DE1012377T1 - FUEL PAPER AND PROCESS FOR PRODUCING IT - Google Patents

FUEL PAPER AND PROCESS FOR PRODUCING IT

Info

Publication number
DE1012377T1
DE1012377T1 DE1012377T DE98934054T DE1012377T1 DE 1012377 T1 DE1012377 T1 DE 1012377T1 DE 1012377 T DE1012377 T DE 1012377T DE 98934054 T DE98934054 T DE 98934054T DE 1012377 T1 DE1012377 T1 DE 1012377T1
Authority
DE
Germany
Prior art keywords
paper
process according
reinforcing agent
per ton
weight
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
Application number
DE1012377T
Other languages
German (de)
Inventor
Stefan Hakansson
Bjoern Nilsson
Ing-Marie Ryden
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.)
ASSIDOMAEN STOCKHOLM AB
Original Assignee
ASSIDOMAEN STOCKHOLM AB
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=20407702&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=DE1012377(T1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by ASSIDOMAEN STOCKHOLM AB filed Critical ASSIDOMAEN STOCKHOLM AB
Publication of DE1012377T1 publication Critical patent/DE1012377T1/en
Pending legal-status Critical Current

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
    • D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/02—Chemical or chemomechanical or chemothermomechanical pulp
    • D21H11/04—Kraft or sulfate pulp
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D1/00—Methods of beating or refining; Beaters of the Hollander type
    • D21D1/20—Methods of refining
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F11/00—Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
    • D21F11/006—Making patterned paper
    • 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
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24—Polysaccharides
    • D21H17/28—Starch
    • 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
    • D21H21/14—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 characterised by function or properties in or on the paper
    • D21H21/18—Reinforcing agents
    • 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
    • D21H27/02—Patterned paper
    • 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
    • D21H27/10—Packing paper

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Paper (AREA)
  • Diaphragms For Electromechanical Transducers (AREA)
  • Bag Frames (AREA)
  • Making Paper Articles (AREA)

Abstract

A method for making kraft paper, wherein a sulphate pulp is subjected to HC refining only or to HC refining in combination with LC beating, the LC beating, if applicable, being carried out at a relatively low energy supply, and wherein a strengthening agent, especially a charged polymer, is subsequently added to the stock, preferably at two separate points in the process, in a total amount of at least 8 kg per tonne of paper. Kraft paper with a tensile energy absorption index of 2.5-3.5 J/g at a porosity (Gurley) of less than 10 seconds. A valve sack made of one or more layers of said kraft paper.

Claims (25)

DE/EP 1 012 377 Tl EP 98 934 054.2 ASSIDOMÄN AB PATENTANSPRÜCHEDE/EP 1 012 377 Tl EP 98 934 054.2 ASSIDOMÄN AB PATENT CLAIMS 1. Verfahren zum Herstellen von Kraftpapier, insbesondere mit einem Quadratmetergewicht von ungefähr 50-140 g/m2, vorzugsweise Sackpapier, so beispielsweise für Ventilsäcke, z.B. für Zement, dadurch gekennzeichnet, daß es die Schritte umfaßt, bei denen ein Sulfatzellstoff nur Dickstoffmahlung (HC refining) oder Dickstoffmahlung in Kombination mit Dünnstoffmahlung (LC beating) unterzogen wird, und wenn Dünnstoffmahlung eingesetzt wird, die Energiezufuhr bei der Dünnstoffmahlung auf einem Wert unter 80 kWh pro Tonne Papier, gerechnet als 100 % trockenes Papier, gehalten wird, und bei denen ein Verstärkungswirkstoff, insbesondere ein geladenes Polymer (charged polymer), z.B. Stärke, dem dabei hergestellten Rohstoff an einem oder mehreren separaten Punkten in dem Prozeß zugesetzt wird, bevor der Rohstoff auf das Sieb einer Papiermaschine geleitet wird, und zwar so, daß die Gesamtmenge des Verstärkungswirkstoffes wenigstens 8 kg (gerechnet für Stärke) pro Tonne Papier (gerechnet als 100 % trockenes Papier) beträgt.1. A process for producing kraft paper, in particular with a square metre weight of approximately 50-140 g/m 2 , preferably sack paper, for example for valve sacks, e.g. for cement, characterized in that it comprises the steps in which a sulphate pulp is subjected to only high-density refining (HC refining) or high-density refining in combination with low-density beating (LC beating), and if low-density beating is used, the energy input during the low-density beating is kept at a value below 80 kWh per tonne of paper, calculated as 100% dry paper, and in which a reinforcing agent, in particular a charged polymer, e.g. starch, is added to the raw material produced thereby at one or more separate points in the process before the raw material is fed onto the screen of a paper machine, in such a way that the total amount of the reinforcing agent is at least 8 kg (calculated for starch) per tonne of paper (calculated as 100% dry paper). 2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß der Verstärkungswirkstoff an zwei oder mehr, vorzugsweise zwei, separaten Punkten zugesetzt wird.2. Process according to claim 1, characterized in that the reinforcing agent is added at two or more, preferably two, separate points. 3. Verfahren nach Anspruch 1 oder 2, dadurch gekennzeichnet, daß ein erster Zusatz des Verstärkungswirkstoffs in Verbindung mit der Maschinenbütte der Papiermaschine ausgeführt wird.3. Process according to claim 1 or 2, characterized in that a first addition of the reinforcing agent is carried out in connection with the machine chest of the paper machine. 4. Verfahren nach Anspruch 1, 2 oder 3, dadurch gekennzeichnet, daß ein zweiter Zusatz des trockenen Verstärkungswirkstoffs an oder in Verbindung mit der Mischpumpe der Papiermaschine ausgeführt wird, und zwar vorzugsweise an ihrer Ansaugseite.4. A process according to claim 1, 2 or 3, characterized in that a second addition of the dry reinforcing agent is carried out on or in connection with the mixing pump of the paper machine, preferably on its suction side. 5. Verfahren nach einem der vorangehenden Ansprüche, dadurch gekennzeich net, daß die Dickstoffmahlung bei einer Konsistenz der Fasersuspension ausgeführt wird, die über 15 Gew.-%, vorzugsweise 15-40 Gew.-% liegt.5. Process according to one of the preceding claims, characterized in that the high-density grinding is carried out at a consistency of the fiber suspension which is above 15% by weight, preferably 15-40% by weight. 6. Verfahren nach Anspruch 5, dadurch gekennzeichnet, daß die Konsistenz bei der Dickstoffmahlung auf 28-40 Gew.-%, vorzugsweise 30-34 Gew.-%, gehalten wird.6. Process according to claim 5, characterized in that the consistency during the thick matter grinding is kept at 28-40 wt.%, preferably 30-34 wt.%. 7. Verfahren nach einem der vorangehenden Ansprüche, dadurch gekennzeich net, daß die Dünnstoffmahlung bei einer Konsistenz der Fasersuspension im Bereich von 2-10 Gew.-%, vorzugsweise 3-6 Gew.-% und insbesondere 4 Gew.-%, ausgeführt wird.7. Process according to one of the preceding claims, characterized in that the thin-material grinding is carried out at a consistency of the fiber suspension in the range of 2-10 wt.%, preferably 3-6 wt.% and in particular 4 wt.%. 8. Verfahren nach einem der vorangehenden Ansprüche, dadurch gekennzeich net, daß die Dickstoffmahlung und/oder die Dünnstoffmahlung in einer Kegelmühle ausgeführt wird.8. Method according to one of the preceding claims, characterized in that the thick material grinding and/or the thin material grinding is carried out in a conical mill. 9. Verfahren nach einem der vorangehenden Ansprüche, dadurch gekennzeich net, daß die Energiezufuhr in Zusammenhang mit der Dünnstoffmahlung auf einem Wert nicht über 50, vorzugsweise nicht über 30 und insbesondere nicht über 20 kWh pro Tonne Papier gehalten wird.9. Method according to one of the preceding claims, characterized in that the energy supply in connection with the thin stock grinding is kept at a value not exceeding 50, preferably not exceeding 30 and in particular not exceeding 20 kWh per ton of paper. 10. Verfahren nach einem der vorangehenden Ansprüche, dadurch gekennzeich net, daß die Energiezufuhr bei der Stickstoffmahlung auf einem Wert im Bereich von 150-400, vorzugsweise 200-300 kWh pro Tonne Papier, gerechnet als 100 % trockenes Papier, gehalten wird.10. Process according to one of the preceding claims, characterized in that the energy supply during nitrogen grinding is kept at a value in the range of 150-400, preferably 200-300 kWh per ton of paper, calculated as 100% dry paper. 11. Verfahren nach einem der vorangehenden Ansprüche, dadurch gekennzeich net, daß maximal insgesamt 20 kg des Verstärkungswirkstoffs pro Tonne Papier zugesetzt werden.11. Process according to one of the preceding claims, characterized in that a maximum of 20 kg of the reinforcing agent is added per ton of paper. 12. Verfahren nach einem der vorangehenden Ansprüche, dadurch gekennzeich net, daß bei einem ersten Zusatz 4-10, vorzugsweise 5-8 kg des Verstärkungswirkstoffs pro Tonne Papier zugesetzt werden. 12. Process according to one of the preceding claims, characterized in that in a first addition 4-10, preferably 5-8 kg of the reinforcing agent are added per ton of paper. OE/EP 1 OJ2377T1OE/EP1 OJ2377T1 13. Verfahren nach einem der vorangehenden Ansprüche, dadurch gekennzeich net, daß bei einem zweiten Zusatz 4-10, vorzugsweise 5-8 kg des Verstärkungswirkstoffs pro Tonne Papier zugesetzt werden. 13. Process according to one of the preceding claims, characterized in that in a second addition 4-10, preferably 5-8 kg of the reinforcing agent are added per ton of paper. 14. Verfahren nach einem der vorangehenden Ansprüche, dadurch gekennzeich net, daß bei zwei Zusätzen des Verstärkungswirkstoffs ein im wesentlichen gleicher Gewichtsanteil des Verstärkungswirkstoffs pro Tonne Papier zugesetzt wird.14. Process according to one of the preceding claims, characterized in that when two additions of the reinforcing agent are made, a substantially equal proportion by weight of the reinforcing agent is added per ton of paper. 15. Verfahren nach einem der vorangehenden Ansprüche 1-13, dadurch gekenn zeichnet, daß bei einem ersten Zusatz des Verstärkungswirkstoffs maximal 6 kg zugesetzt werden und bei einem zweiten Zusatz des Verstärkungswirkstoffs mehr als 6 kg pro Tonne Papier zugesetzt werden, d.h. vorzugsweise 5-6 kg bzw. mehr als 6 und bis zu 8 kg pro Tonne Papier.15. Process according to one of the preceding claims 1-13, characterized in that in a first addition of the reinforcing agent a maximum of 6 kg are added and in a second addition of the reinforcing agent more than 6 kg per ton of paper are added, ie preferably 5-6 kg or more than 6 and up to 8 kg per ton of paper. 16. Verfahren nach einem der vorangehenden Ansprüche, dadurch gekennzeich net, daß beim Trocknen der Papierbahn, die das Sieb der Papiermaschine verläßt, die Papierbahn mit einer Prägeeinrichtung, die ein Prägesieb umfaßt, geprägt wird.16. Method according to one of the preceding claims, characterized in that during drying of the paper web leaving the screen of the paper machine, the paper web is embossed with an embossing device comprising an embossing screen. 17. Verfahren nach Anspruch 16, dadurch gekennzeichnet, daß das Prägesieb in bezug auf die Papierbahn separat angetrieben wird, wobei das Prägesieb vorzugsweise langsamer oder schneller angetrieben wird als die Papierbahn.17. Method according to claim 16, characterized in that the embossing screen is driven separately with respect to the paper web, wherein the embossing screen is preferably driven slower or faster than the paper web. 18. Kraftpapier, insbesondere mit einem Quadratmetergewicht von 50-140 g/m2, vorzugsweise Sackpapier, so beispielsweise für Ventilsäcke, z.B. für Zement, ge kennzeichnet durch die folgende Kombination physischer Daten:18. Kraft paper, in particular with a weight of 50-140 g/m 2 , preferably sack paper, such as for valve bags, e.g. for cement, characterised by the following combination of physical data: Zugenergieabsorptionsindex 2,5-3,5 J/g bei einer Gurley-Porosität von weniger als 10 Sekunden, vorzugsweise weniger als 7 Sekunden.Tensile energy absorption index 2.5-3.5 J/g at a Gurley porosity of less than 10 seconds, preferably less than 7 seconds. 19. Kraftpapier nach Anspruch 18, gekennzeichnet durch einen Zugenergieabsorptionsindex von 2,7-3,5 J/g bei einer Gurley-Porosität von weniger als 10 Sekunden, vorzugsweise weniger als 7 Sekunden, insbesondere bei einem ungebleichten Papier.19. Kraft paper according to claim 18, characterized by a tensile energy absorption index of 2.7-3.5 J/g at a Gurley porosity of less than 10 seconds, preferably less than 7 seconds, in particular for an unbleached paper. 20. Kraftpapier nach Anspruch 19, dadurch gekennzeichnet, daß es einen Zugenergieabsorptionsindex von ungefähr 3 J/g bei einer Gurley-Porosität von ungefähr 5 Sekunden aufweist.20. Kraft paper according to claim 19, characterized in that it has a tensile energy absorption index of about 3 J/g at a Gurley porosity of about 5 seconds. 21. Kraftpapier nach Anspruch 19 oder 20, das mit dem Verfahren nach einem der Ansprüche 1-17 hergestellt werden kann.21. Kraft paper according to claim 19 or 20, which can be produced by the process according to any of claims 1-17. 22. Ventilsack, der aus einer oder mehreren Schichten aus Kraftpapier nach einem der Ansprüche 18-21 besteht.22. Valve bag consisting of one or more layers of kraft paper according to any one of claims 18-21. 23. Ventilsack nach Anspruch 22, dadurch gekennzeichnet, daß er keine Perforationen aufweist.23. Valve bag according to claim 22, characterized in that it has no perforations. 24. Ventilsack nach Anspruch 22 oder 23, dadurch gekennzeichnet, daß er aus zwei Schichten aus dem Kraftpapier besteht, wobei die Schichten jeweils ein maximales Quadratmetergewicht von 70 g/m2 haben.24. Valve bag according to claim 22 or 23, characterized in that it consists of two layers of kraft paper, the layers each having a maximum weight per square meter of 70 g/m 2 . 25. Ventilsack nach Anspruch 22, 23 oder 24, dadurch gekennzeichnet, daß er aus lediglich einer Schicht aus dem Kraftpapier besteht, wobei die Schicht ein maximales Quadratmetergewicht von 120 g/m2 hat.25. Valve bag according to claim 22, 23 or 24, characterized in that it consists of only one layer of the kraft paper, the layer having a maximum square meter weight of 120 g/m 2 .
DE1012377T 1997-07-09 1998-07-07 FUEL PAPER AND PROCESS FOR PRODUCING IT Pending DE1012377T1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE9702656A SE510506C2 (en) 1997-07-09 1997-07-09 Kraft paper and process for making this and valve bag
PCT/SE1998/001340 WO1999002772A1 (en) 1997-07-09 1998-07-07 Kraft paper and method for making the same

Publications (1)

Publication Number Publication Date
DE1012377T1 true DE1012377T1 (en) 2000-11-02

Family

ID=20407702

Family Applications (2)

Application Number Title Priority Date Filing Date
DE69806168T Expired - Fee Related DE69806168T2 (en) 1997-07-09 1998-07-07 FUEL PAPER AND METHOD FOR THE PRODUCTION THEREOF
DE1012377T Pending DE1012377T1 (en) 1997-07-09 1998-07-07 FUEL PAPER AND PROCESS FOR PRODUCING IT

Family Applications Before (1)

Application Number Title Priority Date Filing Date
DE69806168T Expired - Fee Related DE69806168T2 (en) 1997-07-09 1998-07-07 FUEL PAPER AND METHOD FOR THE PRODUCTION THEREOF

Country Status (17)

Country Link
EP (1) EP1012377B1 (en)
AT (1) ATE219536T1 (en)
AU (1) AU8365898A (en)
BG (1) BG63849B1 (en)
BR (1) BR9810569B1 (en)
CA (1) CA2295075A1 (en)
CZ (1) CZ297129B6 (en)
DE (2) DE69806168T2 (en)
EE (1) EE04531B1 (en)
ES (1) ES2147169T3 (en)
HU (1) HU222668B1 (en)
PL (1) PL187952B1 (en)
PT (1) PT1012377E (en)
RU (1) RU2208079C2 (en)
SE (1) SE510506C2 (en)
WO (1) WO1999002772A1 (en)
ZA (1) ZA986082B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3786079B1 (en) 2019-08-27 2022-04-06 BillerudKorsnäs AB A paper bag

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SE515722C2 (en) * 2000-01-10 2001-10-01 Valmet Karlstad Ab Heat treatment of ground, chemically prepared pulp suspension
EP1889972A1 (en) * 2006-06-26 2008-02-20 Biltube India Limited Core board
DK2808440T3 (en) 2009-03-30 2019-09-30 Fiberlean Tech Ltd Process for the preparation of nanofibrillar cellulose suspensions
ES2650373T3 (en) 2009-03-30 2018-01-18 Fiberlean Technologies Limited Procedure for the production of nanofibrillar cellulose gels
SI2386682T1 (en) 2010-04-27 2014-07-31 Omya International Ag Process for the manufacture of structured materials using nano-fibrillar cellulose gels
DK2386683T3 (en) 2010-04-27 2014-06-23 Omya Int Ag Process for the preparation of gel-based composite materials
EP2388203A1 (en) * 2010-05-19 2011-11-23 Franco Benedetti Paper sack comprising a combination of sack kraft paper and recycled containerboard paper
JP6198376B2 (en) * 2012-09-12 2017-09-20 日本製紙株式会社 Kraft paper
CN103321084B (en) * 2013-06-21 2016-06-22 杭州特种纸业有限公司 Water suction kraft paper and processing technology thereof
CA2918147A1 (en) 2013-07-18 2015-01-22 Nippon Paper Industries Co., Ltd. Clupak paper
PL2963178T3 (en) * 2014-07-04 2016-12-30 Production of sack paper
RS55155B1 (en) 2014-07-04 2017-01-31 Billerudkorsnaes Ab Coated sack paper
PL3009371T3 (en) 2014-10-15 2017-03-31 Billerudkorsnäs Ab Sack with discontinuous longitudinal seam
RU2676489C1 (en) * 2014-11-28 2018-12-29 Фойт Патент Гмбх Method and device for manufacturing packaging paper
SE539344E (en) 2015-03-02 2020-02-11 Billerudkorsnaes Ab Pulp mixture for production of a paper product with high strength in z-direction
EP3088606A1 (en) * 2015-04-29 2016-11-02 BillerudKorsnäs AB Disintegratable brown sack paper
EP3362508B1 (en) 2015-10-14 2019-06-26 FiberLean Technologies Limited 3d-formable sheet material
ES2666830T3 (en) * 2015-11-10 2018-05-08 Billerudkorsnäs Ab Paper for a vertical wrapping machine
EP3184296B1 (en) 2015-12-21 2017-11-08 BillerudKorsnäs AB Rain resistant paper sack
EP3184694A1 (en) 2015-12-21 2017-06-28 BillerudKorsnäs AB Rainproof paper sack
EP3202979B1 (en) * 2016-02-04 2018-08-22 BillerudKorsnäs AB Liquid packaging paper
EP3211135B1 (en) * 2016-02-29 2018-08-29 BillerudKorsnäs AB High-stretch sackpaper
EP3385445B1 (en) * 2017-04-06 2019-06-05 BillerudKorsnäs AB Production of highly stretchable paper having satisfactory surface properties
PL3385444T3 (en) * 2017-04-06 2020-01-31 Billerudkorsnäs Ab Production of paper that is highly stretchable in the cross direction
CN112431060B (en) * 2020-11-13 2022-10-21 福建省青山纸业股份有限公司 Production method of environment-friendly craft paper
AT526106B1 (en) * 2022-05-03 2024-02-15 Mondi Ag Kraft paper

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DE3223149C1 (en) * 1982-06-22 1984-01-19 Hermann 4020 Mettmann Frey Process for the production of paper or similar materials
SU1650840A1 (en) * 1989-01-19 1991-05-23 Всесоюзное научно-производственное объединение целлюлозно-бумажной промышленности Bagging paper

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3786079B1 (en) 2019-08-27 2022-04-06 BillerudKorsnäs AB A paper bag

Also Published As

Publication number Publication date
RU2208079C2 (en) 2003-07-10
CZ476399A3 (en) 2000-08-16
EE200000009A (en) 2000-08-15
EE04531B1 (en) 2005-08-15
BG63849B1 (en) 2003-03-31
ES2147169T3 (en) 2002-11-16
ZA986082B (en) 1999-01-26
ES2147169T1 (en) 2000-09-01
HUP0003123A2 (en) 2001-02-28
BG104046A (en) 2000-07-31
HU222668B1 (en) 2003-09-29
PT1012377E (en) 2002-10-31
SE9702656L (en) 1999-01-10
CA2295075A1 (en) 1999-01-21
CZ297129B6 (en) 2006-09-13
ATE219536T1 (en) 2002-07-15
WO1999002772A1 (en) 1999-01-21
SE510506C2 (en) 1999-05-31
PL337972A1 (en) 2000-09-11
HUP0003123A3 (en) 2001-12-28
DE69806168D1 (en) 2002-07-25
SE9702656D0 (en) 1997-07-09
EP1012377A1 (en) 2000-06-28
PL187952B1 (en) 2004-11-30
DE69806168T2 (en) 2002-11-28
AU8365898A (en) 1999-02-08
EP1012377B1 (en) 2002-06-19
BR9810569A (en) 2000-09-19
BR9810569B1 (en) 2008-11-18

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