WO1988002416A1 - Method of making soft paper - Google Patents

Method of making soft paper Download PDF

Info

Publication number
WO1988002416A1
WO1988002416A1 PCT/SE1987/000424 SE8700424W WO8802416A1 WO 1988002416 A1 WO1988002416 A1 WO 1988002416A1 SE 8700424 W SE8700424 W SE 8700424W WO 8802416 A1 WO8802416 A1 WO 8802416A1
Authority
WO
WIPO (PCT)
Prior art keywords
wet
layer
dry
fibres
fibre
Prior art date
Application number
PCT/SE1987/000424
Other languages
French (fr)
Inventor
Irene Katarina Wedin
Bo Ragnar Ek
Original Assignee
Sunds Defibrator Aktiebolag
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 Sunds Defibrator Aktiebolag filed Critical Sunds Defibrator Aktiebolag
Priority to AT87906631T priority Critical patent/ATE66980T1/en
Priority to DE8787906631T priority patent/DE3772774D1/en
Publication of WO1988002416A1 publication Critical patent/WO1988002416A1/en
Priority to NO882404A priority patent/NO170500C/en
Priority to FI891577A priority patent/FI100899B/en

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
    • D21H5/00—Special paper or cardboard not otherwise provided for
    • D21H5/26—Special paper or cardboard manufactured by dry method; Apparatus or processes for forming webs by dry method from mainly short-fibre or particle material, e.g. paper pulp
    • D21H5/2678—Manufacture of layered products (assembly of superposed sheets), comprising the consolidation of such a structure
    • D21H5/2685—Manufacture of layered products (assembly of superposed sheets), comprising the consolidation of such a structure by dry method on to a web or on or between several preformed webs, at least one of which has been formed by another method, e.g. by wet method
    • 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
    • D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
    • D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
    • D21H23/22—Addition to the formed paper
    • D21H23/24—Addition to the formed paper during paper manufacture
    • D21H23/26—Addition to the formed paper during paper manufacture by selecting point of addition or moisture content of the paper
    • D21H23/28—Addition before the dryer section, e.g. at the wet end or press section
    • 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
    • D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
    • D21H27/30—Multi-ply
    • 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
    • D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
    • D21H27/30—Multi-ply
    • D21H27/38—Multi-ply at least one of the sheets having a fibrous composition differing from that of other sheets

Definitions

  • This invention relates to the making of soft paper from cellulose fibres.
  • Soft paper is a common denomination for paper used for absorbing purposes, such as tissue, drying cloth, napkins and handkerchiefs. Soft paper competes with woven fabrics, but in contrast to them is intended for one-way use. The properties desired are rapid and effective absorption, soft and smooth structure and good strength also in wet state.
  • Soft paper is manufactured mainly by wet forming, i.e. a fibre suspension in water is caused to flow out on a running wire where it is dewatered and then dried.
  • criping is carried out usually by means of a so-called Yankee cylinder where the paper web is scraped off after drying.
  • Soft paper manufactured in this way is very bulky, i.e. has a very loose structure.
  • the machine speed must be low, about 50 m/min.
  • the manufacturing cost is very high, and the products have to be sold at a high price.
  • Dry-formed soft paper thus, has a higher bulk than wet-formed paper.
  • the reason of this is that the fibres in the dry-formed paper have not been softened in water and, therefore, are not bent down into the paper plane. Furthermore, no water has to be drained through the structure and, therefore, no capillary forces contract the structure at the removal of water by drying.
  • At dry-forming the fibres deposit at random in all directions both in the plane of the paper and perpendicularly thereto, while at wet- -forming the fibres substantially deposit in the plane of the paper.
  • the present invention is a combination of wet-forming and dry-forming whereby the advantages of both methods have been utilized.
  • air-borne fibres are deposited directly on a wet-formed layer while the layer is still wet.
  • Its dry solids content preferably should be 5-25 % .
  • the dry-formed layer should not have too great a thickness.
  • every dry-formed fibre should meet the wet-formed layer. This implies in praetice a grammage of 2-20 g/m 2 . Between the two layers fibre bindings arise which ensure good cohesion of the layers.
  • a particularly advantageous quality of soft paper is obtained by depositing air-borne dry fibres on both sides of the wet-formed layer.
  • the manufactured soft paper has a soft and smooth surface, higher bulk than wet-formed paper and higher strength than dry-forned paper without addition of chemicals.
  • the method according to the invention also results in high internal bond strength (z-strength) in spite of the absence of special binding agents.
  • the machine speed for wet-forming i.e. 500-2000 m/min, can be maintained.
  • a fibre suspension flows out onto a running wire 2 thereby forming a first fibre layer in a wet manner on the wire.
  • Dewatering takes place through suction boxes 3 located beneath the wire 2.
  • Air-borne dry fibres are deposited directly on the wet- -formed layer,while it is still wet, by means of a forming box 4 located above the wire 2 and a vacuum box 5 located beneath the wire.
  • the dry fibres thereby form a second fibre layer on the first one. Between the layers fibre bindings arise.
  • the dry fibres are exposed in a defibering device 6, for example a hammer mill or coarse shredder, followed by a refiner for fluffing.
  • the fibres are transported by means of a fan 7 to the forming box 4 , which can be of the type shown in patent application SE 85 05 918-6. Reject discharged from the forming box 4 through a conduit 8 can be re-cycled, possibly after renewed defibering.
  • the wet-formed layer shall have a grammage of 10-100g/m 2 .
  • the wet-formed layer, at:-.the application of the air-borne dry fibres, shall have been dewatered to a dry solids content of 5-25 % .
  • the dry fibres preferably should have been taken from chemical pulp in order to yield a surface of high softness.
  • the fibres shall be well dispersed in the air.
  • the flow rate in the inlet to the forming box shall exceed 100 m/s.
  • the distribution between the reject flow through the conduit 8 and the fibre flow dry-formed on the wet-formed layer shall be so that between 25 % and 100 % of incoming fibres are deposited on the wet-formed layer.
  • the flow rate should be lower than 10 m/s, and the fibre concentrazion in the air flow should not exceed 10 % .
  • wet-forming on a fourdrinier wire is shown, but alternatively the forming can be carried out by means of twin wire, in such a way that the dry fibres are deposited when one wire has left the wet-formed layer.
  • dry fibres can be deposited on one side of the wet-formed layer while it is on the forming wire, so that a second fibre layer arises. Thereafter the web thus formed is transferred to a second wire whereby dry fibres are deposited also on the rear side of the wet-formed layer while it is still wet, so that a third fibre layer is formed in the same way as the second fibre layer.

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Paper (AREA)
  • Materials For Medical Uses (AREA)
  • Diaphragms For Electromechanical Transducers (AREA)
  • Sanitary Thin Papers (AREA)
  • Ultra Sonic Daignosis Equipment (AREA)
  • Amplifiers (AREA)
  • Laminated Bodies (AREA)
  • Multicomponent Fibers (AREA)

Abstract

Soft paper from cellulose fibres is manufactured by wet-forming a first fibre layer. Thereafter air-borne dry fibres are deposited directly on one or both sides of the wet-formed layer while this is still wet, so that a second and possibly a third fibre layer are formed on the first one. Fibre bindings thereby arise between the layers. The wet-formed fibre layer gives the soft paper its strength, while the dry-formed fibres give a soft surface.

Description

Method of making soft paper
This invention relates to the making of soft paper from cellulose fibres.
Soft paper is a common denomination for paper used for absorbing purposes, such as tissue, drying cloth, napkins and handkerchiefs. Soft paper competes with woven fabrics, but in contrast to them is intended for one-way use. The properties desired are rapid and effective absorption, soft and smooth structure and good strength also in wet state.
Soft paper is manufactured mainly by wet forming, i.e. a fibre suspension in water is caused to flow out on a running wire where it is dewatered and then dried. High-
-speed machines with wire speeds of between 500 and 2000 m/min are used. The grammage is 20-30 g/m2. For giving the paper necessary extensibility and softness, criping is carried out usually by means of a so-called Yankee cylinder where the paper web is scraped off after drying.
A small amount of soft paper is manufactured by dry- -forming, i.e. dried papermaking pulp is fluffed whereafter air-borne fibres without addition of water are deposited on an air-pervious wire. Binding is effected by means of suitable chemical binding agents. Soft paper manufactured in this way is very bulky, i.e. has a very loose structure. The machine speed must be low, about 50 m/min. The manufacturing cost is very high, and the products have to be sold at a high price.
Dry-formed soft paper, thus, has a higher bulk than wet-formed paper. The reason of this is that the fibres in the dry-formed paper have not been softened in water and, therefore, are not bent down into the paper plane. Furthermore, no water has to be drained through the structure and, therefore, no capillary forces contract the structure at the removal of water by drying. At dry-forming the fibres deposit at random in all directions both in the plane of the paper and perpendicularly thereto, while at wet- -forming the fibres substantially deposit in the plane of the paper.
Dry-forming yields almost unbound fibres. In order to obtain necessary strength without water addition, chemical binding agents are used. This implies, that the binding level in the final product can be controlled, and no crêping is required. Binding agents, however, are expensive, and the amount required thereof costs as much as the fibre raw material.
The high manufacturing cost for dry-formed soft paper is the main reason why this paper has such a small share of the market.
The present invention is a combination of wet-forming and dry-forming whereby the advantages of both methods have been utilized. According to the invention, air-borne fibres are deposited directly on a wet-formed layer while the layer is still wet. Its dry solids content preferably should be 5-25 % . The dry-formed layer should not have too great a thickness. Preferably every dry-formed fibre should meet the wet-formed layer. This implies in praetice a grammage of 2-20 g/m2. Between the two layers fibre bindings arise which ensure good cohesion of the layers.
A particularly advantageous quality of soft paper is obtained by depositing air-borne dry fibres on both sides of the wet-formed layer.
Owing to the invention, the manufactured soft paper has a soft and smooth surface, higher bulk than wet-formed paper and higher strength than dry-forned paper without addition of chemicals. The method according to the invention also results in high internal bond strength (z-strength) in spite of the absence of special binding agents. The machine speed for wet-forming, i.e. 500-2000 m/min, can be maintained. The invention is described in greater detail in the following by way of an embodiment thereof, with reference to the accompanying Figure showing schematically an arrangement for the manufacture of soft paper.
From a head box 1 a fibre suspension flows out onto a running wire 2 thereby forming a first fibre layer in a wet manner on the wire. Dewatering takes place through suction boxes 3 located beneath the wire 2.
Air-borne dry fibres are deposited directly on the wet- -formed layer,while it is still wet, by means of a forming box 4 located above the wire 2 and a vacuum box 5 located beneath the wire. The dry fibres thereby form a second fibre layer on the first one. Between the layers fibre bindings arise. The dry fibres are exposed in a defibering device 6, for example a hammer mill or coarse shredder, followed by a refiner for fluffing. The fibres are transported by means of a fan 7 to the forming box 4 , which can be of the type shown in patent application SE 85 05 918-6. Reject discharged from the forming box 4 through a conduit 8 can be re-cycled, possibly after renewed defibering.
The wet-formed layer shall have a grammage of 10-100g/m2. The wet-formed layer, at:-.the application of the air-borne dry fibres, shall have been dewatered to a dry solids content of 5-25 % . The dry fibres preferably should have been taken from chemical pulp in order to yield a surface of high softness.
At the dry-forming the fibres shall be well dispersed in the air. For ensuring this, the flow rate in the inlet to the forming box shall exceed 100 m/s.
The distribution between the reject flow through the conduit 8 and the fibre flow dry-formed on the wet-formed layer shall be so that between 25 % and 100 % of incoming fibres are deposited on the wet-formed layer. When the dry fibres adhere on the wet-formed layer, the flow rate should be lower than 10 m/s, and the fibre concentrazion in the air flow should not exceed 10 % .
In the Figure wet-forming on a fourdrinier wire is shown, but alternatively the forming can be carried out by means of twin wire, in such a way that the dry fibres are deposited when one wire has left the wet-formed layer.
At the manufacture of soft paper with dry- formed fibre layers on both sides of the wet-formed layer, dry fibres can be deposited on one side of the wet-formed layer while it is on the forming wire, so that a second fibre layer arises. Thereafter the web thus formed is transferred to a second wire whereby dry fibres are deposited also on the rear side of the wet-formed layer while it is still wet, so that a third fibre layer is formed in the same way as the second fibre layer.
The invention is not restricted to the embodiments described, but can be varied within the scope of the inventon idea.

Claims

Claims
1. A method of manufacturing soft paper from cellulose fibres, comprising wet-forming of a first fibre layer, c h a r a c t e r i z e d i n that air-borne dry fibres are deposited directly on the wet-formed layer while this is still wet, so that a second fibre layer is formed on the first one, whereby fibre bindings between the layers arise.
2. A method as defined in claim 1, c h a r a c t e r i z e d i n that the dry-formed layer is deposited to a grammage of 2-20 g/m2.
3. A method as defined in claim 1 or 2, c h a r a c te r i z e d i n that the forming of the layers takes place at a speed of 500-2000 m/min.
4. A method as defined in any one of the preceding claims, c h a r a c t e r i z e d i n that the wet- -forming of the first layer takes place on a running fourdrinier wire, and the second layer is dry-formed on the first layer while it is still on the wire.
5. A method as defined in any one of the preceding claims, c h a r a c t e r i z e d i n that the wet- -formed layer has a dry solids content of 5-25% at the application of the air-borne dry fibres thereon.
6. A method as defined in any one of the preceding claims, c h a r a c t e r i z e d i n that air-borne dry fibres are deposited directly also on the opposite side of the wet-formed layer while this is still wet, so that a third fibre layer is formed on the first one.
PCT/SE1987/000424 1986-10-02 1987-09-22 Method of making soft paper WO1988002416A1 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
AT87906631T ATE66980T1 (en) 1986-10-02 1987-09-22 PROCESS FOR MAKING SOFT PAPER.
DE8787906631T DE3772774D1 (en) 1986-10-02 1987-09-22 METHOD FOR PRODUCING SOFT PAPER.
NO882404A NO170500C (en) 1986-10-02 1988-06-01 PROCEDURE FOR MANUFACTURING TISSUE PAPER
FI891577A FI100899B (en) 1986-10-02 1989-03-31 Procedure for making tissue paper

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE8604190A SE454521B (en) 1986-10-02 1986-10-02 SET FOR MANUFACTURING TOWELS
SE8604190-2 1986-10-02

Publications (1)

Publication Number Publication Date
WO1988002416A1 true WO1988002416A1 (en) 1988-04-07

Family

ID=20365800

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/SE1987/000424 WO1988002416A1 (en) 1986-10-02 1987-09-22 Method of making soft paper

Country Status (12)

Country Link
US (1) US5061344A (en)
EP (1) EP0332618B1 (en)
JP (1) JP2520682B2 (en)
AT (1) ATE66980T1 (en)
AU (1) AU596455B2 (en)
CA (1) CA1319287C (en)
DE (1) DE3772774D1 (en)
FI (1) FI100899B (en)
NO (1) NO170500C (en)
NZ (1) NZ222004A (en)
SE (1) SE454521B (en)
WO (1) WO1988002416A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005118955A1 (en) * 2004-05-28 2005-12-15 Kimberly-Clark Worldwide, Inc. Wet-laid tissue sheet having an air-laid outer surface

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5928472A (en) * 1997-09-03 1999-07-27 Watkins; Kenneth S. Paper web and process for making the same
GR1003296B (en) * 1998-07-03 2000-01-18 New method for the production of a soft and voluminous sheet and the product produced by it.
MY162376A (en) 2009-08-05 2017-06-15 Shell Int Research Method for monitoring a well
PL2462276T3 (en) 2009-08-05 2015-04-30 Int Paper Co Dry fluff pulp sheet additive
PL2462277T3 (en) 2009-08-05 2015-04-30 Int Paper Co Process for applying composition containing a cationic trivalent metal and debonder and fluff pulp sheet made from same
PL2365129T3 (en) * 2010-03-04 2013-12-31 Duni Ab New material
ES2952420T3 (en) 2010-07-20 2023-10-31 Int Paper Co Composition containing a multivalent cationic metal and an amine-containing antistatic agent and methods of manufacture and use
CN103003488B (en) 2010-07-22 2015-04-15 国际纸业公司 Process for preparing fluff pulp sheet with cationic dye and debonder surfactant and fluff pulp sheet made from same
US11834240B2 (en) 2013-09-06 2023-12-05 David P. Goodrich Expanded slit sheet cushioning products with novel alternating expansion patterns
WO2015035335A1 (en) 2013-09-06 2015-03-12 David Goodrich Expandable slit sheet packaging material that interlocks when layered and expanded
US10226907B2 (en) * 2014-09-08 2019-03-12 David P. Goodrich Expandable slit sheet packaging material that interlocks when layered and expanded

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3954554A (en) * 1972-09-09 1976-05-04 Karl Kroyer St. Anne's Limited Multi-ply paper and paperboard having a wet-laid ply and a dry-laid ply
SE388447B (en) * 1975-02-07 1976-10-04 Rottneros Ab PROCEDURE FOR PRODUCTION OF SHEETS OF CELLULOSIAN FIBERS WITH EVEN THICKNESS
US4046622A (en) * 1973-08-23 1977-09-06 Karl Kroyer St. Anne's Limited Multi-ply fibrous sheets having a wet-laid ply and a dry-laid ply

Family Cites Families (5)

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Publication number Priority date Publication date Assignee Title
US2057166A (en) * 1931-02-27 1936-10-13 Brown Co Manufacture of sheeted fiberbinder products
US2913365A (en) * 1954-12-01 1959-11-17 C H Dexter & Sons Inc Fibrous webs and method and apparatus for making same
US2881072A (en) * 1956-01-17 1959-04-07 Fibrofelt Corp Method of making reinforced multiply paper
US4486268A (en) * 1981-05-04 1984-12-04 Kimberly-Clark Corporation Air/water hybrid former
US4464224A (en) * 1982-06-30 1984-08-07 Cip Inc. Process for manufacture of high bulk paper

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3954554A (en) * 1972-09-09 1976-05-04 Karl Kroyer St. Anne's Limited Multi-ply paper and paperboard having a wet-laid ply and a dry-laid ply
US4046622A (en) * 1973-08-23 1977-09-06 Karl Kroyer St. Anne's Limited Multi-ply fibrous sheets having a wet-laid ply and a dry-laid ply
SE388447B (en) * 1975-02-07 1976-10-04 Rottneros Ab PROCEDURE FOR PRODUCTION OF SHEETS OF CELLULOSIAN FIBERS WITH EVEN THICKNESS

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005118955A1 (en) * 2004-05-28 2005-12-15 Kimberly-Clark Worldwide, Inc. Wet-laid tissue sheet having an air-laid outer surface

Also Published As

Publication number Publication date
FI100899B (en) 1998-03-13
NO882404L (en) 1988-06-01
US5061344A (en) 1991-10-29
NO882404D0 (en) 1988-06-01
NO170500C (en) 1992-10-21
FI891577A (en) 1989-03-31
EP0332618B1 (en) 1991-09-04
FI891577A0 (en) 1989-03-31
DE3772774D1 (en) 1991-10-10
NZ222004A (en) 1989-01-06
SE8604190D0 (en) 1986-10-02
JP2520682B2 (en) 1996-07-31
SE454521B (en) 1988-05-09
AU8036987A (en) 1988-04-21
ATE66980T1 (en) 1991-09-15
JPH02500453A (en) 1990-02-15
CA1319287C (en) 1993-06-22
NO170500B (en) 1992-07-13
EP0332618A1 (en) 1989-09-20
AU596455B2 (en) 1990-05-03

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