and then sheeting and drying the pulp in conventional manner. The cationic ureaformaldehyde resin was formed by reacting urea, aqueous formaldehyde and triethylenetetramine (technical grade) together first for a short time under alkaline conditions and then under acid conditions until the viscosity of the solution rose to about V-W Gardner-Holdt. The reactants were utilized in a ratio of about 21.32 parts of urea, 63.26 parts of 37% formaldehyde, 82.84 parts of triethylenetetramine.
Example 1 Twenty grams of the wet-strength broke described above was immersed in a solution containing ml. of Dazzle bleach (5.25% NaOCl), 1 g. of sodium hydroxide (98% NaOH) and 300 ml. of water. The mixture was heated to F. and maintained at this temperature during the treatment. Five minutes after charging, the stock was light cream in color and sufficiently tender to be dispersed in water after rolling a piece between the thumb and the forefinger. The condition of the stock 15 minutes after charging was about the same as at 5 minutes. Thirty minutes after charging the stock was white in color and easily dispersed in water. The fiber length was good.
Example 2 Twenty grams of the same wet-strength broke treated in Example 1 was immersed in a solution containing 100 ml. of Dazzle bleach (5.25% NaOCl), 0.5 g. of sodium hydroxide (98% NaOH) and 350 ml. of water. The mixture was warmed to F. and placed on a hot water bath.
Five minutes after charging the stock was pale yellow in color and was partially defibered when rolled between the thumb and forefinger.
Ten minutes after charging the stock was almost all defibered when pieces were rolled between the thumb and forefinger.
Thirty minutes after charging the stock was white and sufficiently softened to be completely defibered when rolled between the thumb and forefinger. Final temperature was F. The liquor was only very slightly slippery but alkaline to phenol phthalein. The pH at 30 C. was 8.9. It required 1 cc. of 3% alum per 30 cc. of liquor to adjust the pH to 7.0.
Two hours after charging the fiber was tender and readily defibered by rolling between the thumb and forefinger. The liquor pH at 30 C. was 8.9.
It is readily apparent that the process of the invention is highly effective in facilitating the defibering of wetstrength broke. While preferred embodiments of the -invention have been disclosed, it is not intended that the invention be limited to the specific details illustrated and described except as they may be included in the following claims.
What I claim and desire to protect by Letters Patent is:
1. A process for the pulping of paper broke composed of cellulose fibers bonded together by an adsorbed content of at least one wet-strength resin which comprises: slurrying said broke with a dilute aqueous solution of an inorganic oxidizing salt thereby loosening the fiber-resinfiber bonds in said broke, and then subjecting the broke to mechanical pulping.
2. A process according to claim 1 wherein the oxidizing salt is a water-soluble colorless metal hypochlorite.
References Cited UNITED STATES PATENTS 3/1926 Plumstead 162-6 2/1959 House et al 1626 FOREIGN PATENTS 6/1960 Canada. 2/1917 Great Britain.
S. LEON BASHORE, Primary Examiner.
U.S. C1. X.R.
Dedication 3,427,217.Har0ld R. Miller, Holyoke, Mass. REPULPING OF WET- STRENGTH BROKE CONTAINING WET-STRENGTH RESIN. Patent dated Feb. 11, 1969. Dedication filed Mar. 13, 1969, by the assignee, Hercules Incorporated. Hereby dedicates to the Public the entire term of said patent.
[Ofiicz'al Gazette July 8, 1.969.]
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US513160A | 1960-01-28 | 1960-01-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
US3427217A true US3427217A (en) | 1969-02-11 |
Family
ID=21714339
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US3427217D Expired - Lifetime US3427217A (en) | 1960-01-28 | 1960-01-28 | Repulping of wet-strength broke containing wet-strength resin |
Country Status (1)
Country | Link |
---|---|
US (1) | US3427217A (en) |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0585955A1 (en) * | 1992-09-03 | 1994-03-09 | Hercules Incorporated | Repulping paper and paperboard |
US5593543A (en) * | 1993-08-26 | 1997-01-14 | Henkel Corporation | Process for repulping wet strength paper |
US5755926A (en) * | 1992-02-24 | 1998-05-26 | Kimberly-Clark Worldwide, Inc. | Integrated pulping process of waste paper yielding tissue-grade paper fibers |
US5904808A (en) * | 1996-09-16 | 1999-05-18 | Hercules Incorporated | Processes and compositions for repulping wet strength paper and paper products |
US5994449A (en) * | 1997-01-23 | 1999-11-30 | Hercules Incorporated | Resin compositions for making wet and dry strength paper and their use as creping adhesives |
US6001218A (en) * | 1994-06-29 | 1999-12-14 | Kimberly-Clark Worldwide, Inc. | Production of soft paper products from old newspaper |
US6027610A (en) * | 1994-06-29 | 2000-02-22 | Kimberly-Clark Corporation | Production of soft paper products from old newspaper |
US6074527A (en) * | 1994-06-29 | 2000-06-13 | Kimberly-Clark Worldwide, Inc. | Production of soft paper products from coarse cellulosic fibers |
US6103861A (en) * | 1997-12-19 | 2000-08-15 | Hercules Incorporated | Strength resins for paper and repulpable wet and dry strength paper made therewith |
US6146497A (en) * | 1998-01-16 | 2000-11-14 | Hercules Incorporated | Adhesives and resins, and processes for their production |
US6296736B1 (en) | 1997-10-30 | 2001-10-02 | Kimberly-Clark Worldwide, Inc. | Process for modifying pulp from recycled newspapers |
US6355137B1 (en) | 1997-12-31 | 2002-03-12 | Hercules Incorporated | Repulpable wet strength paper |
US6387210B1 (en) | 1998-09-30 | 2002-05-14 | Kimberly-Clark Worldwide, Inc. | Method of making sanitary paper product from coarse fibers |
CN114318924A (en) * | 2021-12-28 | 2022-04-12 | 山东龙德复合材料科技股份有限公司 | Method for high-value utilization of solidified filter paper waste paper |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB104048A (en) * | 1916-03-15 | 1917-02-22 | Andrew Poulson | An Improved Process for Bleaching Textile Fabrics or the like Material. |
US1576994A (en) * | 1925-11-16 | 1926-03-16 | Jessup & Moore Paper Co | Deinking paper stock |
US2872313A (en) * | 1955-09-08 | 1959-02-03 | American Cyanamid Co | Pulping of paper broke containing wet-strength resins |
CA600455A (en) * | 1960-06-21 | F. Donnelly Harold | Manufacture of cellulosic products |
-
1960
- 1960-01-28 US US3427217D patent/US3427217A/en not_active Expired - Lifetime
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA600455A (en) * | 1960-06-21 | F. Donnelly Harold | Manufacture of cellulosic products | |
GB104048A (en) * | 1916-03-15 | 1917-02-22 | Andrew Poulson | An Improved Process for Bleaching Textile Fabrics or the like Material. |
US1576994A (en) * | 1925-11-16 | 1926-03-16 | Jessup & Moore Paper Co | Deinking paper stock |
US2872313A (en) * | 1955-09-08 | 1959-02-03 | American Cyanamid Co | Pulping of paper broke containing wet-strength resins |
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5755926A (en) * | 1992-02-24 | 1998-05-26 | Kimberly-Clark Worldwide, Inc. | Integrated pulping process of waste paper yielding tissue-grade paper fibers |
US5674358A (en) * | 1992-09-03 | 1997-10-07 | Hercules Incorporated | Repulping wet strength paper and paperboard with persulfate and a carbonate buffer |
EP0585955A1 (en) * | 1992-09-03 | 1994-03-09 | Hercules Incorporated | Repulping paper and paperboard |
US5593543A (en) * | 1993-08-26 | 1997-01-14 | Henkel Corporation | Process for repulping wet strength paper |
US6027610A (en) * | 1994-06-29 | 2000-02-22 | Kimberly-Clark Corporation | Production of soft paper products from old newspaper |
US6074527A (en) * | 1994-06-29 | 2000-06-13 | Kimberly-Clark Worldwide, Inc. | Production of soft paper products from coarse cellulosic fibers |
US6001218A (en) * | 1994-06-29 | 1999-12-14 | Kimberly-Clark Worldwide, Inc. | Production of soft paper products from old newspaper |
US5904808A (en) * | 1996-09-16 | 1999-05-18 | Hercules Incorporated | Processes and compositions for repulping wet strength paper and paper products |
US5994449A (en) * | 1997-01-23 | 1999-11-30 | Hercules Incorporated | Resin compositions for making wet and dry strength paper and their use as creping adhesives |
US6296736B1 (en) | 1997-10-30 | 2001-10-02 | Kimberly-Clark Worldwide, Inc. | Process for modifying pulp from recycled newspapers |
US6103861A (en) * | 1997-12-19 | 2000-08-15 | Hercules Incorporated | Strength resins for paper and repulpable wet and dry strength paper made therewith |
US6245874B1 (en) | 1997-12-19 | 2001-06-12 | Hercules Incorporated | Process for making repulpable wet and dry strength paper |
US6355137B1 (en) | 1997-12-31 | 2002-03-12 | Hercules Incorporated | Repulpable wet strength paper |
US6146497A (en) * | 1998-01-16 | 2000-11-14 | Hercules Incorporated | Adhesives and resins, and processes for their production |
US6387210B1 (en) | 1998-09-30 | 2002-05-14 | Kimberly-Clark Worldwide, Inc. | Method of making sanitary paper product from coarse fibers |
CN114318924A (en) * | 2021-12-28 | 2022-04-12 | 山东龙德复合材料科技股份有限公司 | Method for high-value utilization of solidified filter paper waste paper |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2872313A (en) | Pulping of paper broke containing wet-strength resins | |
US3427217A (en) | Repulping of wet-strength broke containing wet-strength resin | |
US4798651A (en) | Process for preparing pulp for paper making | |
US3582461A (en) | Pitch control in pulp and papermaking processes | |
US2583548A (en) | Production of pigmented cellulosic pulp | |
US6066233A (en) | Method of improving pulp freeness using cellulase and pectinase enzymes | |
US5674358A (en) | Repulping wet strength paper and paperboard with persulfate and a carbonate buffer | |
EP0333398B1 (en) | Process for bleaching mechanical wood pulp | |
US3382149A (en) | Bleaching of hardwood sulfite pulp with hydrogen peroxide, including pretreatment with alkali | |
SE8604313D0 (en) | CATIONIC CELLULOSA PRODUCT AND PROCEDURES FOR PRODUCING THEREOF | |
US3658640A (en) | Pulping of wet strength broke containing polyvinylamide-glyoxal resin | |
US2147618A (en) | Method of bleaching pulp | |
US3062703A (en) | Wet-strength paper containing polymeric dialdehydes | |
US4411737A (en) | Pulp treating process | |
US3738908A (en) | Prehydrolysis and digestion of bagasse fibers | |
US2610119A (en) | Defibering presoaked ligno-cellulose | |
US3832278A (en) | Prehydrolysis and digestion of bagasse fibers | |
US1644447A (en) | Treatment of paper pulp | |
US3619358A (en) | Method for improving water drainage from a paper web on a wire-screen of a paper machine by using a modified polyacrylamide prepared from a water-soluble polyacrylamide by the hoffman reaction | |
US1894501A (en) | Manufacture of wood pulp | |
US4978426A (en) | Production of high strength linerboard with oxygen and alkali | |
US3407113A (en) | Pulping of wet strength paper with hypochlorous acid | |
CA1103413A (en) | Process for the manufacture of mechanical pulp | |
US4526651A (en) | Process for oxygen bleaching paper pulp using melamine as a viscosity stabilizer | |
US3436302A (en) | Method of bleaching groundwood pulp web with acid |