DE1165985B - Process to prevent resin from settling in papermaking from sulphite pulp - Google Patents
Process to prevent resin from settling in papermaking from sulphite pulpInfo
- Publication number
- DE1165985B DE1165985B DER29413A DER0029413A DE1165985B DE 1165985 B DE1165985 B DE 1165985B DE R29413 A DER29413 A DE R29413A DE R0029413 A DER0029413 A DE R0029413A DE 1165985 B DE1165985 B DE 1165985B
- Authority
- DE
- Germany
- Prior art keywords
- settling
- papermaking
- weight
- prevent resin
- resin
- 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.)
- Pending
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP 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
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/02—Agents for preventing deposition on the paper mill equipment, e.g. pitch or slime control
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP 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
- D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
- D21H11/02—Chemical or chemomechanical or chemothermomechanical pulp
- D21H11/06—Sulfite or bisulfite pulp
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S162/00—Paper making and fiber liberation
- Y10S162/04—Pitch control
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Paper (AREA)
Description
DEUTSCHESGERMAN
PATENTAMTPATENT OFFICE
AUSLEGESCHRIFTEDITORIAL
Deutsche Kl.: 55 b-5/01 German class: 55 b -5/01
Nummer: Aktenzeichen: Anmeldetag: Auslegetag:Number: File number: Registration date: Display day:
R 29413 VIb/55 b
7.Januar 1961
19. März 1964 R 29413 VIb / 55 b
January 7, 1961
March 19, 1964
In der Patentanmeldung R27159VIb/55b ist ein Verfahren zur Verhütung des Absetzens von Harz bei der Herstellung von Papier aus Sulfitzellstoff beschrieben, das dadurch gekennzeichnet ist, daß dem Sulfitzellstoff 0,05 bis 0,5 Gewichtsprozent (berechnet auf das Gewicht der Breifeststoffe) eines Polymeren aus 80 bis 100 Gewichtsprozent N-Vinyl-2-pyrrolidinon in dem Stadium unmittelbar vor dem Kochen bis unmittelbar vor dem Stoffauflauf einverleibt werden.In the patent application R27159VIb / 55b is a Described method for preventing the settling of resin in the manufacture of paper from sulphite pulp, which is characterized in that the sulfite pulp contains 0.05 to 0.5 percent by weight (calculated based on the weight of the pulp solids) of a polymer composed of 80 to 100 percent by weight of N-vinyl-2-pyrrolidinone incorporated at the stage just before cooking to just before the headbox will.
Es wurde nun gefunden, daß zur Erreichung des gewünschten Effektes die Menge des zugesetzten Polymeren bis auf 0,005 Gewichtsprozent, vorzugsweise 0,02 bis 0,05 Gewichtsprozent, herabgesetzt werden kann. Das Absetzen von Harz kann mit diesen Mengen erfolgreich durchgeführt werden, insbesondere sind die verwendeten Polymeren besonders geeignet in den Fällen, in denen eine Kontrolle des Harzabsetzens unbedingt wesentlich ist.It has now been found that to achieve the desired effect, the amount of added Polymers reduced to 0.005 percent by weight, preferably 0.02 to 0.05 percent by weight can be. Settling of resin can be carried out successfully with these amounts, in particular The polymers used are particularly suitable in those cases where a control resin settling is essential.
Ein Holzbrei mit einer Konsistenz von 3,5 °/o aus 454 kg gebleichtem Kraftstoff und 544 kg gebleichtem Sulfit, 2,27 kg eines Harzleims, der eine kleine Menge eines Addukts aus einem Harz und Maleinsäure enthält, 301 einer Klebstofflösung (11,34 kg/ 196,821) und 1,8 kg Natriumaluminat wurde in heißem Wasser entfasert und dann 2 Stunden lang bei 77101 C gemahlen. Dann gab man 36,3 kg Titaniumdioxydpigment und 18 kg Alaun zu. Eine Lösung, die 0,24% (4,54 kg/189,25 1) eines Homopolymeren von N-Vinyl-2-pyrrolidinon mit einem K-Wert von 30 enthielt, wurde kurz vor den Flügelpumpen (wo der Brei eine Konsistenz von 0,5 °/o aufwies) mit einer Menge von 1,78 1 Lösung in der Minute dem Brei zugesetzt. Dies entspricht 0,038 °/o des Homopolymeren, bezogen auf das Gewicht der Faser in dem Brei. Man erzielt dabei eine ausgezeichnete harzdispergierende Wirkung. Tatsächlich beträgt die Menge des normalerweise verwendeten Harzdispergierungsmittels (Natriumsalz eines sulfonierten Kondensats aus Formaldehyd und Naphthalin), die zur Erzielung guter Ergebnisse erforderlich ist, 0,38 % des Dispergierungsmittels, bezogen auf das Gewicht des Papierbreis.A wood pulp with a consistency of 3.5% made from 454 kg of bleached fuel and 544 kg of bleached sulfite, 2.27 kg of a resin glue containing a small amount of an adduct of a resin and maleic acid, 301 of an adhesive solution (11.34 kg / 196.821) and 1.8 kg of sodium aluminate were defibrated in hot water and then milled at 77 101 C for 2 hours. Then 36.3 kg of titanium dioxide pigment and 18 kg of alum were added. A solution containing 0.24% (4.54 kg / 189.25 l) of a homopolymer of N-vinyl-2-pyrrolidinone with a K value of 30 was just before the vane pumps (where the slurry had a consistency of 0.5%) was added to the slurry at a rate of 1.78 liters of solution per minute. This corresponds to 0.038% of the homopolymer based on the weight of the fiber in the slurry. An excellent resin-dispersing effect is achieved. In fact, the amount of resin dispersant normally used (sodium salt of a sulfonated condensate of formaldehyde and naphthalene) required for good results is 0.38% of the dispersant based on the weight of the pulp.
Verfahren zur Verhütung des Absetzens von Harz bei der Papierherstellung aus Sulfitzellstoff
Zusatz zur Anmeldung: R 27159 VI b / 55 b —
Auslegeschrift 1157 468Process for preventing resin settling in papermaking from sulphite pulp
Addition to registration: R 27159 VI b / 55 b -
Interpretation document 1157 468
Anmelder:Applicant:
Rohm & Haas Company, Philadelphia, Pa.
(V. St. A.)Rohm & Haas Company, Philadelphia, Pa.
(V. St. A.)
Vertreter:Representative:
Dr. W. Beil, A. Hoeppener und Dr. H. J. Wolff,Dr. W. Beil, A. Hoeppener and Dr. H. J. Wolff,
Rechtsanwälte,Lawyers,
Frankfurt/M.-Höchst, Antoniterstr. 36Frankfurt / M.-Höchst, Antoniterstr. 36
Als Erfinder benannt:Named as inventor:
Thomas James Drennen, Lafayette Hill, Pa.,Thomas James Drennen, Lafayette Hill, Pa.,
Louis Erwin Kelley, Wyncote, Pa. (V. St. A.)Louis Erwin Kelley, Wyncote, Pa. (V. St. A.)
Beanspruchte Priorität:Claimed priority:
V. St. v. Amerika vom 10. Februar 1960V. St. v. America 10 February 1960
(Nr. 7743)(No. 7743)
Bemerkenswerte Vorteile erzielt man dann, wenn die Menge des N-Vinyl-2-pyrrolidinon-Polymeren auf etwa 0,02 "/o, bezogen auf die Faser, herabgesetzt wird.Notable advantages are achieved when the amount of N-vinyl-2-pyrrolidinone polymer is increased about 0.02 "/ o based on the fiber is decreased.
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US7743A US3081219A (en) | 1960-02-10 | 1960-02-10 | Prevention of deposition of pitch in papermaking |
Publications (1)
Publication Number | Publication Date |
---|---|
DE1165985B true DE1165985B (en) | 1964-03-19 |
Family
ID=21727895
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DER29413A Pending DE1165985B (en) | 1960-02-10 | 1961-01-07 | Process to prevent resin from settling in papermaking from sulphite pulp |
Country Status (2)
Country | Link |
---|---|
US (1) | US3081219A (en) |
DE (1) | DE1165985B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0249891A1 (en) * | 1986-06-14 | 1987-12-23 | BASF Aktiengesellschaft | Process for producing paper and cardboard |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3272689A (en) * | 1963-02-04 | 1966-09-13 | Owens Illinois Inc | Delignification of lignocellulose with an nu-(lower alkyl)-2-pyrrolidone |
US3354027A (en) * | 1963-09-11 | 1967-11-21 | Abitibi Power & Paper Co | Deinking of waste paper |
US3325346A (en) * | 1964-06-26 | 1967-06-13 | Chemirad Corp | Process of making paper using reaction product of polyethyleneimine and polyisocyanate |
US3873417A (en) * | 1974-01-31 | 1975-03-25 | Basf Wyandotte Corp | Pitch and pigment dispersant in aqueous pulp slurries |
US4190491A (en) * | 1976-08-02 | 1980-02-26 | Rohm And Haas Company | Process for controlling pitch in papermaking |
US4184912A (en) * | 1976-08-09 | 1980-01-22 | Nalco Chemical Company | Pitch control method |
US5626720A (en) * | 1986-01-09 | 1997-05-06 | W.R. Grace & Co.-Conn. | Method for controlling pitch on a papermaking machine |
US5223097A (en) * | 1986-01-09 | 1993-06-29 | W. R. Grace Ab | Method for controlling pitch on a paper-making machine |
US5074961A (en) * | 1986-06-03 | 1991-12-24 | Betz Laboratories, Inc. | Process for controlling pitch deposition from pulp in papermaking systems |
US4744865A (en) * | 1986-06-03 | 1988-05-17 | Betz Laboratories, Inc. | Process for controlling pitch deposition from pulp in papermaking systems |
US4846933A (en) * | 1986-06-03 | 1989-07-11 | Betz Laboratories, Inc. | Process for controlling pitch deposition from pulp in papermaking systems |
US4765867A (en) * | 1986-07-02 | 1988-08-23 | Betz Laboratories, Inc. | Pitch control process utilizing quaternized polyamine ionene polymer |
GB2205591B (en) * | 1987-05-01 | 1990-03-07 | Grace W R & Co | Pitch control aid |
US4995944A (en) * | 1988-09-16 | 1991-02-26 | Dearborn Chemical Company Ltd. | Controlling deposits on paper machine felts using cationic polymer and cationic surfactant mixture |
DE4311599A1 (en) * | 1993-04-08 | 1994-10-13 | Henkel Kgaa | Process for controlling the settling of sticky contaminants from pulp suspensions |
DE4311598A1 (en) * | 1993-04-08 | 1994-10-13 | Henkel Kgaa | Process for controlling the settling of sticky contaminants from pulp suspensions |
DE19515273A1 (en) * | 1995-04-26 | 1996-10-31 | Henkel Kgaa | Process for controlling the settling of sticky contaminants from pulp suspensions |
CN1906359A (en) * | 2004-03-30 | 2007-01-31 | 日油瑞新株式会社 | Pitch controlling agent |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL217723A (en) * | 1939-08-02 | |||
US2667473A (en) * | 1952-02-08 | 1954-01-26 | Monsanto Chemicals | Vinyl acetate-n-vinyl-pyrrolidone copolymers |
US2771362A (en) * | 1954-02-09 | 1956-11-20 | Rohm & Haas | Cellulose fibrous products containing polymers of vinyloxyethylurea and method of producing them |
BE553532A (en) * | 1955-12-19 | |||
US2945863A (en) * | 1958-06-24 | 1960-07-19 | Gen Aniline & Film Corp | Amides of aminoalkyl pyrrolidones |
-
1960
- 1960-02-10 US US7743A patent/US3081219A/en not_active Expired - Lifetime
-
1961
- 1961-01-07 DE DER29413A patent/DE1165985B/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0249891A1 (en) * | 1986-06-14 | 1987-12-23 | BASF Aktiengesellschaft | Process for producing paper and cardboard |
Also Published As
Publication number | Publication date |
---|---|
US3081219A (en) | 1963-03-12 |
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