US1824837A - Papermaking composition - Google Patents

Papermaking composition Download PDF

Info

Publication number
US1824837A
US1824837A US407569A US40756929A US1824837A US 1824837 A US1824837 A US 1824837A US 407569 A US407569 A US 407569A US 40756929 A US40756929 A US 40756929A US 1824837 A US1824837 A US 1824837A
Authority
US
United States
Prior art keywords
pulp
fibered
white
alpha cellulose
long
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
US407569A
Inventor
George A Richter
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.)
Brown Co
Original Assignee
Brown 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 Brown Co filed Critical Brown Co
Priority to US407569A priority Critical patent/US1824837A/en
Application granted granted Critical
Publication of US1824837A publication Critical patent/US1824837A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H11/00Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/16Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only modified by a particular after-treatment
    • D21H11/20Chemically or biochemically modified fibres

Definitions

  • This invention relates to apermaking compositions, being more particularly concerned with compositions which may be used in making high grade papers having a combination of desirable characteristics heretofore unattained by the use of ordinary papermaking furnishes.
  • long-'fibered stocks such as described must be treated in a manner to generate suflicient cellulose gel therein to impart the desired strength and folding endurance to the paper, as well as to reduce length of fiber sufliciently to result in a well-formed or closed in sheet.
  • T0 attain these results,-the papermaker subjects the stock to the action of a beater engine until it has acquired the desired gelatinized condition or slowness, and then passes it through a Jordan engine.
  • the Jordan engine cuts the fibers and so conditions them for improved paper formation, but the shortened fibers do not ofl'er as great resistance to tearing in the paper made therefrom as would the longfibered stock if employed as a raw material.
  • the Wood in chipped condition may be cooked in an acid sulphite liquor, for instance in the usual calcium base 1i uor containing1% combined and 5% free g0 or .in a sodium base liquor, to produce a cleaner and more easily bleachable pulp.
  • the cooking operation may be carried out at a temperature of about 275 to 285 F. for about nine to ten hours, during which time free SO may be released from the digester to maintain the pressure at about 75 pounds.
  • the digester contents may then be blown into a pit, and the raw woodpulp may be separated from the spent liquor by washing in the usual manner.
  • the raw pulp may be converted to a white product of high alpha cellulose content by'suitable-refining steps. To this end, it may initially be treated at room temperature for about two to three hours, with a liquor containin about 1% to 3% chlorine or 1% to 5% hypoc lorite bleach, based on the dry weight of pulp. Or, if desired, both a suitable chlorine water treatment and hypochlorite bleach liquor treatment may be employed.
  • the chlorine water and/or bleach liquor removes lignin and other coloring matter from the pulp, or renders such matter soluble in alkaline liquors.
  • the pulp is then washed, whereupon it may be treated with an alkaline liquor to remove chlorine reaction products and other nonalpha cellulose constituents from the pulp.
  • the ulp when mixed with long-fi
  • the ulp maybe treated at about 100 C. or at hig or temperature and under super-atmospheric pressure for about four to six hours, with a solution containing about 10% to 12% caustic soda, based on the weight of dry pulp.
  • the treatment may be effected at lower temperature with a more concentrated caustic soda solution, for instance at from 20 to 40 (1., for about two hours, in a solution containing 50% caustic soda, based on the weight of dry pulp.
  • the refined pulp may then be bleached with a suitable agent to the desired whiteness, for instance, with calcium orsodium hypochlorite bleach liquor, preferably containin sufiicient free alkali to ensure a condition 0 distinct alkalinity throughout the bleaching operation, as such a condition prevents the formation of oxycellulose and accordingly results in a white product of maximum alpha cellulose content and stability.
  • a permanganate bleach liquor may be employed, in which case the liquor should be maintained neutral or acid, in order to avoid degradation of fiber into oxycelluloses.
  • the short-fibered pulps may e ad ed in desired fproportion, say 10% to 25%, to suitable longbered stock, such as rag pulp or wood 'pulp of high alpha cellulose content derived rom long-fibere'd woods such as spruce, either before or after the long-fibered stock has been subjected to beating to produce cellulose gel in suflicient amount to impart the desired strength and folding endurance to the resultin paper.
  • suitable longbered stock such as rag pulp or wood 'pulp of high alpha cellulose content derived rom long-fibere'd woods such as spruce
  • a apermaking composition com rising a sta 1e, white, long-fibered pul of igh alpha. cellulose content and a su ordinate pro 'ortion of stable, white, poplar pulp of 'g alpha cellulose content.
  • a process which comprises forming a mixture of stable, white, long-fibered pulp of high alpha cellulose content in gelatimzed condition and stable, white, short-fibered wood pulp of high alpha cellulose content in free condition; and running off the m1xture into paper.
  • a process which comprises beating a stable, white lo'ng-fibered pulp to the desired slowness; mixin a subordinate proportion of unbeaten, stab e, white, poplar pulp therewith; and running off the mixture into paper.
  • Apapermakm composition comprising a blend of two cel ulose pulps, both being stable, white pulps of high alpha cellulose content, but one being derived from a longfibered cellulosic source, and the other being derived from a short-fibered cellulosic source.
  • Apapermakin composition comprising a blend of two woo pulps, both being stable, white pulps of high alpha cellulose content, but one being derived from a long-fibered wood of the type of spruce, and the other being derived from a short-fibered wood of the type of poplar.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Biochemistry (AREA)
  • Paper (AREA)

Description

Patented Sept. 29.19 31 {UNITED STATES. PATENT OFFICE GEORGE A.
RICHTER, OF BERLIN, NEW HAMPSHIRE, ASSIGNOR '10 BROWN COMPANY,
OF BERLIN, NEW HAMPSHIRE, A CORPORATION OF MAINE runnmxnm oonrosrrron Io Drawing.
This invention relates to apermaking compositions, being more particularly concerned with compositions which may be used in making high grade papers having a combination of desirable characteristics heretofore unattained by the use of ordinary papermaking furnishes.
In making the hi hest grade writing and printing papers, it has been the practice to use, as raw material, stable, white fibers, such as rag pulps or wood pulps of high alpha cellulose content derived from woods such as spruce. Because the fibers, of such pulps are comparatively lon they interfelt well on the apermaking mac ine and, because they are ree from non-alpha cellulose impurities, the resulting papers are resistant to the deterioratin action of air, heat and light, possessing w at is known in the art as high permanenc or good ageing qualities.
Before ormmg into paper, long-'fibered stocks such as described must be treated in a manner to generate suflicient cellulose gel therein to impart the desired strength and folding endurance to the paper, as well as to reduce length of fiber sufliciently to result in a well-formed or closed in sheet. T0 attain these results,-the papermaker subjects the stock to the action of a beater engine until it has acquired the desired gelatinized condition or slowness, and then passes it through a Jordan engine. The Jordan engine cuts the fibers and so conditions them for improved paper formation, but the shortened fibers do not ofl'er as great resistance to tearing in the paper made therefrom as would the longfibered stock if employed as a raw material.
In accordance with the present invention, a subordinate proportion of stable, white pulp of short fiber len th is used along with longfibered stocks suc as hereinbefore described, as the use of such a mixture of fibers makes possible dispensing with or minimizing the use of a Jordan engine, and the production of well-formed papers of the desired strength, folding endurance, and of much higher tear resistance than that possessed by paper made from stock which has been passed through a Jordan engine. The short-fibered pulp which I employ may be derived from Application filed November 15, 1929. Serial No. 407,588.
short-fibered woods, such as poplar. It is essential that it be of high alpha cellulose content, as the use of ashort-fibered raw material such as soda pulp is disadvantageous in themanufacture of high grade papers,
owing to its high proportion of non-alpha cellulose constituents, such as pentosans. The alpha cellulose content of the usual commercial soda pulp is only about 83% to 85%, and its pentosan content is about 8% to 15%, which latter constituent, together with other impurities, renders the pulp unstable and unfit for use in high grade papers. The shortfibered wood pulp employed in the papermaking composition of the present invention is of high alpha cellulose and low pentosan content. It may be prepared from shortfibered woods, such as poplar, by a process such as follows. The Wood in chipped condition may be cooked in an acid sulphite liquor, for instance in the usual calcium base 1i uor containing1% combined and 5% free g0 or .in a sodium base liquor, to produce a cleaner and more easily bleachable pulp.
The cooking operation may be carried out at a temperature of about 275 to 285 F. for about nine to ten hours, during which time free SO may be released from the digester to maintain the pressure at about 75 pounds. The digester contents may then be blown into a pit, and the raw woodpulp may be separated from the spent liquor by washing in the usual manner. The raw pulp may be converted to a white product of high alpha cellulose content by'suitable-refining steps. To this end, it may initially be treated at room temperature for about two to three hours, with a liquor containin about 1% to 3% chlorine or 1% to 5% hypoc lorite bleach, based on the dry weight of pulp. Or, if desired, both a suitable chlorine water treatment and hypochlorite bleach liquor treatment may be employed. 1 The chlorine water and/or bleach liquor removes lignin and other coloring matter from the pulp, or renders such matter soluble in alkaline liquors. The pulp is then washed, whereupon it may be treated with an alkaline liquor to remove chlorine reaction products and other nonalpha cellulose constituents from the pulp.
that when mixed with long-fi For instance, the ulp maybe treated at about 100 C. or at hig or temperature and under super-atmospheric pressure for about four to six hours, with a solution containing about 10% to 12% caustic soda, based on the weight of dry pulp. Or, if desired, the treatment may be effected at lower temperature with a more concentrated caustic soda solution, for instance at from 20 to 40 (1., for about two hours, in a solution containing 50% caustic soda, based on the weight of dry pulp. The refined pulp may then be bleached with a suitable agent to the desired whiteness, for instance, with calcium orsodium hypochlorite bleach liquor, preferably containin sufiicient free alkali to ensure a condition 0 distinct alkalinity throughout the bleaching operation, as such a condition prevents the formation of oxycellulose and accordingly results in a white product of maximum alpha cellulose content and stability. If desired, a permanganate bleach liquor may be employed, in which case the liquor should be maintained neutral or acid, in order to avoid degradation of fiber into oxycelluloses.
The resulting product is extremely free and resistant to gelatinization bgebeatmg, so red stocks such as rag pulp or long-fibered wood ulps, and beaten, it retains its opacity and bul iness' and imparts these characteristics and better printing properties to the resultin In either beaten or unbeaten con ition, it shrinks and swells much less than .do the long fibers, and accordingly may be used to advantage in admixture with the long fibers to produce papers which undergo much less change in dimensions when exposed to varying humidit conditions or when immersed in aqueous bat s and then dried, than papers heretofore produced. This property of the fiber renders it especially valuable for use in the manufacture of blueprint and photographic papers, which are subjected to such conditions.
In producing papermakin com ositions, the short-fibered pulps may e ad ed in desired fproportion, say 10% to 25%, to suitable longbered stock, such as rag pulp or wood 'pulp of high alpha cellulose content derived rom long-fibere'd woods such as spruce, either before or after the long-fibered stock has been subjected to beating to produce cellulose gel in suflicient amount to impart the desired strength and folding endurance to the resultin paper. Excellent results may be obtaine when the unbeaten, shortfibered pulp is added after the long-fibered stock has been beaten to the desired slowness, as in such case the short-fibered portion may be incorporated throughout the beaten and "elatinized long-fibered portion, with the beater roll sufiiciently raised from the bedplate of the beater engine to effect merely a mixing of the fibers. The composition may aper..
'of excellent formation and having excel ent stability, strength, folding endurance, tear resistance, bulk, and opaqueness.
I. claim: I
1. A papermaking composition comprisin a stable, white, long-fibered pulp of hig alpha cellulose content in elatinized condition, and a stable, white, s ort-fibered wood pulp of high alpha cellulose content in free condition.
.2. A apermaking composition, com rising a sta 1e, white, long-fibered pul of igh alpha. cellulose content and a su ordinate pro 'ortion of stable, white, poplar pulp of 'g alpha cellulose content.
3. A process which comprises forming a mixture of stable, white, long-fibered pulp of high alpha cellulose content in gelatimzed condition and stable, white, short-fibered wood pulp of high alpha cellulose content in free condition; and running off the m1xture into paper.
4. A process which comprises beating a stable, white lo'ng-fibered pulp to the desired slowness; mixin a subordinate proportion of unbeaten, stab e, white, poplar pulp therewith; and running off the mixture into paper.
5. Apapermakm composition comprising a blend of two cel ulose pulps, both being stable, white pulps of high alpha cellulose content, but one being derived from a longfibered cellulosic source, and the other being derived from a short-fibered cellulosic source. 6. Apapermakin composition comprising a blend of two woo pulps, both being stable, white pulps of high alpha cellulose content, but one being derived from a long-fibered wood of the type of spruce, and the other being derived from a short-fibered wood of the type of poplar.
In testimony whereof I have affixed my signature.
' GEORGE A. RICHTER.
US407569A 1929-11-15 1929-11-15 Papermaking composition Expired - Lifetime US1824837A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US407569A US1824837A (en) 1929-11-15 1929-11-15 Papermaking composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US407569A US1824837A (en) 1929-11-15 1929-11-15 Papermaking composition

Publications (1)

Publication Number Publication Date
US1824837A true US1824837A (en) 1931-09-29

Family

ID=23612624

Family Applications (1)

Application Number Title Priority Date Filing Date
US407569A Expired - Lifetime US1824837A (en) 1929-11-15 1929-11-15 Papermaking composition

Country Status (1)

Country Link
US (1) US1824837A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6391154B1 (en) * 1997-09-16 2002-05-21 M-Real Oyj Paper web and a method for the production thereof
US6406592B2 (en) * 1997-09-16 2002-06-18 M-Real Oyj Process for preparing base paper for fine paper
US6436238B1 (en) 1997-09-16 2002-08-20 M-Real Oyj Process for preparing a paper web

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6391154B1 (en) * 1997-09-16 2002-05-21 M-Real Oyj Paper web and a method for the production thereof
US6406592B2 (en) * 1997-09-16 2002-06-18 M-Real Oyj Process for preparing base paper for fine paper
US6436238B1 (en) 1997-09-16 2002-08-20 M-Real Oyj Process for preparing a paper web

Similar Documents

Publication Publication Date Title
WO2007065969A1 (en) Method of producing paper and cardboard
US3919041A (en) Multi-stage chlorine dioxide delignification of wood pulp
US1824837A (en) Papermaking composition
US1838326A (en) Refined wood pulp of low pentosan content
US2566130A (en) Manufacture of glassine paper
US3591451A (en) Pretreatment of vegetable matter and delignification of the refined matter with chloring dioxide
USRE28777E (en) Refining of vegetable matter and delignification of the refined matter with chlorine dioxide
US1802575A (en) High alpha cellulose fiber and process of producing same
US1809286A (en) Pulp of high whiteness and strength and process of producing same
US2083744A (en) Manufacture of sheeted cellulose fiber adapted for conversion into cellulose derivatives
US2215353A (en) Process of making fiberboard
El‐Taraboulsi et al. A modified method of nitric acid pulping of bagasse
Rasch A STUDY OFPURIFIED WOOD FIBERS AS Apaper-MAKING MATERIAL
US1850139A (en) Papermaking composition
US4836892A (en) Pulp blends for linerboards
US1899637A (en) Chemical pulping and refining process
US2687352A (en) Process of refining hardwood pulp
US1780943A (en) Fiber liberating and bleaching process
US3031371A (en) Paper of improved strength
Fahmy et al. Rice straw for paper making
US1709322A (en) Wood fiber for high-grade paper and derivative manufacture
US1742219A (en) Pulp-treating process
US1968345A (en) Treating sulphite pulp
US2159675A (en) Paper for nitration
US1921540A (en) Manufacture of glassine papers