[go: up one dir, main page]

US2178696A - Material treatment - Google Patents

Material treatment Download PDF

Info

Publication number
US2178696A
US2178696A US188576A US18857638A US2178696A US 2178696 A US2178696 A US 2178696A US 188576 A US188576 A US 188576A US 18857638 A US18857638 A US 18857638A US 2178696 A US2178696 A US 2178696A
Authority
US
United States
Prior art keywords
bleaching
chlorine
solution
water
hocl
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
Application number
US188576A
Inventor
Irving E Muskat
George H Cady
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
PPG Industries Inc
Original Assignee
Pittsburgh Plate Glass Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Pittsburgh Plate Glass Co filed Critical Pittsburgh Plate Glass Co
Priority to US188576A priority Critical patent/US2178696A/en
Application granted granted Critical
Publication of US2178696A publication Critical patent/US2178696A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06LDRY-CLEANING, WASHING OR BLEACHING FIBRES, FILAMENTS, THREADS, YARNS, FABRICS, FEATHERS OR MADE-UP FIBROUS GOODS; BLEACHING LEATHER OR FURS
    • D06L4/00Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs
    • D06L4/20Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which contain halogen
    • D06L4/22Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which contain halogen using inorganic agents
    • D06L4/23Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which contain halogen using inorganic agents using hypohalogenites
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06LDRY-CLEANING, WASHING OR BLEACHING FIBRES, FILAMENTS, THREADS, YARNS, FABRICS, FEATHERS OR MADE-UP FIBROUS GOODS; BLEACHING LEATHER OR FURS
    • D06L4/00Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs
    • D06L4/20Bleaching fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods; Bleaching leather or furs using agents which contain halogen

Definitions

  • alkaline hypochlorites of the alkali or alkaline earth metals
  • certain disadvantages arise from such a procedure.
  • Alkaline hypochlorites of course contain substantial quantities of alkali and are therefore c0r l0 rosive and tend to contaminate and to attack the material being treated to an undesirable degree.
  • Bleaching with alkaline hypochlorites results in the contamination of the fibrous product with alkali or alkaline earth metal hydrcxides and carbonates which must be removed before t e' treated product may be suitably sized. This necessitates considerable washing and consequent expenditure of time, labor and money.
  • the alkaline hypochlorites in genera], contain substantial quantities of chlorates which are also corrosive and which attack the fibers being bleached. Furthermore, the rate of bleaching action of the alkaline hypochlorites is relatively low and as a result, considerable time is required to produce a suitably bleached product.
  • chlorine water has been used to some extent as a bleaching agent, it has similar disadvantages.
  • Chlorine water is highly corrosive due to the presence of large amounts of HCl therein.
  • the use of this bleaching agent in general, results in a severe attack upon the fibers and in considerable contamination thereof.
  • the solubility of chlorine in water is so low that suitable bleaching can be secured only after prolonged trea-tment fo a considerable length of time.
  • further quantities of HCl are generated thereby, resulting in a corresponding decrease in bleaching power and an increase in the corrosiveness of the liquor.
  • the use of chlorine water as a bleaching agent is unsuitable for many purposes.
  • HOCl may be used efiicient- 1y as a commercial bleaching agent under certain conditions.
  • commercial HOCl contained substantial quantities of HCl, chlorine, chlorides, chlorates, bicarbonates, salts of the alkali or alkaline earth metals, etc., and we have determined that the undesirable results obtained from the use of this material in bleaching proc esses have been due to one or more of these impurities.
  • excellent bleaching may be secured from use of aqueous solutions of H001 which initially are substantially free of these impurities. Such solutions are comparatively very stable and require only a relatively short period of time to efiect a satisfactory bleaching.
  • Fibrous materials such as rayon, cotton, silk, wood pulp, etc.
  • llll HOCl as used in this process may be prepared by a convenient method which will insure the desired purity.
  • extremely pure HOCl may be prepared by contacting water, which is substantially free from impurities, with 15 chlorine monoxide. Ordinary tap water is generally suitable for this purpose. Other methods of making HOCl may also be found satisfactory.
  • the amount of chlorine monoxide per liter of water may be varied to some dgree but, in gen- 2d eral, asolution containing up to 20 per cent HOCI is found to be satisfactory.
  • the chlorine monoxide used may be in the form of a pure gas if desired, but, in general, it is found preferable to treat water with alfiuid containing small quan- 26 tities of C120, from 1 to 25 per, cent, the remainder of the fluid being made up of suitable diluents, such as carbon dioxide, nitrogen, helium, carbon tetrachloride, etc., but preferably free of contaminating impurities, such as hydrogen chloride, 30) oxides of nitrogen, chlorine dioxide, etc.
  • suitable diluents such as carbon dioxide, nitrogen, helium, carbon tetrachloride, etc.
  • Sub-- stantial quantities of chlorine may be present in the-chlorine monoxide-containing fluid since it is found that the chlorine monoxide dissolves in water so much more rapidly than chlorine that 35' the HOCl solution prepared will contain only very minor quantities of HCl or chlorine.
  • the temperature is preferably maintained at or below room temperature in order to avoid decomposition. 4a
  • the HOCl may be prepared previous to the bleaching operation and used in the bleaching process before substantial decomposition of the HOCl occurs. This may be done, for example, by introducing chlorine monoxide into water and 4d in roducing the resultant HOCl solutions into the bleaching vat within a few minutes after formation. If desired, however, this acid may be generated in situ during the bleaching process by a convenient method as, for example, by contact- 50 ing the aqueous slurry containing the fibers to be bleached with chlorine monoxide.
  • the process may be used to treat various fibrous products, such as Wood pulp, silk, artificial silk fiber such as rayon, textile materials, etc., and
  • treatment of wood pulp it may be used as a means of solubilizing noncellulosic incrustants, as a means of bleaching pulp from which the incrustants have been removed, or may be used to accomplish both of these results.
  • the treatment may be used in conjunction with other bleaching processes which may precede or follow this process.
  • Example I A solution of hypochlorous acid containing 0.1% active Cl was prepared by introducing chlorine monoxide substantially free of HCl, chlorine dioxide or oxides of nitrogen, into a quantity of water at a temperature of 25 C. Skeins of viscose fibers were dipped in this solution at a temperature of 25-30 C. for a period of 6 minutes and were thereafter dipped in dilute sodium carbonate solution and thoroughly washed. The product was very white and the treatment exhibited no tenderizing action. When a similar process is carried out under the same conditions, using an alkaline hypochlorite solution of equivalent active chlorine content, several times the period of treatment herein used is required to secure an equivalent bleaching.
  • Example II A quantity of substantially pure HOCl solution was added to a 3 per cent aqueous suspension of kraft pulp in an amount sufiicient toestablish an available chlorine content of 0.3% and the pH was adjusted to 1.5 by addition of H2804. After 5 minutes, the slurry filtered, repulped and a 0.5% solution of calcium hypochlorite and vigorously agitated for 25 minutes. The resultant pulp was filtered, thoroughly washed and treated with 0.1% solution of substantially pure HOCI solution. The product, after washing, was extremely white and free from contamination.
  • Example III An aqueous slurry of pulp of 4 per cent containing 1 per cent lignin consistency was vigorously agitated and a quantity of a gas containing chlorine monoxide diluted with carbon dioxide was bubbled into the slurry. After 30 minutes, treatment was discontinued and the pulp obtained. was white and free from lignin.
  • the concentration of the bleaching solution may be varied to some degree but, in general, willnot exceedan available chlorine content of 1.2%.
  • the H00] solutions may be prepared in concentrated form (form -20% H001) and diluted to the desired concentration when used.
  • the bleaching liquor becomes contaminated with certain impurities such as HCl, chlorine, chlorates, chlorides, etc.
  • certain impurities such as HCl, chlorine, chlorates, chlorides, etc.
  • the process of bleaching fibrous materials which comprises treating a quantity of water with chlorine monoxide, which is substantially free of hydrochloric acid, chlorine dioxide and oxides of nitrogen in concentrations sufficient to produce a solution of hypochlorous acid and bleaching fibrous materials with this solution.
  • a process of bleaching fibrous materials which comprises immersing said materials in a. body of water which is substantially free from the impurities, chlorine dioxide, hydrochloric acid body of water which is substantially free from the impurities, chlorine dioxide, hydrochloric acid and oxides of nitrogen and introducing a fluid comprising chlorine monoxide which is substantially free from said impurities and a gaseous diluent which is substantially inert to fibrous materials into said body.
  • the process of bleaching fibrous materials which comprises treating a quantity of water with chlorine monoxide which is substantially free from chlorine dioxide, hydrochloric acid or oxides of nitrogen to produce a relatively concentrated solution of hypochlorous acid of relatively high purity, diluting this solution with water to form a more dilute solution of said acid of higher purityand bleaching fibrous materials with said solution before substantial decomposition of the solution can occur.

Landscapes

  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Paper (AREA)

Description

Patented Nov. 7, 1939 UNITED STATES PATENT ()FFICE MATERIAL TREATMENT Irving E. Muskat, Akron, and George H. Cady, Wadsworth, Ohio, assignors to Pittsburgh Plate Glass Company, Allegheny County, Pa., a corporation of Pennsylvania No Drawing. Application February 3, 1938, Serial No. 188,576
7 Claims.
mon to efiect bleaching by means of hypochlorites of the alkali or alkaline earth metals, certain disadvantages arise from such a procedure. Alkaline hypochlorites of course contain substantial quantities of alkali and are therefore c0r l0 rosive and tend to contaminate and to attack the material being treated to an undesirable degree. Bleaching with alkaline hypochlorites, in general, results in the contamination of the fibrous product with alkali or alkaline earth metal hydrcxides and carbonates which must be removed before t e' treated product may be suitably sized. This necessitates considerable washing and consequent expenditure of time, labor and money. .In addition, the alkaline hypochlorites, in genera], contain substantial quantities of chlorates which are also corrosive and which attack the fibers being bleached. Furthermore, the rate of bleaching action of the alkaline hypochlorites is relatively low and as a result, considerable time is required to produce a suitably bleached product.
While chlorine water has been used to some extent as a bleaching agent, it has similar disadvantages. Chlorine water is highly corrosive due to the presence of large amounts of HCl therein. The use of this bleaching agent, in general, results in a severe attack upon the fibers and in considerable contamination thereof. Moreover, the solubility of chlorine in water is so low that suitable bleaching can be secured only after prolonged trea-tment fo a considerable length of time. During treatment, further quantities of HCl are generated thereby, resulting in a corresponding decrease in bleaching power and an increase in the corrosiveness of the liquor. Thus, the use of chlorine water as a bleaching agent is unsuitable for many purposes.
Hypochlorous acid has been used to some extent for bleaching but, in general, this acid has been too unstable and the results obtained have been too irregular to be suitable for commercial processes In accordance with our invention, we
have discovered that HOCl may be used efiicient- 1y as a commercial bleaching agent under certain conditions. In the past, comercial HOCl contained substantial quantities of HCl, chlorine, chlorides, chlorates, bicarbonates, salts of the alkali or alkaline earth metals, etc., and we have determined that the undesirable results obtained from the use of this material in bleaching proc esses have been due to one or more of these impurities. We have found that excellent bleaching may be secured from use of aqueous solutions of H001 which initially are substantially free of these impurities. Such solutions are comparatively very stable and require only a relatively short period of time to efiect a satisfactory bleaching. Fibrous materials, such as rayon, cotton, silk, wood pulp, etc., may be bleached successfully with this agent. llll HOCl as used in this process may be prepared by a convenient method which will insure the desired purity. We have found that extremely pure HOCl may be prepared by contacting water, which is substantially free from impurities, with 15 chlorine monoxide. Ordinary tap water is generally suitable for this purpose. Other methods of making HOCl may also be found satisfactory. The amount of chlorine monoxide per liter of water may be varied to some dgree but, in gen- 2d eral, asolution containing up to 20 per cent HOCI is found to be satisfactory. The chlorine monoxide used may be in the form of a pure gas if desired, but, in general, it is found preferable to treat water with alfiuid containing small quan- 26 tities of C120, from 1 to 25 per, cent, the remainder of the fluid being made up of suitable diluents, such as carbon dioxide, nitrogen, helium, carbon tetrachloride, etc., but preferably free of contaminating impurities, such as hydrogen chloride, 30) oxides of nitrogen, chlorine dioxide, etc. Sub-- stantial quantities of chlorine may be present in the-chlorine monoxide-containing fluid since it is found that the chlorine monoxide dissolves in water so much more rapidly than chlorine that 35' the HOCl solution prepared will contain only very minor quantities of HCl or chlorine. The temperature is preferably maintained at or below room temperature in order to avoid decomposition. 4a
The HOCl may be prepared previous to the bleaching operation and used in the bleaching process before substantial decomposition of the HOCl occurs. This may be done, for example, by introducing chlorine monoxide into water and 4d in roducing the resultant HOCl solutions into the bleaching vat within a few minutes after formation. If desired, however, this acid may be generated in situ during the bleaching process by a convenient method as, for example, by contact- 50 ing the aqueous slurry containing the fibers to be bleached with chlorine monoxide.
The process may be used to treat various fibrous products, such as Wood pulp, silk, artificial silk fiber such as rayon, textile materials, etc., and
is especially effective in the bleaching of textiles without reduction of the tensile strength of the fibers.
In treatment of wood pulp, it may be used as a means of solubilizing noncellulosic incrustants, as a means of bleaching pulp from which the incrustants have been removed, or may be used to accomplish both of these results. The treatment may be used in conjunction with other bleaching processes which may precede or follow this process.
In bleaching wood pulp, or other fibrous materials, it has been found that it is desirable to dissolve the incrustants by treatment in an acid bleaching solution such as a substantially pure solutionof H001 strongly acidified with suitable acid, such as H2804, then to bleach in an alkaline solution such as a solution of an alkali metal or alkaline earth metal hypochlorite. This partially bleached product may then be thoroughly washed and treated in our high purity solution of H001.
The following examples illustrate the invention:
Example I.A solution of hypochlorous acid containing 0.1% active Cl was prepared by introducing chlorine monoxide substantially free of HCl, chlorine dioxide or oxides of nitrogen, into a quantity of water at a temperature of 25 C. Skeins of viscose fibers were dipped in this solution at a temperature of 25-30 C. for a period of 6 minutes and were thereafter dipped in dilute sodium carbonate solution and thoroughly washed. The product was very white and the treatment exhibited no tenderizing action. When a similar process is carried out under the same conditions, using an alkaline hypochlorite solution of equivalent active chlorine content, several times the period of treatment herein used is required to secure an equivalent bleaching.
Example II .A quantity of substantially pure HOCl solution was added to a 3 per cent aqueous suspension of kraft pulp in an amount sufiicient toestablish an available chlorine content of 0.3% and the pH was adjusted to 1.5 by addition of H2804. After 5 minutes, the slurry filtered, repulped and a 0.5% solution of calcium hypochlorite and vigorously agitated for 25 minutes. The resultant pulp was filtered, thoroughly washed and treated with 0.1% solution of substantially pure HOCI solution. The product, after washing, was extremely white and free from contamination.
Example III.An aqueous slurry of pulp of 4 per cent containing 1 per cent lignin consistency was vigorously agitated and a quantity of a gas containing chlorine monoxide diluted with carbon dioxide was bubbled into the slurry. After 30 minutes, treatment was discontinued and the pulp obtained. was white and free from lignin.
The concentration of the bleaching solution may be varied to some degree but, in general, willnot exceedan available chlorine content of 1.2%. If desired, the H00] solutions may be prepared in concentrated form (form -20% H001) and diluted to the desired concentration when used. By this method, we are able to obtain bleaching solutions which are very free from undesirable impurities since dilution of the concentrated solutions which themselves are substantially free from HCl, chlorates, chlorides, carbonates or alkali metal or alkaline earth metal salts, insures the production of solutions of HOCl containing no appreciable quantities of these impurities.
During treatment of the fibers with HOCl, it may be found that the bleaching liquor becomes contaminated with certain impurities such as HCl, chlorine, chlorates, chlorides, etc. In order to avoid substantial accumulation of these substances, it may be desirable to replace a portion of the bleaching liquor with fresh HOCl continuously or from time to time. In this manner, we may maintain the bleach liquor substantially free from these impurities during the major portion of the treatment.
Although the invention has been described in connection with the specific embodiments of certain details thereof, it is not intended that they shall be regarded as limiting the scope of the invention except insofar as included in the accompanying claims.
We claim:
1. The process of bleaching fibrous materials which comprises treating a quantity of water with chlorine monoxide, which is substantially free of hydrochloric acid, chlorine dioxide and oxides of nitrogen in concentrations sufficient to produce a solution of hypochlorous acid and bleaching fibrous materials with this solution.
2. A process of bleaching fibrous materials which comprises immersing said materials in a. body of water which is substantially free from the impurities, chlorine dioxide, hydrochloric acid body of water which is substantially free from the impurities, chlorine dioxide, hydrochloric acid and oxides of nitrogen and introducing a fluid comprising chlorine monoxide which is substantially free from said impurities and a gaseous diluent which is substantially inert to fibrous materials into said body.
5. The process of claim 3 wherein the diluent is carbon dioxide.
6. The process of bleaching fibrous material which comprises immersing said materials in a body of water and introducing a gaseous mixture containing chlorine and chlorine monoxide which is substantially free from hydrochloric acid, chlorine dioxide and oxides of nitrogen into said body of water.
'7. The process of bleaching fibrous materials which comprises treating a quantity of water with chlorine monoxide which is substantially free from chlorine dioxide, hydrochloric acid or oxides of nitrogen to produce a relatively concentrated solution of hypochlorous acid of relatively high purity, diluting this solution with water to form a more dilute solution of said acid of higher purityand bleaching fibrous materials with said solution before substantial decomposition of the solution can occur.
IRVING E. MUSKAT. GEORGE H. CADY.
US188576A 1938-02-03 1938-02-03 Material treatment Expired - Lifetime US2178696A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US188576A US2178696A (en) 1938-02-03 1938-02-03 Material treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US188576A US2178696A (en) 1938-02-03 1938-02-03 Material treatment

Publications (1)

Publication Number Publication Date
US2178696A true US2178696A (en) 1939-11-07

Family

ID=22693723

Family Applications (1)

Application Number Title Priority Date Filing Date
US188576A Expired - Lifetime US2178696A (en) 1938-02-03 1938-02-03 Material treatment

Country Status (1)

Country Link
US (1) US2178696A (en)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3619349A (en) * 1968-12-16 1971-11-09 Pulp Paper Res Inst Bleaching of shredded or fluffed cellulosic pulp with gaseous chlorine monoxide
US4504456A (en) * 1983-08-29 1985-03-12 Quantum Technologies, Inc. Process and apparatus for the manufacture of hyprochlorous acid
US4584178A (en) * 1984-11-16 1986-04-22 Quantum Teechnologies, Inc. Apparatus for the manufacture of hypochlorous acid
WO1987003313A1 (en) * 1985-11-25 1987-06-04 Quantum Technologies, Inc. Bleaching process and composition
US5792316A (en) * 1992-02-28 1998-08-11 International Paper Company Bleaching process for kraft pulp employing high consistency chlorinated pulp treated with gaseous chlorine and ozone
US20070119556A1 (en) * 2003-09-23 2007-05-31 Zheng Tan Chemical activation and refining of southern pine kraft fibers
US8282774B2 (en) 2005-05-02 2012-10-09 International Paper Company Ligno cellulosic materials and the products made therefrom
US9512561B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US9512237B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Method for inhibiting the growth of microbes with a modified cellulose fiber
US9512563B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Surface treated modified cellulose from chemical kraft fiber and methods of making and using same
US9511167B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US9951470B2 (en) 2013-03-15 2018-04-24 Gp Cellulose Gmbh Low viscosity kraft fiber having an enhanced carboxyl content and methods of making and using the same
US10138598B2 (en) 2013-03-14 2018-11-27 Gp Cellulose Gmbh Method of making a highly functional, low viscosity kraft fiber using an acidic bleaching sequence and a fiber made by the process
US10865519B2 (en) 2016-11-16 2020-12-15 Gp Cellulose Gmbh Modified cellulose from chemical fiber and methods of making and using the same
US11332886B2 (en) 2017-03-21 2022-05-17 International Paper Company Odor control pulp composition

Cited By (34)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3619349A (en) * 1968-12-16 1971-11-09 Pulp Paper Res Inst Bleaching of shredded or fluffed cellulosic pulp with gaseous chlorine monoxide
US4504456A (en) * 1983-08-29 1985-03-12 Quantum Technologies, Inc. Process and apparatus for the manufacture of hyprochlorous acid
US4584178A (en) * 1984-11-16 1986-04-22 Quantum Teechnologies, Inc. Apparatus for the manufacture of hypochlorous acid
WO1987003313A1 (en) * 1985-11-25 1987-06-04 Quantum Technologies, Inc. Bleaching process and composition
US4740212A (en) * 1985-11-25 1988-04-26 Quantum Technologies, Inc. Process and composition for bleaching cellulosic material with hypochlorous acid
US5792316A (en) * 1992-02-28 1998-08-11 International Paper Company Bleaching process for kraft pulp employing high consistency chlorinated pulp treated with gaseous chlorine and ozone
US20070119556A1 (en) * 2003-09-23 2007-05-31 Zheng Tan Chemical activation and refining of southern pine kraft fibers
US20090054863A1 (en) * 2003-09-23 2009-02-26 Zheng Tan Chemical activation and refining of southern pine kraft fibers
US8262850B2 (en) 2003-09-23 2012-09-11 International Paper Company Chemical activation and refining of southern pine kraft fibers
US8282774B2 (en) 2005-05-02 2012-10-09 International Paper Company Ligno cellulosic materials and the products made therefrom
US8753484B2 (en) 2005-05-02 2014-06-17 International Paper Company Ligno cellulosic materials and the products made therefrom
US10907304B2 (en) 2005-05-02 2021-02-02 International Paper Company Ligno cellulosic materials and the products made therefrom
US9777432B2 (en) 2009-05-28 2017-10-03 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
USRE49570E1 (en) 2009-05-28 2023-07-04 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US9512562B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US9511167B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US9512237B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Method for inhibiting the growth of microbes with a modified cellulose fiber
US9909257B2 (en) 2009-05-28 2018-03-06 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US9926666B2 (en) 2009-05-28 2018-03-27 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US10731293B2 (en) 2009-05-28 2020-08-04 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US9970158B2 (en) 2009-05-28 2018-05-15 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US10106927B2 (en) 2009-05-28 2018-10-23 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US9512561B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US9512563B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Surface treated modified cellulose from chemical kraft fiber and methods of making and using same
US11111628B2 (en) 2009-05-28 2021-09-07 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US10138598B2 (en) 2013-03-14 2018-11-27 Gp Cellulose Gmbh Method of making a highly functional, low viscosity kraft fiber using an acidic bleaching sequence and a fiber made by the process
US10174455B2 (en) 2013-03-15 2019-01-08 Gp Cellulose Gmbh Low viscosity kraft fiber having an enhanced carboxyl content and methods of making and using the same
US10753043B2 (en) 2013-03-15 2020-08-25 Gp Cellulose Gmbh Low viscosity kraft fiber having an enhanced carboxyl content and methods of making and using the same
US10550516B2 (en) 2013-03-15 2020-02-04 Gp Cellulose Gmbh Low viscosity kraft fiber having an enhanced carboxyl content and methods of making and using the same
US10294614B2 (en) 2013-03-15 2019-05-21 Gp Cellulose Gmbh Low viscosity kraft fiber having an enhanced carboxyl content and methods of making and using the same
US9951470B2 (en) 2013-03-15 2018-04-24 Gp Cellulose Gmbh Low viscosity kraft fiber having an enhanced carboxyl content and methods of making and using the same
US10865519B2 (en) 2016-11-16 2020-12-15 Gp Cellulose Gmbh Modified cellulose from chemical fiber and methods of making and using the same
US11332886B2 (en) 2017-03-21 2022-05-17 International Paper Company Odor control pulp composition
US11613849B2 (en) 2017-03-21 2023-03-28 International Paper Company Odor control pulp composition

Similar Documents

Publication Publication Date Title
US2178696A (en) Material treatment
US2129719A (en) Bleaching method
US2166330A (en) Method of bleaching
EP0246314A1 (en) Bleaching process and composition
US3020197A (en) Method for production of high brightness high strength wood pulps
US2147618A (en) Method of bleaching pulp
US1298552A (en) Process of bleaching.
US2249646A (en) Bleaching cellulose with titanium compounds
US2772138A (en) Continuous bleaching process
US2195302A (en) Bleaching pulp
US2235837A (en) Bleaching cellulose
US2170108A (en) Stabilized hypochlorite solution and method therefor
US2203205A (en) Method of bleaching pulp
US2119519A (en) Process of bleaching cellulose
US2140863A (en) Process for producing a pure white cellulose
US2070893A (en) Process for improving the color of wood pulp
US2938826A (en) Bleaching of cellulosic pulp
JPS6024875B2 (en) Improved oxygen/alkali delignification process for wood pulp
US4409066A (en) Bleaching procedure using chlorine dioxide and chlorine solutions
US2727804A (en) Bleaching of polyamides
US3481826A (en) Process for bleaching wood pulp with fluorine,hydrofluoric acid,and oxygen difluoride
US2202331A (en) Treatment of textiles
US2424797A (en) Process for the purification of cellulosic material
US3481827A (en) Process for bleaching wood pulp with fluorine,hydrofluoric acid,and oxygen difluoride
US2202334A (en) Treatment of textiles