US1786538A - Chemical-pulp paper-making process - Google Patents

Chemical-pulp paper-making process Download PDF

Info

Publication number
US1786538A
US1786538A US226526A US22652627A US1786538A US 1786538 A US1786538 A US 1786538A US 226526 A US226526 A US 226526A US 22652627 A US22652627 A US 22652627A US 1786538 A US1786538 A US 1786538A
Authority
US
United States
Prior art keywords
paper
pulp
chemical
stock
grinder
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
US226526A
Inventor
Frank A Johnson
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.)
DILTS MACHINE WORKS Inc
JOHN D HASKELL
JOHN H O CONNELL
Original Assignee
DILTS MACHINE WORKS Inc
JOHN D HASKELL
JOHN H O CONNELL
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 DILTS MACHINE WORKS Inc, JOHN D HASKELL, JOHN H O CONNELL filed Critical DILTS MACHINE WORKS Inc
Priority to US226526A priority Critical patent/US1786538A/en
Application granted granted Critical
Publication of US1786538A publication Critical patent/US1786538A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment

Definitions

  • the invention relates to chemical pulp paper making processes, and its object is the formulating and practice of a method for producing paper of a high grade, more expeditiously and at less cost than by any I means for the same purpose with which this applicant is acquainted. This could also be termed a process for grinding or hydrating chemical pulp.
  • the chemical pulp as received'from the pulp mill can either be in the form of dry Sheets approximately thirty-two inches long, or it can be shipped in laps which figure or are treated to be thirty to forty per centum dry.
  • the common method so far as applicants information extends, is to furnish the pulp directly into the heaters, and to lower the beater roll by degrees to bring about the necessary refinement. This is usually an extended and time-consuming operation when fully carried out.
  • the laps are charged into the magazineof a pulp grinder, and such magazine may be constructed of special design to accommodate the large size or full size bales.
  • the plunger of the hydraulic cylinder of the grinder may be of fourteen inches diameter, and the hydraulic pressure applied may vary from twenty to eighty pounds to the inch. In the making of grease proof paper this pressure at the cylinder would run between forty and Sixty pounds The pulp is thus held against the grinder stone in the presence of a small spray of wa invention.
  • the pulp produced by the grinder is of a diiierent nature from that produced by the beaters with rolls filled with steel or bronze bars, because when the heaters are used the individual fibers are apt to have the ends oi their cells closed by the action of the impulses of the beater roll on the bedplate'. 1 That is to say, the ends of the fibers are found to be flattened down and the cellular structure of the fiber closed at the ends. This prevents the thorough hydrationwhich is necessary to produce the character of stock required in accordance with this invention. For that reason the grinder stone is employed by applicant in carrying out this invention.
  • the grinder stone is equipped with a standard type of sharpener, in order that the surface of the stone may be roughened to any degree demanded, depending upon the nature of the pulp to be produced. It is customary to arrange immediatelybelow the grinder Where the stock discharges from the stone, a sand trap to catch' grit and other heavy particles which must be kept out of this high grade Samples of stock are taken at this point, and tested for freeness. Any standard make of freeness tester may be employed, and on the weight of sheet of grease proof paper mentioned, this test would run from to 80.
  • the process in accordance with this invention may be made very simple.
  • the pulp is reduced tothe paper-making consistency in the one operationof grinding, and goes thence to the paper machine in an almost constant stream, only a few minutes intervening between the grinding of the pulp and the finishing of the paper. Therefore, when the finished paper fails of the required test, the operator can go at once to the grinder, make the necessary correction, and the improved quality of paper comes right along.
  • it is the experience of this applicant that sometimes many hours are required to treat the pulp as and to the degree demanded, and paper that fails to test at the finishing end of the paper machine must continue to come for several hours before a correction can be properly made and become effective.
  • the purpose of the beating at this stage of the process is to permit the colors, alum, size or other substances tobe added to the pulp, and the stock is circulated in a light brushing contact with the hedplate.
  • the action of the beater roll also tends to open up the stock, and about one hours time is necessary to thoroughly work through the color or other substances stated.
  • the stock is dumped from the beater into a chestwhere it is agitated and kept in a suspended condition.
  • the stock is also usually diluted somewhatat this point.
  • From the agitator chest the stock is'pumped directly to the screen ahead of the paper machine where oversize fibers, lumps, sand or other foreign bodies are taken out before the paper is finally carried onto the forming wire of the machine. Up to this point only two men on each shift are required to produce the pulp, one of them at the grinder and one at the beater. When this same paper is producedin heaters, .six or eight men would probably be called for to get out the same tonnage.
  • a process for treating chemical pulp for making paper consisting in subjecting chem ical pulp to a grinding operation as distinguished from a beating action, varying the character of the grinding stones or the equivalent thereof in accordance with the nature and quality of the paper to be produced, applying freeness tests at the point of grinding, varying the pressure of the pulp against the grinders and introducing water in accordance with the requirements of the par-' ticular pulp under treatment and the product desired.
  • a process for treating chemical pulp for making-paper consisting in subjecting chemical pulp to a grinding operation as distinguished from a beating action, varying the character of the grinding stones or the equivalent thereof in accordance with the nature and quality of the paper to he produced, applying freeness tests at the point of grind ing, varying the pressure againstthe grinders and introducing water in accordance with the requirements of the particular pulp under treatment and the product desired, and forming sheet paper quickly from the treated pulp by increasing the Vacuum acting upon the sheet during its formation.
  • the paper is run over the driers in the regular 'way, and over one set of calender rolls before going to the reels.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Paper (AREA)

Description

No Drawing. a v
Patented Dee. 3t 19%) TQE FRANK A. JOHNSOBL OF BELTS MILLS, NEW YORK, ASSIGNOR OF ONE-FOURTH T0 JOHN H. OGONNELL, or SPRINGFIELD, MASSACHUSETTS, ONE-FOURTH 'ro JOHN D. HASKELL, or rUL'roN, NEW YORK, AND ONE-FOURTH TO DILTS MACHINE wonns, me, or rULroN, ew roan, a conronaxrroN or NEW YORK CHEMICAL-PULP PAPER-MAKING PROCESS The invention relates to chemical pulp paper making processes, and its object is the formulating and practice of a method for producing paper of a high grade, more expeditiously and at less cost than by any I means for the same purpose with which this applicant is acquainted. This could also be termed a process for grinding or hydrating chemical pulp.
Taking What is known as grease proof papers as an example in explaining the ini tent of this invention se :tar as applicant is aware, this paper at present is made in beaters requiring from eight to twelve hours of heating with a stone roll and bedplate in order to produce the super-hydrated characteristics which give the grease proofing qualities. The Same grade of paper is used for making glassine by a super-calendering process which gives the paper gloss and transparency. The paper taken for the example is'made from No. 2 grade Burgess bleached sulphite. That is the commercial designation of this particular pulp. It has been cooked some fourteen hours. The chemical pulp as received'from the pulp mill can either be in the form of dry Sheets approximately thirty-two inches long, or it can be shipped in laps which figure or are treated to be thirty to forty per centum dry. The common method, so far as applicants information extends, is to furnish the pulp directly into the heaters, and to lower the beater roll by degrees to bring about the necessary refinement. This is usually an extended and time-consuming operation when fully carried out. In accordance with the invention of this applicant the laps are charged into the magazineof a pulp grinder, and such magazine may be constructed of special design to accommodate the large size or full size bales. The plunger of the hydraulic cylinder of the grinder may be of fourteen inches diameter, and the hydraulic pressure applied may vary from twenty to eighty pounds to the inch. In the making of grease proof paper this pressure at the cylinder would run between forty and Sixty pounds The pulp is thus held against the grinder stone in the presence of a small spray of wa invention.
pa-per.
Application filed October 15, 1927. Serial No. 226,526.
ter, which produces the super-hydration necessary without prolonged brushing, asis the case when the pulp is acted upon in the beaters. The pulp produced by the grinder is of a diiierent nature from that produced by the beaters with rolls filled with steel or bronze bars, because when the heaters are used the individual fibers are apt to have the ends oi their cells closed by the action of the impulses of the beater roll on the bedplate'. 1 That is to say, the ends of the fibers are found to be flattened down and the cellular structure of the fiber closed at the ends. This prevents the thorough hydrationwhich is necessary to produce the character of stock required in accordance with this invention. For that reason the grinder stone is employed by applicant in carrying out this invention. The grinder stone is equipped with a standard type of sharpener, in order that the surface of the stone may be roughened to any degree demanded, depending upon the nature of the pulp to be produced. It is customary to arrange immediatelybelow the grinder Where the stock discharges from the stone, a sand trap to catch' grit and other heavy particles which must be kept out of this high grade Samples of stock are taken at this point, and tested for freeness. Any standard make of freeness tester may be employed, and on the weight of sheet of grease proof paper mentioned, this test would run from to 80.
The opportunity to almost immediately correct any departure from the desired quality of the paper, by proper attention to pressure, to the abrasive surface of the stone, to the spray of water and other details, at the point where the chemical pulp is ground on the stone, and from which it passes to the being inadvertently lost in the production of inferior paper before the improved quality would come again over the machine. believed that by reason of the testing stated,
It is Y to a standard beater.
the process in accordance with this invention may be made very simple. The pulp is reduced tothe paper-making consistency in the one operationof grinding, and goes thence to the paper machine in an almost constant stream, only a few minutes intervening between the grinding of the pulp and the finishing of the paper. Therefore, when the finished paper fails of the required test, the operator can go at once to the grinder, make the necessary correction, and the improved quality of paper comes right along. In present systems of making paper where the pulp is produced in heating engines, it is the experience of this applicant that sometimes many hours are required to treat the pulp as and to the degree demanded, and paper that fails to test at the finishing end of the paper machine must continue to come for several hours before a correction can be properly made and become effective.
From the grinder the stock is carried over a thickener of any standard design, and
some of the water removed, and from this thickener stock may be conveyed if desired The purpose of the beating at this stage of the process is to permit the colors, alum, size or other substances tobe added to the pulp, and the stock is circulated in a light brushing contact with the hedplate. The action of the beater roll also tends to open up the stock, and about one hours time is necessary to thoroughly work through the color or other substances stated.
The stock is dumped from the beater into a chestwhere it is agitated and kept in a suspended condition. The stock is also usually diluted somewhatat this point. From the agitator chest, the stock is'pumped directly to the screen ahead of the paper machine where oversize fibers, lumps, sand or other foreign bodies are taken out before the paper is finally carried onto the forming wire of the machine. Up to this point only two men on each shift are required to produce the pulp, one of them at the grinder and one at the beater. When this same paper is producedin heaters, .six or eight men would probably be called for to get out the same tonnage.
In carrying the paper over the machine it is necessary to use in this invention more vacuum boxes on the wire, as the actual sheet of paper must be formed quickly. In proceeding in accordance with this invention nine Vacuum boxes are used instead of four,
machine would approximate 250 feet per minute on grease proof paper, and after leaving the machine the paper may be given various degrees of calendering by the use of super-calenders.
The outstanding advantages of this invention are believed to he that the result is more uniform stock by super or extra hydration, and since an accurate ch'eckis practicable and easy by means of the testing stated, less human element enters into the manufacture. Where heaters are used the degree of hydration is usually determined by the,feel of the stock by the beater engineer, and no two beater men have the same feel. Hence, through a twenty-four hour run the same machine is likely to deliver pulp possessing three or four different qualities. Applicant holds that by the practice of this invention more uniform hydration of bone dry stock as well as of wet raw pulp is produced at the grinder, and that the same uniformity cannot be reached by heaters.
Having now described this invention and the manner of working the same, I claim 1. A process for treating chemical pulp for making paper, consisting in subjecting chem ical pulp to a grinding operation as distinguished from a beating action, varying the character of the grinding stones or the equivalent thereof in accordance with the nature and quality of the paper to be produced, applying freeness tests at the point of grinding, varying the pressure of the pulp against the grinders and introducing water in accordance with the requirements of the par-' ticular pulp under treatment and the product desired.
2. A process for treating chemical pulp for making-paper, consisting in subjecting chemical pulp to a grinding operation as distinguished from a beating action, varying the character of the grinding stones or the equivalent thereof in accordance with the nature and quality of the paper to he produced, applying freeness tests at the point of grind ing, varying the pressure againstthe grinders and introducing water in accordance with the requirements of the particular pulp under treatment and the product desired, and forming sheet paper quickly from the treated pulp by increasing the Vacuum acting upon the sheet during its formation.
In testimony whereof I atfixmy signature.
FRANK A. JOHNSON.
with about 5 or 6 inches of vacuum applied., I
and in directing the paper over the presses extreme care must be taken in watching the stretch of the sheet at this point. The paper is run over the driers in the regular 'way, and over one set of calender rolls before going to the reels. The average speed of the
US226526A 1927-10-15 1927-10-15 Chemical-pulp paper-making process Expired - Lifetime US1786538A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US226526A US1786538A (en) 1927-10-15 1927-10-15 Chemical-pulp paper-making process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US226526A US1786538A (en) 1927-10-15 1927-10-15 Chemical-pulp paper-making process

Publications (1)

Publication Number Publication Date
US1786538A true US1786538A (en) 1930-12-30

Family

ID=22849269

Family Applications (1)

Application Number Title Priority Date Filing Date
US226526A Expired - Lifetime US1786538A (en) 1927-10-15 1927-10-15 Chemical-pulp paper-making process

Country Status (1)

Country Link
US (1) US1786538A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE748862C (en) * 1937-12-21 1944-11-11 Friedrich Ruehlemann Dr Ing Process for the production of cellulose flour
US2629295A (en) * 1945-06-15 1953-02-24 Eastman Kodak Co Method of making paper

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE748862C (en) * 1937-12-21 1944-11-11 Friedrich Ruehlemann Dr Ing Process for the production of cellulose flour
US2629295A (en) * 1945-06-15 1953-02-24 Eastman Kodak Co Method of making paper

Similar Documents

Publication Publication Date Title
CN104499342B (en) The manufacturing process of water resistance brown paper
US1786538A (en) Chemical-pulp paper-making process
US2006209A (en) Dull finish coated paper
US2158265A (en) Leather pulp and products made therefrom
US2045095A (en) Process of making porous long fibered nonhydrated paper
US2237235A (en) Process for making leather sheets
US1881419A (en) Fiber derivative
US1936697A (en) Paper manufacture
US1583788A (en) Method of and apparatus for finishing paper
US1083102A (en) Method of preparing paper-pulp.
NO133989B (en)
US1881985A (en) Method and means for manufacture of paper
US487912A (en) Process of and apparatus for disintegrating fibrous substances
US1983572A (en) Paper and process of and apparatus for making the same
US1598793A (en) Method of and means for making machine-glazed paper
US295835A (en) Manufacture of paper from grain-cuticles
US2018490A (en) Method of producing paper pulp from fibrous material
DE874698C (en) Process for removing loosely felted fiber knots in the manufacture of paper and cardboard from alkaline digested or treated cellulose
US2389254A (en) Manufacture of paper
DE418304C (en) Process for the production of cardboard from fiber materials of all kinds
Shaw et al. Research on the production of currency paper in the bureau of standards experimental paper mill
US1580814A (en) Method of hydrating cellulose fibers
US1946953A (en) Process for producing synthetic lumber that is not attacked by molds
Carson et al. Wearing quality of experimental currency-type papers
US1599831A (en) Process of preparing paper half stock