WO1990000213A1 - Materiau a base de lignocellulose et procede de fabrication d'un tel materiau - Google Patents
Materiau a base de lignocellulose et procede de fabrication d'un tel materiau Download PDFInfo
- Publication number
- WO1990000213A1 WO1990000213A1 PCT/SE1989/000357 SE8900357W WO9000213A1 WO 1990000213 A1 WO1990000213 A1 WO 1990000213A1 SE 8900357 W SE8900357 W SE 8900357W WO 9000213 A1 WO9000213 A1 WO 9000213A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- pulp
- web
- solids content
- dry solids
- accordance
- 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.)
- Ceased
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
-
- 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
- D21H11/08—Mechanical or thermomechanical pulp
Definitions
- FIG 1 is a schematic block view which illustrates a known process for the manufacturing of sheet structures from pulp suspensions. Reference to this known process is made below, under the heading "Standpoint of Techniques”.
- the pulp sheet produced in accordance with the invention was substantially thinner than that of the sheet produced in accordance with the known technique.
- the method of the invention also had a pronounced effect on pulp density and the increase, expressed in rela ⁇ tive percent, is about 35%. Considering that the pulp web was compressed in a dry state and at a speed of 58 m/minute, the result is surprisingly good.
- Long-fibre spruce pulp obtained by fractionation in accordance with US-A-4,562,969 was produced in a groundwood pulp mill.
- the fractionated pulp was placed in a container and transported to the CTMP-mill according to Example 1.
- the pulp was slushed in a pulper (not shown in the Figure) in a conventional manner and then diluted with water to a pulp consistency of 1.2%.
- the pulp suspension was passed through a conduit 2 (see Figure 2) to a headbox 3 and deposited on a wire .
- the pulp suspension was dewatered on the wire to a pulp concentration (pc) of 26%.
- the pulp web was then pressed in three stages.
- the pulp web com ⁇ pressed in accordance with the invention was then further dried in a second drying section 11, to a dry solids content of 91.3%.
- the pulp web was then reeled onto a reeling drum. Smaller and narrower rolls were produced from the jumbo-reel and delivered to consumers, e.g. converters.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Paper (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Nonwoven Fabrics (AREA)
Abstract
La présente invention se rapporte à un matériau à base de lignocellulose ayant une structure stratifiée et une teneur en particules solides sèches supérieure à 80 %, de préférence à 85 %. Ledit matériau se caractérise par une densité comprise entre 400 et 575 kg/m3 mesurée selon le procédé standard SCAN-P7:75 et par une capacité de désintégration (calculée comme la quantité d'énergie électrique consommée pendant la désintégration du matériau dans un broyeur à marteaux) comprise entre 30 et 60 kWh/tonne de pulpe, de préférence entre 35 et 50 kWh/tonne de pulpe. En outre, après avoir été désintégré, la matériau présente une masse volumique en vrac de 15 à 23 cm3/g mesurée selon le procédé standard SCAN-C33:80 et une résistance de réticulation de 2 à 4,5 N. La présente invention se rapporte également à un procédé servant à produire une bande formée au mouillé en continu de matériau à base de lignocellulose et consistant à égoutter et à presser la bande jusqu'à ce qu'elle présente une teneur en particules solides sèches comprise entre environ 30 et 60 %, puis à sécher la bande. Ledit procédé se caractérise par la compression de la bande formée au mouillé ayant une teneur en particules solides sèches d'au moins 50 %, de préférence d'au moins 80 %, au moyen d'une pression linéaire produisant un accroissement de la masse volumique de plus de 10 %.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SE8802450-0 | 1988-06-29 | ||
| SE8802450A SE461472B (sv) | 1988-06-29 | 1988-06-29 | Lignocellulosamaterial med arkstruktur foer torrdesintegrering och foerfarande foer framstaellning daerav |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1990000213A1 true WO1990000213A1 (fr) | 1990-01-11 |
Family
ID=20372775
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/SE1989/000357 Ceased WO1990000213A1 (fr) | 1988-06-29 | 1989-06-21 | Materiau a base de lignocellulose et procede de fabrication d'un tel materiau |
Country Status (2)
| Country | Link |
|---|---|
| SE (1) | SE461472B (fr) |
| WO (1) | WO1990000213A1 (fr) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2925533A1 (fr) * | 2007-12-20 | 2009-06-26 | Inst Francais Du Petrole | Procede de conversion de solutions lignocellulosiques a haute teneur en matiere seche |
| US8871054B2 (en) | 2010-07-22 | 2014-10-28 | International Paper Company | Process for preparing fluff pulp sheet with cationic dye and debonder surfactant |
| US8974636B2 (en) | 2010-07-20 | 2015-03-10 | International Paper Company | Composition containing a multivalent cationic metal and amine-containing anti-static agent and methods of making and using |
| US9260820B2 (en) | 2009-08-05 | 2016-02-16 | International Paper Company | Composition containing a cationic trivalent metal and debonder and methods of making and using the same to enhance fluff pulp quality |
| US10260201B2 (en) | 2009-08-05 | 2019-04-16 | International Paper Company | Process for applying composition containing a cationic trivalent metal and debonder and fluff pulp sheet made from same |
| US10415190B2 (en) | 2009-08-05 | 2019-09-17 | International Paper Company | Dry fluff pulp sheet additive |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3047453A (en) * | 1959-04-06 | 1962-07-31 | Sprout Waldron & Co Inc | Pulp handling system, method and apparatus |
| US3627630A (en) * | 1969-12-04 | 1971-12-14 | Beloit Corp | Method of flash drying pulp |
| US4112587A (en) * | 1976-02-09 | 1978-09-12 | A. Ahlstrom Osakeyhtio | Method and means for drying a fibre material containing cellulose |
-
1988
- 1988-06-29 SE SE8802450A patent/SE461472B/sv not_active Application Discontinuation
-
1989
- 1989-06-21 WO PCT/SE1989/000357 patent/WO1990000213A1/fr not_active Ceased
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3047453A (en) * | 1959-04-06 | 1962-07-31 | Sprout Waldron & Co Inc | Pulp handling system, method and apparatus |
| US3627630A (en) * | 1969-12-04 | 1971-12-14 | Beloit Corp | Method of flash drying pulp |
| US4112587A (en) * | 1976-02-09 | 1978-09-12 | A. Ahlstrom Osakeyhtio | Method and means for drying a fibre material containing cellulose |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2925533A1 (fr) * | 2007-12-20 | 2009-06-26 | Inst Francais Du Petrole | Procede de conversion de solutions lignocellulosiques a haute teneur en matiere seche |
| WO2009095549A1 (fr) * | 2007-12-20 | 2009-08-06 | Ifp | Procédé de conversion de solutions lignocellulosiques a haute teneur en matière sèche |
| US8623175B2 (en) | 2007-12-20 | 2014-01-07 | IFP Energies Nouvelles | Process for the conversion of lignocellulosic solutions containing a high proportion of dry material |
| US8940131B2 (en) | 2007-12-20 | 2015-01-27 | IFP Energies Nouvelles | Screw compression process for the conversion of lignocellulosic suspensions containing a high proportion of dry material |
| US9260820B2 (en) | 2009-08-05 | 2016-02-16 | International Paper Company | Composition containing a cationic trivalent metal and debonder and methods of making and using the same to enhance fluff pulp quality |
| US10260201B2 (en) | 2009-08-05 | 2019-04-16 | International Paper Company | Process for applying composition containing a cationic trivalent metal and debonder and fluff pulp sheet made from same |
| US10415190B2 (en) | 2009-08-05 | 2019-09-17 | International Paper Company | Dry fluff pulp sheet additive |
| US10513827B2 (en) | 2009-08-05 | 2019-12-24 | International Paper Company | Composition containing a cationic trivalent metal and debonder and methods of making and using the same to enhance fluff pulp quality |
| US8974636B2 (en) | 2010-07-20 | 2015-03-10 | International Paper Company | Composition containing a multivalent cationic metal and amine-containing anti-static agent and methods of making and using |
| US8871054B2 (en) | 2010-07-22 | 2014-10-28 | International Paper Company | Process for preparing fluff pulp sheet with cationic dye and debonder surfactant |
Also Published As
| Publication number | Publication date |
|---|---|
| SE461472B (sv) | 1990-02-19 |
| SE8802450L (sv) | 1989-12-30 |
| SE8802450D0 (sv) | 1988-06-29 |
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