US2359782A - Bleaching process and composition - Google Patents

Bleaching process and composition Download PDF

Info

Publication number
US2359782A
US2359782A US386083A US38608341A US2359782A US 2359782 A US2359782 A US 2359782A US 386083 A US386083 A US 386083A US 38608341 A US38608341 A US 38608341A US 2359782 A US2359782 A US 2359782A
Authority
US
United States
Prior art keywords
bleaching
glucosate
bleached
fibers
cold
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
US386083A
Inventor
Ralph R Oliver
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.)
Lockport Cotton Batting Co
Original Assignee
Lockport Cotton Batting 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 Lockport Cotton Batting Co filed Critical Lockport Cotton Batting Co
Priority to US386083A priority Critical patent/US2359782A/en
Application granted granted Critical
Publication of US2359782A publication Critical patent/US2359782A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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
    • D21C9/1026Other features in bleaching processes
    • D21C9/1036Use of compounds accelerating or improving the efficiency of the processes
    • 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

Definitions

  • This invention relates to the bleaching of cellulose fibers, such as exist in cotton textiles and in cotton and wood pulp for example.
  • halogen containing, bleaching agents such as sodium and calcium hypochlorites, for example,
  • this improved process is particularly advantageous because an analysis of pulp bleached by this improved process shows adecrease of from sixteen to thirtythree percent less ash, apparently through the prevention of the'adherence of encrusting materials to the bleached fibers.
  • cellulose fibers of any kind which are bleached in the presence of the inorganic beta cause they are 'free from encrusting chemicals or matter.
  • glucosates are preferably the insmples of such glucosates which-I have found very satisfactory forv this .purpose and which are glucosates have a better luster and greater bril- "liancy than can be obtained by the bleaching processes heretofore employed, apparently bematerials. Equally satisfactory results are ob 'tained inthe bleaching of chemical wood pulp colloidal particles around theencrusting mineral I obtained by the d P the Qulphate P ess and modifications of the sulphate process knownastheKraft process where the manufac-, ture' ofa strong paper .sheetis required.
  • the glucosates are preferably the insmples of such glucosates which-I have found very satisfactory forv this .purpose and which are glucosates have a better luster and greater bril- "liancy than can be obtained by the bleaching processes heretofore employed, apparently bematerials. Equally satisfactory results are ob 'tained inthe bleaching
  • Glucosates of this type may be coagulated by bi-valent ionsand apparl 'ently form colloidal particles or insoluble hydro philic -gels around the encrustingmineral and crustation'forming.
  • the fibers may be sepa.-
  • rated from the cellulose fibers byfdraining be the bath-with the suspended colloids and washing commonlyencountered in a bleaching bath are calcium, magnesium, silicon, iron, carbonates sulphates and organic materials suchas oils, fats,
  • the proportions cf the glucosateto be employed may be varied to' 'some extentpdepending upon the character of the fibers and of the encrusting materials that may be Present, as determined by ionic analysis.
  • glucosates may be formed may be represented by bon ra dical depending upon the material from which the glucoside is formed:
  • Beta glucosldc O CHARCHOH-CHOH-lH-CHOH-CHzOH Glucosates formed from such a glucoside and which are excellent catalysts and inhibiting ma-' terials in the present process are:
  • Example A 50 grams of caustic boiled and washed cotton linters treated for three hours with 400 ml. of
  • Example B 50 grams of the same caustic boiled and washed cotton linters treated for three hours with 460 ml. of cold calcium hypochlorite containing 6 grams per litre of active chlorine and entrained in this solution 25 P. P. M; (parts per million) of tetra-phospho-glucosate.
  • Example D 50 grams of the same caustic boiled and washed cotton llnters treated for three hours with 400 ml. of cold calcium hypochlorite containing 6 grams per litre of active chlorine and entrained in this solution 50 P. P. M. (parts per million) of tetra-phospho-glucosate.
  • Example E Procedure asin Example D, withan entrainment of 100 P. P. M. (parts per phospho-glucosate.
  • Example F Procedure as in Example D, with an entrainment of 10 P. P. M. (parts per million) of tetraphospho-glucosate.
  • Comparison of Examples E and F shows the extremes ofentrainment of tetra-phospho-glucosate for this particular grade of cotton linters.
  • the amount to be used will vary with different grades of stock to be bleached.
  • beta glucosates appear to be irreversible colloids which react with alkali and alkaline earth metals to form insoluble hydrophilic gels.
  • An improved method oi. cold bleaching of cellulose fibers which comprises subjecting the material to be bleached to the action at the same time, of a hypochlorite bleaching agent and a preformed inorganic glucosate of the type which will be coagulated by bi-valent ions to form colloidal particles.
  • An improved method of cold bleaching cellulose fibers in a minimum time interval which comprises subjecting the fibers to a hypochlorite bleaching agent in the presence of a preformed inorganic beta glucosate- I 3.
  • An improved method of cold bleaching cellulose fibers in a minimum time interval which comprises subjecting the fibers to a halogen containing, .bleaching. .compound combined with a member of the group consisting of alkali and alkaline earth metals in the presence of a preformed inorganic beta glucosate.
  • An improved methodcf cold bleaching or cellulose fibrous materials which comprises subjecting the materials to bebleached to the action million) of tetraparticles and containing an at the same time in a bleaching bath of a hypochlorite, bleaching agent and preformed tetraphospho-glucosate.
  • An improved method of cold bleaching of fibers of Vegetable origin which comprises subjecting the fibers to be bleached to a bleaching bath having in solution therein a calcium hypochlorite bleaching agent and preformed tetraphospho-glucosate.
  • the method of cold bleaching of fibers of vegetable origin which comprises subjecting the fibers to be bleached to a bleaching bath, containing a calcium hypochlorite bleaching agent and a preformed inorganic glucosate capable of, coagulation by bi-valent ions to form colloidal particles and combined with a salt of phosphoric acid.
  • a bleaching composition operable for the cold bleaching of cellulose fibers in a manner to give the bleached fibers a good luster, a high brilliancy, and freedom from encrusting materials which comprises a mixture of a hypochlorite bleaching agent and a preformed agent contaim ing an inorganic beta glucosate and capable of coagulation by bi-valent ions to form colloidal agent combined with a member of the group consisting of alkali and alkaline earth metals, and a preformed agent containing a glucosate combined with an inorganic salt and capable of coagulation by bi-valent ions to form colloidal particles.
  • a bleaching composition operable for cold rials which comprises, a mixture of a halogen containing bleaching. agent combined with a member of the group consisting ofalkali and alkaline earth metals and a preformed agent containing tetra-phospho-glucosate.
  • a bleaching composition operable for the cold bleaching of cellulose fibers in a manner to give the bleached fibers a good luster, a high brilliancy, and freedom from encrusting materials which comprises a mixture of a calcium hypochlorite bleaching agent and a preformed agent containing tetra-phospho-glucosate.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Textile Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Paper (AREA)
  • Chemical Or Physical Treatment Of Fibers (AREA)
  • Detergent Compositions (AREA)

Description

smscnma rn'oosss comosrrron Ralph E. Oliver, Lockpoi't, N. n, assignor to Lockport Cotton Batting (30., Lockport, N. X.
No Drawing. Application March 31, 194i,
Serial No. 386,083
14 Claims. (c 252-137) This invention relates to the bleaching of cellulose fibers, such as exist in cotton textiles and in cotton and wood pulp for example. Heretofore, halogen containing, bleaching agents, such as sodium and calcium hypochlorites, for example,
have been employed extensively in solutionsto bleach cellulose fibers, but results have not been entirely satisfactory due to the adherence to, or
deposit upon, the cellulose fibers of encrusting materials during the bleaching process. Such deposits are objectionable because they weaken 'cr embrittle the bleached fibers and destroy or erated and a bleached product of better quality obtained by performing the bleaching action with a. halogen containing, bleaching agent in the presence of an inorganic .glucosate which may be coagulated by bi-valent ions so as to form that their action may be re arded' as a state and not a form of matter, an that the action is I apparently physical as well as chemical.
In the manufacture of so called chemical cot-' ton and chemical cellulose from wood pulp where a low ash is of primeimportance, this improved process is particularly advantageous because an analysis of pulp bleached by this improved process shows adecrease of from sixteen to thirtythree percent less ash, apparently through the prevention of the'adherence of encrusting materials to the bleached fibers. I have also found .,that cellulose fibers of any kind which are bleached in the presence of the inorganic beta cause they are 'free from encrusting chemicals or matter. These glucosatesare preferably the insmples of such glucosates which-I have found very satisfactory forv this .purpose and which are glucosates have a better luster and greater bril- "liancy than can be obtained by the bleaching processes heretofore employed, apparently bematerials. Equally satisfactory results are ob 'tained inthe bleaching of chemical wood pulp colloidal particles around theencrusting mineral I obtained by the d P the Qulphate P ess and modifications of the sulphate process knownastheKraft process where the manufac-, ture' ofa strong paper .sheetis required. The
fibers' .bleached"by this improved method have typical of materials of this type are sodium-glucosate, phospho-glucosate, pyro-glucosate and tetra-phospho -glucosateh Glucosates of this type may be coagulated by bi-valent ionsand apparl 'ently form colloidal particles or insoluble hydro philic -gels around the encrustingmineral and crustation'forming. elements in what: may be of cotton tha'tis tobe' fabricated by carding greaterstrength' thanv has heretofore been possible, because they are not 'embrittled by any encrusting- 'scal e'or chemicals, and hence this process'ls'fi'lfio-llarticularly useful for the bleachand garnetting, where fiber strength is important.
p 1 have also discovered that these same inorganic other foreign matter-and holdthe scale :or enaptly termed. delayed. precipitation during the; bleaching process.- Thus, the glucosates convert the materials in the bleaching solutionand. on d the fiberswhich would normally. tend to form,
an encrustation on the fibers, into, nonadherent I suspensoids'which hold the encrusting materials in the form of suspended colloids and remain in' suspension in the liquid bleaching bath. After the bleaching action, the colloids may be sepa.-
rated from the cellulose fibers byfdraining be the bath-with the suspended colloids and washing commonlyencountered in a bleaching bath are calcium, magnesium, silicon, iron, carbonates sulphates and organic materials suchas oils, fats,
waxes; and living organisms; While'theexact H y heta glucosides from which satisfactory inorganic beta glucosatesapparently act as catalysts on the bleaching action and byspeeding up the bleaching. reaction, the time required for a bleaching action is materially decreased. The proportions cf the glucosateto be employed may be varied to' 'some extentpdepending upon the character of the fibers and of the encrusting materials that may be Present, as determined by ionic analysis. Generally, excellent results may be obtained by "usingffrom one to one hundred parts by weight or the-glucosate per million parts of the hypochlorite bleaching solution, but ordinarily, it is unnecessary to use more than twentyfive parts of glucosate permillion parts of are sufliciently identified by these names, but as action 01 these inorganic beta 'glucosates. in in hibiting'the deposits of encrusting materials upon the fibers is not definitely known, it is believed the following formula inwhich R is a hydrocara matter fbfjrcorfd, and byway of, example, the
glucosates may be formed may be represented by bon ra dical depending upon the material from which the glucoside is formed:
Beta glucosldc O CHARCHOH-CHOH-lH-CHOH-CHzOH Glucosates formed from such a glucoside and which are excellent catalysts and inhibiting ma-' terials in the present process are:
Scdium-glucosate CHO R- CH ONa-CHOH-bH- CH ONa' CHzOH Phospho-glucosate O CIEO R- CHOH-CHOII-CH-CHOPzOeNm CHzOH Tetra-phospho-glucosate inc n-ononcnon-oh -onNairioncnion In order to further explain the nature of my discovery, reference may be had to the followingspecific examples in which the discovery is given practical application:
Example A 50 grams of caustic boiled and washed cotton linters treated for three hours with 400 ml. of
cold calcium hypochlorite containing 6 grams.
per litre of active chlorine.
After bleaching the stock was washed free from v active chlorine anddried to bone dry base.
The stock bleached toa brightness of 70 G. E. .(The brightness of a standard magnesia block being. 100 G. E.) v
Ash contents-0.75%.
Example B 50 grams of the same caustic boiled and washed cotton linters treated for three hours with 460 ml. of cold calcium hypochlorite containing 6 grams per litre of active chlorine and entrained in this solution 25 P. P. M; (parts per million) of tetra-phospho-glucosate.
After bleaching, the stock was washed free from active chlorine and dried to bone dry base.
The stock bleached to a brightness of 75 G. E.
Ash contents-0.63%.
Comparison of Results 'A and B Example D 50 grams of the same caustic boiled and washed cotton llnters treated for three hours with 400 ml. of cold calcium hypochlorite containing 6 grams per litre of active chlorine and entrained in this solution 50 P. P. M. (parts per million) of tetra-phospho-glucosate.
After bleaching, the stock was washed free from active chlorine and dried to bone dry base.
Stock bleached to a brightness of '75 G. E.
Ash contents-0.51%.
Comparison of Results C and D Difference in brightness-7%. Difference in ash-30%.
Example E Procedure asin Example D, withan entrainment of 100 P. P. M. (parts per phospho-glucosate.
Stock bleached to a brightness of 75 G. E.
Ash contents-0.52%.
Example F Procedure as in Example D, with an entrainment of 10 P. P. M. (parts per million) of tetraphospho-glucosate.
Stock bleached to a brightness of G. E.
Ash contents0.655%.
Comparison of Examples E and F shows the extremes ofentrainment of tetra-phospho-glucosate for this particular grade of cotton linters.
The amount to be used will vary with different grades of stock to be bleached.
In each example using'tetra-phospho-glucosate the cotton reached a brightness of 70 G. E. in two and one-half hours.
The beta glucosates appear to be irreversible colloids which react with alkali and alkaline earth metals to form insoluble hydrophilic gels.
It will be understood that various changes in the details, materials and steps which have been hereinabove described in order to explain the nature of my invention, may be made by those skilled in the art within the principle and scope of the invention, as expressed in the appended claims.
I claim as my invention:
1. An improved method oi. cold bleaching of cellulose fibers which comprises subjecting the material to be bleached to the action at the same time, of a hypochlorite bleaching agent and a preformed inorganic glucosate of the type which will be coagulated by bi-valent ions to form colloidal particles.
2,. An improved method of cold bleaching cellulose fibers in a minimum time interval which comprises subjecting the fibers to a hypochlorite bleaching agent in the presence of a preformed inorganic beta glucosate- I 3. An improved method of cold bleaching cellulose fibers in a minimum time interval which comprises subjecting the fibers to a halogen containing, .bleaching. .compound combined with a member of the group consisting of alkali and alkaline earth metals in the presence of a preformed inorganic beta glucosate.
4. An improved methodof cold bleaching celcomprises subjecting the material to be bleached to the action, at the same time, Ms hypochlorite bleaching agent and a preformed inorganic glucosate capable of coagulation by bi-valent ions to form colloidal alkali metal.
6. An improved methodcf cold bleaching or cellulose fibrous materials which comprises subiecting the materials to bebleached to the action million) of tetraparticles and containing an at the same time in a bleaching bath of a hypochlorite, bleaching agent and preformed tetraphospho-glucosate.
'7. An improved method of cold bleaching of fibers of Vegetable origin which comprises subjecting the fibers to be bleached to a bleaching bath having in solution therein a calcium hypochlorite bleaching agent and preformed tetraphospho-glucosate.
8. The method of cold bleaching of fibers of vegetable origin which comprises subjecting the fibers to be bleached to a bleaching bath, containing a calcium hypochlorite bleaching agent and a preformed inorganic glucosate capable of, coagulation by bi-valent ions to form colloidal particles and combined with a salt of phosphoric acid.
9. A bleaching composition operable for the cold bleaching of cellulose fibers in a manner to give the bleached fibers a good luster, a high brilliancy, and freedom from encrusting materials, which comprises a mixture of a hypochlorite bleaching agent and a preformed agent contaim ing an inorganic beta glucosate and capable of coagulation by bi-valent ions to form colloidal agent combined with a member of the group consisting of alkali and alkaline earth metals, and a preformed agent containing a glucosate combined with an inorganic salt and capable of coagulation by bi-valent ions to form colloidal particles.
11. A bleaching composition operable for cold rials, which comprises, a mixture of a halogen containing bleaching. agent combined with a member of the group consisting ofalkali and alkaline earth metals and a preformed agent containing tetra-phospho-glucosate.
14. A bleaching composition operable for the cold bleaching of cellulose fibers in a manner to give the bleached fibers a good luster, a high brilliancy, and freedom from encrusting materials, which comprises a mixture of a calcium hypochlorite bleaching agent and a preformed agent containing tetra-phospho-glucosate.
RALPH R. OLIVER.
US386083A 1941-03-31 1941-03-31 Bleaching process and composition Expired - Lifetime US2359782A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US386083A US2359782A (en) 1941-03-31 1941-03-31 Bleaching process and composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US386083A US2359782A (en) 1941-03-31 1941-03-31 Bleaching process and composition

Publications (1)

Publication Number Publication Date
US2359782A true US2359782A (en) 1944-10-10

Family

ID=23524089

Family Applications (1)

Application Number Title Priority Date Filing Date
US386083A Expired - Lifetime US2359782A (en) 1941-03-31 1941-03-31 Bleaching process and composition

Country Status (1)

Country Link
US (1) US2359782A (en)

Similar Documents

Publication Publication Date Title
US2583548A (en) Production of pigmented cellulosic pulp
US2194956A (en) Bleaching pulp
US2178696A (en) Material treatment
US2280307A (en) Process of manufacturing paper
US3878037A (en) Method of enhancing the hypochlorite bleaching of pulp
US1923292A (en) Purification of cellulose material
US2354838A (en) Waxy starch product and method of making
US2147618A (en) Method of bleaching pulp
US2359782A (en) Bleaching process and composition
US2036606A (en) Chemical purification and modification of cellulose fiber
US2920011A (en) Elevated temperature and pressure two stage hypochlorite peroxide pulp bleaching process
US2772138A (en) Continuous bleaching process
US1880046A (en) Processing of cellulose fiber
US2120678A (en) Bleaching and purifying process
US2625474A (en) Acid-alkali process for the preparation of cellulose fibers
US2161763A (en) Process of making paper pulp
US2203205A (en) Method of bleaching pulp
KR20200074477A (en) Manufacturing method of cotton pulp and cotton pulp thereof
US1522561A (en) Bleaching solution
US2694631A (en) Process of preparing wood pulp
US2140863A (en) Process for producing a pure white cellulose
US2018276A (en) Art of treating vegetable fibers
US2397389A (en) Method for bleaching shellac
US2502330A (en) Washing paper pulp to remove coloring matter
US1741540A (en) Process for the production of high-alpha cellulose fiber for the manufacture of cellulose derivatives