US2203205A - Method of bleaching pulp - Google Patents

Method of bleaching pulp Download PDF

Info

Publication number
US2203205A
US2203205A US167902A US16790237A US2203205A US 2203205 A US2203205 A US 2203205A US 167902 A US167902 A US 167902A US 16790237 A US16790237 A US 16790237A US 2203205 A US2203205 A US 2203205A
Authority
US
United States
Prior art keywords
pulp
bleaching
chlorine
hypochlorite
treatment
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
US167902A
Inventor
Francis G Rawling
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.)
West Virginia Pulp and Paper Co
Original Assignee
West Virginia Pulp and Paper 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 West Virginia Pulp and Paper Co filed Critical West Virginia Pulp and Paper Co
Priority to US167902A priority Critical patent/US2203205A/en
Application granted granted Critical
Publication of US2203205A publication Critical patent/US2203205A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/10Bleaching ; Apparatus therefor
    • D21C9/12Bleaching ; Apparatus therefor with halogens or halogen-containing compounds

Definitions

  • My present invention relates to bleaching of pulp especially of the types known as suliite, soda, kraft, monosulte and the semi-cooked pulps.
  • bleaching pulps of these types it is custom- 5 ary to treat the pulp with chlorine or other bleaching agents up to around 70% of the total chemicals required to bleach to a white color, and then wash the pulp.
  • the washed pulp is then treated with an alkali such as caustic soda, lime,
  • the number of washing steps required in the treatment above outlined adds substantially to the cost of the treatment.
  • I eliminate a number of these washing steps by changing the character of the' bleaching solution simply by altering the pH of the solution through a substantial range, as for example, by carrying out a hypochlorite bleach at a pH of not less than 8, and then by adding acid, converting the bleach into hypochlorous acid, HClO, at a pH of approximately 7, and then upon further addition of acid to elemental chlorine at a pH of 5, time being allowed for reaction on the pulp at these hydrogen ion concentrations.
  • the pH is then changed to the alkaline side by addition of sodium hydroxide, for example, thereby reversing the cycle and ending up with sodium hypochlorite. If necessary, this pH cycle may lbe repeaied.
  • the material is then washed and is ready for the beaters.
  • a suitable lquantity of kraft pulp is treated with about 5 to 8% of its weight with calcium hypochlorite solution at a pulp consistency of around 5%, Without washing, enough chlorine is added so that a slight excess remains .at the .end of thirty minutes treatment.
  • the pulp is then washed, treated with caustic soda until the pH of the pulp remains about 10 to 11.
  • the pulp is then washed and is then submitted to alternate bleaching treatments as follows:
  • a hypochlorite solution about 3% on the weight of the pulp is added to the pulp suspension, is mixed for a period of about ten minutes, where- -upon sulfuric acid is added until the pH of the pulp reaches a nal valueof around 5.
  • free chlorine will be present in the pulp in accordance with the following equation:
  • hypochlorite should be added prior to the acidication so as to aiord suilcient chlorine to carry through the cycleY of pH change. If in- 25 suflicient hypochlorite is present, more should be added to the pulp. In place of hypochlorites, chlorine may be added to the pulp, since it will form hypochlorites when the pulp is alkaline.
  • the bleaching action can be further 30 intensified by blowing air into the pulp, since the dissolved oxygen removes coloring material from the pulp in the presence of alkali, as described and claimed in my copending application, Serial No. 72,059, referred April 1, 1936, Patent Num- 35 ber 2,147,618 patented February 14, 1939.
  • hypochlorites are formed and the cycle of change of pH value of the pulp from 10 or thereabouts to 5 and back to 10 can be made by the alternate addition of acid and alkali until the desired color 50 or whiteness is obtained, after which the pulp ls washed.
  • the method of carrying out an after-bleach comprising subjecting the partially bleached pulp to alternate treatments with chlorine and alkaline hypochlorite, without Washing between the treatments, by rst treating the pulp by adding one of said compounds (chlorine or hypochlorite) to the pulp in an amount in excess of that required to complete the bleaching in one stage, and thereafter appropriately varying the pH of the treated pulp by adding alkali in the case of chlorine treatment and acid in the case of the hypochlorlte treatment to produce a pH over a range of from an excess of 9 to not substantially more than 5 to form the other compound in situ from said excess of the rst compound, and alternately ycontinuing such treatments each for a period on the order of from 10-15 minutes, whereby the pulp in the afterbleach is subjected to a series of comparatively rapid continuously oxidizing

Description

June 4, 1940. F G, RAWLlNG 2,203,205
METHOD 0F BLEACHINGPULP Filed Oct. 8, 1937 Patented June 4, 1940 PATENT OFFICE METHOD OF BLEACHING PULP Francis G. Rawling, Piedmont, W. Va., assigner to West Virginia Pulp & Paper Company, New York, N. Y., a corporation of Delaware Application October 8, 1937, Serial No. 167,902
1 Claim.
My present invention relates to bleaching of pulp especially of the types known as suliite, soda, kraft, monosulte and the semi-cooked pulps.
In bleaching pulps of these types it is custom- 5 ary to treat the pulp with chlorine or other bleaching agents up to around 70% of the total chemicals required to bleach to a white color, and then wash the pulp. The washed pulp is then treated with an alkali such as caustic soda, lime,
sodium carbonate, etc., at room or elevated temperatures to remove lignin material and bleach residues. The pulp is again washedl and submitted to further treatments with hypochlorites either under neutral or alkaline conditions, for
periods of time up to six hours, with a washing 'step between each treatment, until the pulp has attained a suicient degree of whiteness.
The number of washing steps required in the treatment above outlined adds substantially to the cost of the treatment. According to my present invention I eliminate a number of these washing steps by changing the character of the' bleaching solution simply by altering the pH of the solution through a substantial range, as for example, by carrying out a hypochlorite bleach at a pH of not less than 8, and then by adding acid, converting the bleach into hypochlorous acid, HClO, at a pH of approximately 7, and then upon further addition of acid to elemental chlorine at a pH of 5, time being allowed for reaction on the pulp at these hydrogen ion concentrations. The pH is then changed to the alkaline side by addition of sodium hydroxide, for example, thereby reversing the cycle and ending up with sodium hypochlorite. If necessary, this pH cycle may lbe repeaied. The material is then washed and is ready for the beaters.
The invention is illustrated in the attached flowsheet which may be read with the following detailed description of a method of carrying out my invention according to a preferred embodiment thereof.
A suitable lquantity of kraft pulp is treated with about 5 to 8% of its weight with calcium hypochlorite solution at a pulp consistency of around 5%, Without washing, enough chlorine is added so that a slight excess remains .at the .end of thirty minutes treatment. The pulp is then washed, treated with caustic soda until the pH of the pulp remains about 10 to 11. The pulp is then washed and is then submitted to alternate bleaching treatments as follows:
A hypochlorite solution about 3% on the weight of the pulp is added to the pulp suspension, is mixed for a period of about ten minutes, where- -upon sulfuric acid is added until the pH of the pulp reaches a nal valueof around 5. At this stage free chlorine will be present in the pulp in accordance with the following equation:
2Naoc1+Hzsoi-NazsoH-mocl 5 with further addition of acid,
Hoc1+Nac1+H2so4 NaHsol+H2o+C12 If calcium hypochlorite is used the reaction is 10 similar.
After maintaining the solution acid for approximately 15 minutes, alkali is added until the, pH becomes preferably between 9 and 10 and the solution held at this stage for approximately an- Il other 15 minutes. 'I'he pulp is then washed and, if necessary, again treated with a small quantity of hypochlorite and/or chlorine.
'I'he treatment of the pulp may be made on batches of pulp or in a continuous bleaching sys- 20 tem by the addition of the acid and alkali at proper points in the continuous apparatus. Enough hypochlorite should be added prior to the acidication so as to aiord suilcient chlorine to carry through the cycleY of pH change. If in- 25 suflicient hypochlorite is present, more should be added to the pulp. In place of hypochlorites, chlorine may be added to the pulp, since it will form hypochlorites when the pulp is alkaline.
If desired the bleaching action can be further 30 intensified by blowing air into the pulp, since the dissolved oxygen removes coloring material from the pulp in the presence of alkali, as described and claimed in my copending application, Serial No. 72,059, iiled April 1, 1936, Patent Num- 35 ber 2,147,618 patented February 14, 1939.
An alternative method of bleaching following the initial treatment of the pulp with hypochlorite then with chlorine, followed by Washing, an alkaline treatment and a secondtwash is the reo placement of the hypochlorite -added to the pulp after the second wash, with chlorine. This chlorine should be added to the pulp in suicient quantity to carry through the cycles of change of pH values. Whenever the pH-value of the pulp 45 is raised to 9 or 10, or so by the addition of alkali,
' hypochlorites are formed and the cycle of change of pH value of the pulp from 10 or thereabouts to 5 and back to 10 can be made by the alternate addition of acid and alkali until the desired color 50 or whiteness is obtained, after which the pulp ls washed.
Various other changes maybe made in the specic example Without departing from the spirit of my invention or the scope of the appended claim. 55
I claim:
In the bleaching of pulp in which the pulp is subjected to a preliminary intensive treatment with a chlorine bleaching agent followed by alkali treatment and removal of the soluble bleach residues by Washing, the method of carrying out an after-bleach comprising subjecting the partially bleached pulp to alternate treatments with chlorine and alkaline hypochlorite, without Washing between the treatments, by rst treating the pulp by adding one of said compounds (chlorine or hypochlorite) to the pulp in an amount in excess of that required to complete the bleaching in one stage, and thereafter appropriately varying the pH of the treated pulp by adding alkali in the case of chlorine treatment and acid in the case of the hypochlorlte treatment to produce a pH over a range of from an excess of 9 to not substantially more than 5 to form the other compound in situ from said excess of the rst compound, and alternately ycontinuing such treatments each for a period on the order of from 10-15 minutes, whereby the pulp in the afterbleach is subjected to a series of comparatively rapid continuously oxidizing bleaching treatments each of which is alternately acid or alkaline, as the case may be.
FRANCIS G. RAWIING.
US167902A 1937-10-08 1937-10-08 Method of bleaching pulp Expired - Lifetime US2203205A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US167902A US2203205A (en) 1937-10-08 1937-10-08 Method of bleaching pulp

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US167902A US2203205A (en) 1937-10-08 1937-10-08 Method of bleaching pulp

Publications (1)

Publication Number Publication Date
US2203205A true US2203205A (en) 1940-06-04

Family

ID=22609285

Family Applications (1)

Application Number Title Priority Date Filing Date
US167902A Expired - Lifetime US2203205A (en) 1937-10-08 1937-10-08 Method of bleaching pulp

Country Status (1)

Country Link
US (1) US2203205A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2424797A (en) * 1943-12-18 1947-07-29 Niagara Alkali Company Process for the purification of cellulosic material
US2502410A (en) * 1945-11-17 1950-04-04 Olin Mathieson Method of bleaching cellulosic materials
US2513787A (en) * 1947-01-31 1950-07-04 Brown Co Bleaching treatment for cellulosic materials
US2805118A (en) * 1953-08-07 1957-09-03 Lawrence Walter Phalti Multistage process bleaching of alkaline-process wood pulps including an acid sour between two terminal alkaline hypochlorite stages
US2850399A (en) * 1954-10-14 1958-09-02 Blanco Alfredo Bernardo Process for elaborating a material based on cactaceous woody texture
US2865701A (en) * 1953-12-07 1958-12-23 Nat Distillers Chem Corp Process of bleaching kraft pulp with alkaline hypochlorite bleach acidifying the pulp containing residual chlorine and then bleaching with alkaline peroxide
US3377235A (en) * 1964-12-03 1968-04-09 Scott Paper Co Process for bleaching multi-colored broke with hypochlorites

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2424797A (en) * 1943-12-18 1947-07-29 Niagara Alkali Company Process for the purification of cellulosic material
US2502410A (en) * 1945-11-17 1950-04-04 Olin Mathieson Method of bleaching cellulosic materials
US2513787A (en) * 1947-01-31 1950-07-04 Brown Co Bleaching treatment for cellulosic materials
US2805118A (en) * 1953-08-07 1957-09-03 Lawrence Walter Phalti Multistage process bleaching of alkaline-process wood pulps including an acid sour between two terminal alkaline hypochlorite stages
US2865701A (en) * 1953-12-07 1958-12-23 Nat Distillers Chem Corp Process of bleaching kraft pulp with alkaline hypochlorite bleach acidifying the pulp containing residual chlorine and then bleaching with alkaline peroxide
US2850399A (en) * 1954-10-14 1958-09-02 Blanco Alfredo Bernardo Process for elaborating a material based on cactaceous woody texture
US3377235A (en) * 1964-12-03 1968-04-09 Scott Paper Co Process for bleaching multi-colored broke with hypochlorites

Similar Documents

Publication Publication Date Title
US3193445A (en) Method of bleaching cellulosic materials with hydrogen peroxide
KR850001341B1 (en) Process for the treatment of chemical paper pulps
US2203205A (en) Method of bleaching pulp
US2147618A (en) Method of bleaching pulp
JP5232164B2 (en) Process for bleaching chemical paper pulp by final ozone treatment at high temperature
US2203212A (en) Bleaching pulp
US2140863A (en) Process for producing a pure white cellulose
US2779656A (en) Bleaching of kraft pulp
PT96816B (en) PAPER PASTE BLEACHING PROCESS
US4132589A (en) Delignification and bleaching of cellulose pulp
US3622444A (en) Pulp bleaching process
US1908481A (en) Method of bleaching fibers
US1953191A (en) Process of refining cellulose
US1768819A (en) Bleaching
US2202334A (en) Treatment of textiles
US2030384A (en) Method of bleaching pulp
US2049676A (en) Process of treating bleached pulp
US2178649A (en) Process for bleaching wood pulp
US2239606A (en) Method of bleaching kraft pulp
US2127765A (en) Bleaching pulp
US2424797A (en) Process for the purification of cellulosic material
US2001268A (en) Pulp treating process
US2202331A (en) Treatment of textiles
US3481827A (en) Process for bleaching wood pulp with fluorine,hydrofluoric acid,and oxygen difluoride
US1968223A (en) Process of treating paper pulp