EP0161443B1 - Herstellung von trocken- oder nassgekreppten Papieren - Google Patents

Herstellung von trocken- oder nassgekreppten Papieren Download PDF

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Publication number
EP0161443B1
EP0161443B1 EP85103781A EP85103781A EP0161443B1 EP 0161443 B1 EP0161443 B1 EP 0161443B1 EP 85103781 A EP85103781 A EP 85103781A EP 85103781 A EP85103781 A EP 85103781A EP 0161443 B1 EP0161443 B1 EP 0161443B1
Authority
EP
European Patent Office
Prior art keywords
ethoxylated
propoxylated
atoms
carboxylic acid
paper
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
Application number
EP85103781A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP0161443A1 (de
Inventor
Hasan Dr. Dipl.-Ing. Ulubay
Horst Schürmann
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.)
Akzo Patente Te Wuppertal Bondsrepubliek Dui GmbH
Original Assignee
Akzo GmbH
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 Akzo GmbH filed Critical Akzo GmbH
Priority to AT85103781T priority Critical patent/ATE27193T1/de
Publication of EP0161443A1 publication Critical patent/EP0161443A1/de
Application granted granted Critical
Publication of EP0161443B1 publication Critical patent/EP0161443B1/de
Expired legal-status Critical Current

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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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • D21H17/05Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/14Carboxylic acids; Derivatives thereof
    • 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • D21H17/05Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/07Nitrogen-containing compounds

Definitions

  • the invention relates to the production of papers, in particular wet or dry creped papers with increased suction speed compared to aqueous media.
  • Increased water absorption speed is particularly required for the papers that are used in the field of hygiene, such. B. toilet paper, paper towels, kitchen rolls, etc.
  • Fibers with a low degree of grinding and large fiber diameters generally lead to more voluminous and thus more absorbent papers.
  • pulps come from softwoods such. B. pine or Douglas fir, followed by spruce.
  • Hardwoods generally result in low absorbency with the exception of beech.
  • Tissue types such as handkerchiefs and kitchen rolls, are given a more or less wet-proof finish.
  • cationic wet strength agents such as B. polyamide-epichlorohydrin condensation products used.
  • the creping of the paper is carried out, for example, in such a way that the paper web is guided to a large-diameter drying cytin and dried there and is detached from the cylinder surface at the end of the path on the cylinder by means of a so-called creping scraper.
  • the extent of the creping is determined by the speed difference between the drying cylinder and the subsequent reeling.
  • creping aids adheresives
  • Increased use of waste paper with a high degree of grinding and a high proportion of filler and fine material as a raw material for tissue generally leads to a deterioration in the drainage in the wire section, to increased adhesion to the drying cylinder and to a strong abrasion of the crepe scrapers.
  • the chemicals used to increase the wet strength additionally deteriorate the drainage and absorbency of the papers and increase the adhesive effect on the drying cylinder.
  • absorbent cellulose products are used which are produced by dry defibrillation of cellulose pulp or cellulose fiber pulp with the formation of flakes.
  • the cellulose pulp should have a low mechanical strength in order to enable the fibers to be separated from one another without destroying them and to reduce the energy required for the breakdown.
  • the flakes obtained after dry-cutting should have a good liquid absorption capacity and a short absorption time.
  • cationic surfactants such as quaternary ammonium compounds to reduce the bonds between the cellulosic fibers. These compounds result in a noticeable impairment of the water absorption time.
  • non-ionic substances which are ethoxylated or propoxylated aliphatic alcohols or alkylphenols are used, and SE-B-402607, referenced in Chemical Abstracts Vol. 89, 181,429, teaches a process in which alkoxylated aliphatic Alcohols in combination with quaternary ammonium compounds can be used as retention agents.
  • Non-ionic compounds are used in the production of absorbent cellulose pulp, these compounds consisting of partial fatty acid esters of polyhydric alcohols having 2 to 8 carbon atoms or their anhydrides, i.e. Anhydro derivatives such as B. inner ethers or of polyethylene or polypropylene glycols with molecular weights up to 500.
  • the object of the present invention was to improve the known processes for the production of absorbent papers, in particular dry or wet creped papers, in such a way that the adhesion to the drying cylinder is reduced and the formation of deposits on the drying cylinder is prevented.
  • Carboxylic acid esters and / or polyethers in which the alkyl group of the ethoxylated and / or propoxylated alkylphenol has 8 to 16 carbon atoms, for example an ethoxylated and / or propoxylated nonylphenol, are preferably used.
  • Particularly suitable alcohols are ethylhexanol, dodecanol, lauryl alcohol, stearyl alcohol and the so-called Guerbet alcohols.
  • Suitable ethoxylated and / or propoxylated amines include, for example, polyoxyethylene cocosamines, polyoxyethylene valley amines, polyoxyethylene oleylamines and polyoxyethylene octadecylamines, which are commercially available with different degrees of ethoxylation under the trade name Ethomeen.
  • Ethoxylated amides are commercially available under the trade name Ethomid "and consist, for example, of polyoxyethylene oleoamides or polyoxyethylene valley amides. These are also suitable starting products for the carboxylic acid esters and / or polyethers to be used according to the invention.
  • Fatty and resin acids are particularly suitable as carboxylic acids.
  • Carboxylic acids containing 12 to 20 carbon atoms for example oleic acid, palmitic acid or abietic acid, are preferred.
  • Long-chain epoxides which are suitable for the invention are, in particular, 1,2-epoxides with 8 to 30 C atoms.
  • Polyethers in which the long-chain 1,2-epoxide contains 12 to 18 carbon atoms are preferably used.
  • the degree of ethoxylation and / or propoxylation of the ethoxylated and / or propoxylated primary or secondary alcohols, alkylphenols, amines and / or amides converted to carboxylic acid esters or polyethers is preferably 5 to 15.
  • the carboxylic acid esters are prepared by reacting the ethoxylated and / or propoxylated alcohols, alkylphenols, amines and / or amides with corresponding carboxylic acids at temperatures between approximately 160-225 ° C. and under normal pressure, using 0.1 to 0.5 as the catalyst % By weight p. Toluenesulfonic acid, based on the total batch, be added. After the majority of the water of reaction has been distilled off, the rest of the water of reaction is drawn off under a vacuum of 80 to 100 mbar. The acid number of the finished products is approx. 5-8.
  • the polyethers are prepared by reacting the ethoxylated and / or propoxylated alcohols, alkylphenols, amines and / or amides with the corresponding long-chain 1,2-epoxides with 0.1 to 0.5% by weight KOH, based on the total batch , as a catalyst at temperatures between 100-180 ° C.
  • the carboxylic acid esters and / or polyethers used according to the invention also have excellent self-emulsification properties which make predilution superfluous. It is therefore a preferred embodiment of the present invention that the carboxylic acid esters and / or polyethers are added in liquid form in an active ingredient concentration of more than 80% by weight.
  • polyethers which are solid, it is preferred that the addition is made in an aqueous dispersion or solution for better metering of the polyether.
  • the carboxylic acid esters and / or polyethers are added to the paper in an amount of 0.05 to 0.5% by weight, based on dry cellulose.
  • the carboxylic acid esters and / or polyethers are added in the Dutch, pulper and / or during sheet formation.
  • a carboxylic acid ester C ester of nonylphenol ethoxylate with 9 EO and stearic acid was used to increase the absorbency.
  • the results and comparative results are summarized in Table 11.
  • the basis weight of the papers was 34 g / m 2 .

Landscapes

  • Paper (AREA)
  • Secondary Cells (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)
  • Air Bags (AREA)
EP85103781A 1984-04-30 1985-03-29 Herstellung von trocken- oder nassgekreppten Papieren Expired EP0161443B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT85103781T ATE27193T1 (de) 1984-04-30 1985-03-29 Herstellung von trocken- oder nassgekreppten papieren.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3416043 1984-04-30
DE3416043A DE3416043C2 (de) 1984-04-30 1984-04-30 Verwendung von Carbonsäureestern oder Polyäthern bei der Herstellung von Papier, insbesondere von trocken- oder naßgekreppten Papieren

Publications (2)

Publication Number Publication Date
EP0161443A1 EP0161443A1 (de) 1985-11-21
EP0161443B1 true EP0161443B1 (de) 1987-05-13

Family

ID=6234702

Family Applications (1)

Application Number Title Priority Date Filing Date
EP85103781A Expired EP0161443B1 (de) 1984-04-30 1985-03-29 Herstellung von trocken- oder nassgekreppten Papieren

Country Status (7)

Country Link
US (1) US4632730A (fi)
EP (1) EP0161443B1 (fi)
JP (1) JPH0621440B2 (fi)
AT (1) ATE27193T1 (fi)
CA (1) CA1248711A (fi)
DE (1) DE3416043C2 (fi)
FI (1) FI83443C (fi)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5048589A (en) * 1988-05-18 1991-09-17 Kimberly-Clark Corporation Non-creped hand or wiper towel
EP0347176B2 (en) * 1988-06-14 1997-07-02 The Procter & Gamble Company Soft tissue paper containing noncationic surfactant
US4940513A (en) * 1988-12-05 1990-07-10 The Procter & Gamble Company Process for preparing soft tissue paper treated with noncationic surfactant
US5314580A (en) * 1992-07-08 1994-05-24 Mauvin Material & Chemical Processing Limited Process for the removal of ink, resin, and adhesive residues from paper, textile fabrics and solid surfaces
US5336373A (en) * 1992-12-29 1994-08-09 Scott Paper Company Method for making a strong, bulky, absorbent paper sheet using restrained can drying
US5458737A (en) * 1993-07-27 1995-10-17 Hoechst Celanese Corporation Quaternary compounds as brightness enhancers
US5560805A (en) * 1993-07-27 1996-10-01 Hoechst Celanese Corporation Enhanced decolorization of waste paper with selected amines
US5580422A (en) * 1993-07-27 1996-12-03 Hoechst Celanese Corporation Brightening color dyed wastepaper with a bleaching agent and a quaternary compound
US5468796A (en) * 1994-08-17 1995-11-21 Kimberly-Clark Corporation Creeping chemical composition and method of use
JP3021054U (ja) * 1995-04-19 1996-02-16 小林木工株式会社 家具の転倒防止装置
JP3128248B2 (ja) 1996-07-18 2001-01-29 花王株式会社 紙用嵩高剤、高嵩高性パルプシート及び該パルプシートの製造方法
US5882478A (en) * 1997-11-12 1999-03-16 Kimberly-Clark Worldwide, Inc. Tissue products containing esters of polyoxyethylene alkyl ether carboxylic acids
EP1398413A2 (en) * 1998-06-12 2004-03-17 Fort James Corporation Method of making a paper web having a high internal void volume of secondary fibers and a product made by the process
US6733773B1 (en) 2000-11-21 2004-05-11 Kimberly-Clark Worldwide, Inc. Paper products treated with oil-in-water emulsions
JP4493674B2 (ja) * 2007-02-28 2010-06-30 大王製紙株式会社 ロール状食材紙

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA878981A (en) * 1971-08-24 Korsnas-Marma Aktiebolag Method of producing highly absorbent cellulose
US2683087A (en) * 1948-02-10 1954-07-06 American Cyanamid Co Absorbent cellulosic products
US2712994A (en) * 1949-01-27 1955-07-12 Monsanto Chemicals Process for improving paper and product
US2683089A (en) * 1952-06-10 1954-07-06 American Cyanamid Co Bibulous sheet
US3180786A (en) * 1962-04-02 1965-04-27 Nalco Chemical Co Amide-ether compounds and use in inhibiting foam
SE338916B (fi) * 1968-11-04 1971-09-20 Korsnaes Marma Ab
US3637869A (en) * 1969-06-02 1972-01-25 Basf Wyandotte Corp Nonionic biodegradable foam control agent
GB1338391A (en) * 1970-12-21 1973-11-21 Ici Ltd Method for emulsifying and dispersing oil slicks on water
BE787398A (fr) * 1971-08-10 1973-02-12 Basf Ag Alcools oxalcoyles et preparations detergentes les contenant comme anti-mousses
DE2161772C3 (de) * 1971-12-13 1984-04-12 Basf Ag, 6700 Ludwigshafen Entschäumer in Papierstreichmassen
SE402607B (sv) * 1975-06-24 1978-07-10 Kema Nord Ab Sett och medel vid framstellning av fluffmassa
SE425512B (sv) * 1978-07-21 1982-10-04 Berol Kemi Ab Settt for framstellning av absorberande cellulosamassa med anvendning av nonjoniska emnen och katjoniskt retentionsmedel samt medel for genomforande av settet
DE3116581A1 (de) * 1981-04-27 1982-12-30 Hoechst Ag, 6000 Frankfurt Verwendung von veresterten oxalkylaten als praeparationsmittel fuer farbstoffe und entsprechende farbstoffzubereitungen
DE3207612C2 (de) * 1982-03-03 1986-04-03 Akzo Gmbh, 5600 Wuppertal Polyätherderivate und deren Verwendung als Emulgatoren
US4483741A (en) * 1982-08-10 1984-11-20 Economics Laboratory, Inc. Low-foaming, pH sensitive, alkylamine polyether surface active agents and methods for using
DE3404086A1 (de) * 1983-02-07 1984-08-09 Arakawa Kagaku Kogyo K.K., Osaka Leimzusammensetzung fuer die papierherstellung
CA1237960A (en) * 1983-12-30 1988-06-14 William A. Sweeney Stable substituted succinic anhydride/emulsifier composition and methods for its use

Also Published As

Publication number Publication date
ATE27193T1 (de) 1987-05-15
FI851500A0 (fi) 1985-04-15
DE3416043C2 (de) 1986-12-04
FI83443B (fi) 1991-03-28
US4632730A (en) 1986-12-30
CA1248711A (en) 1989-01-17
DE3416043A1 (de) 1985-10-31
JPS6112999A (ja) 1986-01-21
EP0161443A1 (de) 1985-11-21
JPH0621440B2 (ja) 1994-03-23
FI851500L (fi) 1985-10-31
FI83443C (fi) 1991-07-10

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