A PROCESS FOR PRODUCTION OF PAPER MATERIALS WITH IMPROVED WET STRENGTH

Description

[0001] The present invention relates to a process for producing paper materials such as paper, linerboard or corrugated linerboard from unbleached and semi-bleached chemical or semichemical pulp or pulp from recycled fibres.

BACKGROUND OF THE INVENTION

[0002] Linerboard and corrugated medium, used for making corrugated paperboard and corrugated cartons, are commonly made from a suspension of unbleached chemical or semichemical pulp or pulp from recycled fibres.

[0003] Typically, the pulp is treated in a screening process, refined, then mixed with paper making additives in the stock preparation section before the pulp suspension is de-watered on the paper/board machine, and the drained water (so-called white water) is recycled back into the process for dilution of the screened stock.

[0004] The white water will normally contain high amounts of wood fibers/fines, sterol esters, resin acids, lignans, and lignin fragments typically in concentrations of 100-500 ppm or higher; all of this material will have phenolic or phenol-like groups.

[0005] Strength, particularly compression strength, is an important mechanical property of the unbleached board grades used to make corrugated boxes: linerboard and corrugated linerboards. Due to new governmental rules in some countries giving an alternative specification based on combined board edge crush and since combined edge crush can be tied directly to the compression strength of the board's components it is now possible to sell board on a performance per square meter basis rather than only by weight.

[0006] Clearly, the wet strength of unbleached board grades used to make corrugated boxes is also of importance.

[0007] EP 429,422 discloses reduction of energy consumption in the refining stages by use of laccase during pulp preparation between the first and second refining stage; the document indicates that some increase of paper strength is also obtained.

[0008] WO 93/23606 (EP 641 403) discloses a process for treating a mechanical pulp with a phenol-oxidizing enzyme system to increase the strength of the produced paper.

[0009] WO 95/09946 discloses a process for producing linerboard or corrugated medium having increased strength by treating pulp with a phenol-oxidizing enzyme.

[0010] WO 95/07604 discloses a process for producing fibreboard having improved mechanical properties by treating a slurry or suspension of a lignin-containing wood fibre material with a phenol-oxidizing enzyme.

[0011] US 4,687,745 discloses a process for enhancing the strength properties and brightness stability of mechanical pulp by treating the pulp with ligninolytic enzymes.

[0012] The wet strength of paper materials may be enhanced by adding wet strength resins to the pulp. However, these resins will enhance the strength of the paper material in such a way that re-use of the paper material will become difficult.

[0013] It is an object of the present invention to provide a process for producing, from unbleached or semi-bleached chemical or semichemical pulp, paper materials such as paper, linerboard or corrugated linerboard having improved wet strength.

SUMMARY OF THE INVENTION

[0014] The present inventors have now surprisingly found that the wet strength of paper materials can be increased by treating a pulp suspension with a phenol-oxidizing enzyme system combined with a mediator prior to the paper machine and followed by additional applying a heat treatment.

[0015] Accordingly, in a first aspect the present invention relates to a process for producing paper materials with improved wet strength, comprising:

(a) preparing a suspension of unbleached or semi-bleached chemical or semichemical pulp or pulp from recycled fibres;

(b) treating the pulp with a phenol oxidizing enzyme and a mediator; and

(c) de-watering the treated pulp in a paper making machine to remove process water and produce the paper material.

[0016] In a preferred embodiment, the process water from step (c) is recycled, and step (a) comprises dilution of the pulp with the recycled process water. Advantageously, the enzymatic treatment of the pulp and white water suspension will to a large extent polymerize the aromatic materials present in the white water (lignans, resin acids, sterol esters, lignin-like compounds, fibres and fines) so that they are retained in the paper sheet, leading to an increased yield and a decreased COD (chemical oxygen demand) load and toxicity of the effluent. Said polymerization is also believed to contribute to strengthening of the linerboard or corrugated medium.

[0017] In a further preferred embodiment the paper material is heated after the completion of step c).

[0018] In a second aspect the present invention relates to a process for making corrugated paperboard or corrugated boxes using the linerboard and/or corrugated linerboard produced by the process of the invention.

[0019] In a third aspect the present invention relates to the use of a phenol-oxidizing enzyme in combination with a mediator to produce a paper material with improved wet strength.

BRIEF DESCRIPTION OF THE DRAWINGS

[0020] 

Figure 1 shows the wet tensile strength of the sheets produced in Example 1. Data is taken from Table 1. Vertical bars indicate the 95% confidence limit.

Figure 2 shows the wet strength after immersion into distilled water for 24 hours of paper subjected to different treatments as described in Example 2. The following abbreviations have been used:

C: Conventional drying in condition chamber.

H: Heat drying of the wet sheet at 150°C for 5 min.

L: Treatment of pulp with 10 LACU/g for 1 hr.

M: Addition of 50 mM PPT.

[0021] The strength of #1 was below the detection limit of 2.2 Nm/g and was a conservative estimate set to this value in Figure 2. Vertical bars indicate the 95% confidence limit.

DETAILED DESCRIPTION OF THE INVENTION

[0022] In the context of the present invention the term "paper material" refers to products, which can be made out of pulp, such as paper, linerboard, corrugated paperboard, corrugated container or boxes.

[0023] The term "improved wet strength" indicates that the wet strength of the paper material is increased/enhanced in comparison to the paper material which has not be treated according to the invention.

Pulp

[0024] The pulp to be used in the process of the invention is a suspension of unbleached or semi-bleached chemical or semichemical pulp or pulp from recycled fibres. Unbleached or semi-bleached pulp is characterised by containing lignin, which is used as substrate for the enzyme system. The chemical pulp may be unbleached kraft pulp, and the semichemical pulp may be NSSC (neutral sulfite semichemical) pulp. The pulp from recycled fibres may be made from a chemical pulp, such as unbleached kraft pulp. A specific example of recycled fibres made from a chemical pulp includes OCC (old corrugated containers).

[0025] The preparation of the pulp suspension may comprise beating or refining of the pulp, depending on the type of pulp.

Phenol oxidizing enzyme system

[0026] The enzyme system used in the invention consists of a suitable oxidase together with O₂ or a suitable peroxidase together with H₂O₂. Suitable enzymes are those, which oxidize and polymerize aromatic compounds such as phenols and lignin.

[0027] Examples of suitable enzymes are catechol oxidase (EC 1.10.3.1), laccase (EC 1.10.3.2), bilirubin oxidase (EC 1.3.3.5) and peroxidase (EC 1.11.1.7) and haloperoxidases. The peroxidase may be derived from a strain of Coprinus, e.g. C. cinerius or C. macrorhizus, or of Bacillus, e.g. B. pumilus, from soy bean or horse radish. It may be preferable to use two different phenol oxidizing enzymes together.

[0028] Suitable laccases may, for example, be derived from a strain of Polyporus sp., in particular a strain of Polyporus pinsitus (also called Trametes villosa) or Polyporus versicolor, or a strain of Myceliophthora sp., e.g. M. thermophila or a strain of Rhizoctonia sp., in particular a strain of Rhizoctonia praticola or Rhizoctonia solani, or a strain of Scytalidium sp., in particular S. thermophilium, or a strain of Pyricularia sp., in particular Pyricularia oryzae, or a strain of Coprinus sp., such as a C. cinereus.

[0029] The laccase may also be derived from a fungus such as Collybia, Fomes, Lentinus, Pleurotus, Aspergillus, Neurospora, Podospora, Phlebia, e.g. P. radiata (WO 92/01046), Coriolus sp., e.g. C. hirsitus (JP 2-238885), or Botrytis.

[0030] In a preferred embodiment of the invention the laccase is derived from a strain of Polyporus sp., especially the Polyporus pinsitus laccase (in short: PpL).

[0031] The amount of peroxidase should generally be in the range 10-10,000 PODU per g of dry substance (PODU unit of peroxidase activity defined below). The amount of laccase should generally be in the range 0.001-1000 units per g of dry substance (unit of laccase activity defined below).

[0032] Molecular oxygen from the atmosphere will usually be present in sufficient quantity. Thus, contrary to prior art bleaching processes (including laccase and mediator) where a high oxygen pressure is necessary, this will usually not be necessary for the purposes described herein. Therefore, the reaction may conveniently be carried out in an open rector, i.e. at atmospheric pressure.

[0033] A suitable amount of H₂O₂ will usually be in the range 0.01-10 mM, particularly 1-10 mM.

Mediator

[0034] According to the invention the phenol-oxidizing enzyme is used in combination with a suitable redox mediator. A so-called " redox mediator" is sometimes in literature referred to as "an enhancing agent". In the present context the term "mediator" will be used.

[0035] A "mediator" is an agent capable of enhancing the activity of phenol-oxidizing enzymes.

[0036] The mediator may be a phenolic mediator or a non-phenolic mediator. Which mediator is preferred depends of the purpose.

[0037] Examples mediators capable of enhancing the activity of phenol-oxidizing enzymes include the compounds described in WO 95/01426, which is hereby incorporated by reference, and described by the general formula I:

[0038] The definition of the R1 to R10 and A groups can be found in WO 95/010426 (see pp. 9 to 11).

[0039] Specifically contemplated compounds within the above formula I include the following: 2,2'-azino-bis(3-ethylbenzothiazoline-6-sulfonate (ABTS); 6-hydroxy-2-naphtoic acid; 7-methoxy-2-naphtol; 7-amino-2-naphthalene sulfonic acid; 5-amino-2-naphthalene sulfonic acid; 1,5-diaminonaphthalene; 7-hydroxy-1,2-naphthimidazole; 10-methylphenothiazine; 10-phenothiazine-propionic acid (PPT); N-hydroxysuccinimide-10-phenothiazine-propionate; benzidine; 3,3'-dimethylbenzidine; 3,3'-dimethoxybenzidine; 3,3',5,5'-tetramethylbenzidine; 4'-hydroxy-4-biphenylcarboxylic acid; 4-amino-4'-methoxystilbene; 4,4'-diaminostilbene-2,2'-disulfonic acid; 4,4'-diaminodiphenylamine; 2,7-diaminofluorene; 4,4'-dihydroxy-biphenylene; triphenylamine; 10-ethyl-4-phenothiazinecarboxylic acid; 10-ethylphenothiazine; 10-propylphenothiazine; 10-isopropylphenothiazine; methyl-10-phenothiazinepropionate; 10-phenylphenothiazine; 10-allylphenothiazine; 10-phenoxazinepropionic acid (POP); 10-(3-(4-methyl-1-piperazinyl)propyl)phenothiazine; 10-(2-pyrrolidinoethyl)phenothiazine; 10-methylphenoxazine; iminostilbene; 2-(p-aminophenyl)-6-methylbenzothiazole-7-sulfonic acid; N-benzylidene-4-biphenylamine; 5-amino-2-naphthalenesulfonic acid; 7-methoxy-2-naphtol; 4,4'-dihydroxybenzophenone; N-(4-(dimethylamino)benzylidene)-p-anisidine; 3-methyl-2-benzothiazolinone(4-(dimethylamino)benzylidene)hydrazone; 2-acethyl-10-methylphenothiazine; 10-(2-hydroxyethyl)phenothiazine; 10-(2-hydroxyethyl)phenoxazine; 10-(3-hydroxypropyl)phenothiazine; 4,4'-dimethoxy-N-methyl-diphenylamine, vanillin azine.

[0040] Other mediators contemplated include 4-hydroxybenzoic acid, L-tyrosine, syringate acids, ferulic acid, sinapic acid, chlorogenic acid, caffeic acid and esters thereof.

[0041] Still further examples include organic compounds described in WO 96/10079, which is hereby incorporated by reference, and by the following formula II:

in which formula A is a group such as -D, -CH=CH-D, -CH=CH-CH=CH-D, -CH=N-D, -N=N-D, or -N=CH-D, in which D is selected from the group consisting of -CO-E, -SO₂-E, -N-XY, and -N⁺-XYZ, in which E may be -H, -OH, -R, or -OR, and X and Y and Z may be identical or different and selected from -H and -R; R being a C₁-C₁₆ alkyl, preferably a C₁-C₈ alkyl, which alkyl may be saturated or unsaturated, branched or unbranched and optionally substituted with a carboxy, sulfo or amino group; and B and C may be the same or different and selected from C_mH_2m+1; 1 ≤ m ≤ 5.

[0042] Specific compounds covered by the above formula I are acetosyringone, syringaldehyde, methylsyringate, syringic acid, ethylsyringate, propylsyringate, butylsyringate, hexylsyringate, octylsyringate and ethyl 3-(4-hydroxy-3,5-dimethoxyphenyl).

[0043] Other suitable mediators are vanillic acid, NHA, HOBT, PPO and violoric acid.

Process conditions

[0044] The enzyme treatment can be done at conventional consistency, e.g., 0.5-25% (particularly 0.5-10%) dry substance, at temperatures of 20-90°C and at a pH of 4-10. Furthermore, the enzyme (and mediator) treatment may be carried out at atmospheric pressure.

[0045] The enzyme activity when using a laccase is 0.001-1000 LACU per gram of dry substance.

Determination of peroxidase activity (PODU)

[0046] Peroxidase activity is determined from the oxidation of 2,2'-azinobis(3-ethylbenzothiazoline-6-sulfonate) (ABTS) by hydrogen peroxide. The greenish-blue color produced is photometered at 418 nm. The analytical conditions are 0.88 mM hydrogen peroxide, 1.67 mM ABTS, 0.1 M phosphate buffer, pH 7.0, 30°C, 3 minutes reaction.

[0047] 1 peroxidase unit (PODU) is the amount of enzyme that catalyses the conversion of 1 mmol hydrogen peroxide per minute at these conditions.

Determination of laccase activity (LACU)

[0048] Laccase activity was determined by a similar method without addition of hydrogen peroxide. 1 laccase unit (LACU) is defined as the amount of enzyme which under standard conditions (pH 5.5, 30°C) oxidizes 1 mmol syringaldazine per minute.

[0049] The invention is further illustrated by the following nonlimiting examples.

EXAMPLES

Example 1 (not according to the present invention)

[0050] A beaten and unbleached kraft pulp kappa 85 obtained from the Obbola mill in Sweden was disintegrated in a laboratory disintegrator and diluted to at consistency of 1%. As water phase was used either tap water or white water from the Obbola mill. pH was adjusted to 5.5 ±0.1 with 1 M sulphuric acid and this was maintained by further addition of acid. An enzyme dosage of 15 LACU/g dry pulp (laccase derived from Polyporus pinsitus) was added and the suspension was stirred for 1 hour.

[0051] Isotropic sheets with a specific weight of 150 g/m² were formed on a semiautomatic papermaker of the Rapid-Konthen type. When comparing the tensile strength of sheets subjected to different treatment it is of crucial importance that the sheets have the same density. Heat drying of a sheet increases its density, and to compensate for this, sheets to be air-dried were pressed to a higher density than sheets to be heat-dried.

[0052] A trial was performed comprising the following variables: White water, laccase and heat drying.

[0053] In experiments without white water, the pulp was suspended in distilled water. Heat dried sheets were dried in oven at 170°C and were stacked with each sheet separated by blotting paper and placed with a weight on top to prevent shrinkage. All blotting papers were replaced after 20, 30 and 40 min. After heat drying all sheets were placed in a condition chamber at 50% RH and 23°C overnight. Sheets not heat dried were dried conventionally in condition chamber at 65% RH and 21 °C.

[0054] Test of tensile strength was performed after SCAN-P67 with 10 test strips. Permanent wet tensile strength was tested after immersion of the test piece into distilled water for 24 hr.

[0055] For each of the 8 treatments, 5 sheets were made. The same batch of pulp and white water was used for all treatments, and the entire experiment was carried out on the same day. Data were analysed with the statistical software package SAS.

Results:

[0056] The obtained results are compiled in Table 1 and Figure 1. From Table 1 it can be seen that the density between the sheets differ somewhat, which should be borne in mind when interpreting the results.

Table 1:

Heat drying 170°C. Result from experiments comprising: White water, PpL laccase and heat drying at 170°C
Exp. No.	White water	15 LACU/g	Drying 170°C	Specific weigth (g/m2)	Density (kg/m3)	Wet tensile index (kNm/kg)
1	-	-	-	154.8	710	2.56
2	+	-	-	154.7	710	2.73
3	-	+	-	155.4	713	3.13
4	+	+	-	166.2	717	3.48
5	-	-	+	154.8	704	5.30
6	+	-	+	152.8	661	5.63
7	-	+	+	153.8	660	6.04
8	+	+	+	161.6	682	6.64

[0057] The main effects are shown in Table 2 with the corresponding least significant difference (LSD) values.

Table 2:

Main effect of variables (difference between means of the variables at high and low level). Significance at the 0.05 level is indicated by *** based on a T-test. Least significant differences (LSD) on the 0.05 level written in parentheses. All values are in Nm/g.
Effect	Wet tensile strength (LSD 0.33)
White water	0.36***
Enzyme (15 LACU/g)	0.77***
Heat drying at 170 °C	2.93***

[0058] The wet tensile strength was significantly affected by all variables. Heat drying had the highest impact on the wet tensile strength with almost 3 Nm/g followed by the laccase treatment with 0.8 Nm/g. The increase in wet tensile strength by adding enzyme to a pulp suspended in white water and where the sheets are heat-dried, is in the order of 20% (compare experiments Nos. 6 and 8) .

Example 2

[0059] A beaten and unbleached kraft pulp kappa 85 obtained from the Obbola mill in Sweden was disintegrated in a laboratory disintegrator and diluted to a consistency of 1%. pH was kept at 5.5 using a 0.05 M sodium acetate buffer. PpL laccase and a mediator were added and the slurry stirred for 1 hour at room temperature. The enzyme dosage was 10 LACU/g dry pulp in all experiments.

[0060] Isotropic handsheets with a specific weight of 150 g/m2 were made of the modified pulp according to SCAN-P:26. In those experiments where the sheets was subjected to a heat treatment this was done to the wet sheets immediately after the second pressing step in a restrained dryer at 150°C for 5 min, and was then conditioned at 65% RH and 23°C.

[0061] All other sheets were dried in a conditioning chamber at 65% RH and 21°C. The dry- and wet tensile strength were determined according to SCAN-P:38. Before measuring the wet tensile strength, the test strip was immersed in distilled water for 1 or 24 hour.

Results:

[0062] A standard method for testing the strength of a chemical pulp was used, where the sheets were dried in a condition chamber at 65% RH and 21°C. The obtained results are compiled in Figure 2.

[0063] As can be seen from Figure 2, the laccase mediator (PPT) treatment gives a significantly increase in the wet tensile strength of the linerboard, both when the paper is subjected to heat treatment (experiments Nos. 3 and 6) and when not subjected to heat treatment (Nos. 1 and 2). Heat treatment of paper is known to confer wet strength, possibly through generation of covalent bonds between cellulose chains, but the treatment of the pulp with laccase and PPT increased this effect by about 50%, cf. Figure 2.

[0064] Addition of PPT or laccase alone (experiments Nos.4 and 5), did not change the wet tensile strength of the heat treated paper. This was also observed when the paper was not heat-treated (not shown).

[0065] Table 3 shows the wet tensile strength of paper sheets made from kraft pulp oxidised with laccase and different mediators prior to sheets formation. Although the error within an experiment was low, the day-to-day variation was rather high, and therefore the effect of a given mediator should be evaluated by comparing all values to the control sheet within the same experiment. By doing so, it becomes evident that PPT, followed by ABTS, yields the highest wet strength.

[0066] Under the right conditions, heat treatment of paper is known to increase the wet strength up to a value of 30% of the dry strength (Stenberg, E.L., Svensk Papperstidning 8:49-54, 1978).

[0067] In this study it was tested if the effects of the laccase/mediator treatment shown in Table 3 could be further increased by combining this with a heat treatment of the paper. It was chosen to apply the heat treatment to the paper as soon as possible after the oxidation with laccase and PPT, and was therefore given after pressing the wet sheet. From the data depicted in Figure 2, it can be seen that the heat treatment itself more than doubles the wet strength. Adding laccase alone or PPT to the pulp before the heat treatment does not effect the wet strength, but using a combination of laccase and PPT gives an increase of 50% in wet strength of the heat-treated paper.

[0068] It should be noted that all wet tensile strength in this part of the report was tested after 24 hours immersion. When a sheet made from pulp oxidised with laccase and PPT and then heat dried, was immersed for only 1 hour a wet tensile strength of 10 Nm/g could be measured (not shown).

Claims

1. A process for producing paper materials with improved wet strength, comprising:

(a) preparing a suspension of unbleached or semi-bleached chemical or semichemical pulp or pulp from recycled fibres;

(b) treating the pulp with a phenol oxidizing enzyme and a mediator;

(c) de-watering the treated pulp in a paper making machine to remove process water and produce the paper material, and;

(d) heat drying the paper material.

2. The process according to claim 1, wherein the mediator is 1 0-phenothiazine-propionic acid (PPT) or 2,2'-azino-bis(3-ethylbenzothiazoline-6-sulfonate (ABTS).

3. The process according to claim 2, wherein the heating is carried out at a temperature above 100°C.

4. The process according to claim 3, wherein the heating is carried out at a temperature above 150°C.

5. The process according to any of claims 1-4, wherein at least a part of the process water from step (c) is recycled, and step (a) comprises dilution of the pulp with the recycled process water.

6. The process according to any of claims 1-5, wherein the enzyme is an oxidoreductase, preferable a laccase.

7. The process according to claim 6, wherein the laccase is derived from Polyporus pinsitus.

8. The process according to claims 6 or 7, wherein the oxidoreductase is present in an amount of 10-10,000 PODU per gram of dry matter or 0.001-1000 LACU per gram of dry matter.

9. The process according to any of claims 1-8, wherein the enzyme treatment is performed on a pulp having a consistency of 0.5-25%, a pH of 4-10, and a temperature of 20-90°C.

10. The process according to any of claims 1-9, wherein the enzyme treatment is carried out at atmospheric pressure.

11. The process according to any of the claims 1-10, wherein the pulp is unbleached or semi-bleached kraft pulp, neutral sulfite semichemical pulp, or recycled pulp from old corrugated containers.

12. The process according to claim 11, wherein the recycled pulp from old corrugated containers is an unbleached kraft pulp.

13. A process for producing corrugated paperboard or corrugated containers, comprising producing linerboard and/or corrugated linerboard by the process according to claim 1, and combining linerboard and corrugated linerboard to produce the corrugated paperboard or container.

Ansprüche

1. Verfahren zur Herstellung von Papier-Werkstoffen mit einer verbesserten Nassfestigkeit, umfassend

(a) Herstellen einer Suspension von ungebleichtem oder halbgebleichtem, chemischem oder halbchemischem Zellstoff oder Zellstoff von wiederaufbereiteten Fasern;

(b) Behandeln der Zellstoffs mit einem Phenol oxidierenden Enzym und einem Vermittler;

(c) Entwässern des behandelten Zellstoffs in einer Maschine zur Papierherstellung zur Entfernung von Prozess-Wasser und zur Herstellung des Papier-Werkstoffs;

(d) Trocknung des Papier-Werkstoffs durch Erwärmen.

2. Verfahren gemäß Anspruch 1, dadurch gekennzeichnet, dass der Vermittler 10-Phenothiazin-propansäure (PPT) oder 2,2'-Azino-bis(3-ethylbenzothiazolin-6-sulfonat) (ABTS) ist.

3. Verfahren gemäß Anspruch 2, dadurch gekennzeichnet, dass das Erwärmen bei einer Temperatur oberhalb 100 °C durchgeführt wird.

4. Verfahren gemäß Anspruch 3, dadurch gekennzeichnet, dass das Erwärmen bei einer Temperatur oberhalb 150 °C durchgeführt wird.

5. Verfahren gemäß einem der Ansprüche 1 bis 4, dadurch gekennzeichnet, dass wenigstens ein Teil des Prozess-Wassers aus Schritt (c) wiederaufbereitat wird, und dass Schritt (a) eine Verdünnung des Zellstoffs mit dem wiederaufbereiteten Prozess-Wasser beinhaltet.

6. Verfahren gemäß einem der Ansprüche 1 bis 5, dadurch gekennzeichnet, dass das Enzym eine Oxidoreduktase, bevorzugt eine Laccase, ist.

7. Verfahren gemäß Anspruch 6, dadurch gekennzeichnet, dass die Laccase von Polyporus pinsitus stammt.

8. Verfahren nach Anspruch 6 oder 7, dadurch gekennzeichnet, dass die Oxidoreduktase in einer Menge von 10 bis 10.000 PODU pro Gramm Trockenmasse oder 0.001 bis 1000 LACU pro Gramm Trockenmasse vorliegt.

9. Verfahren nach einem der Ansprüche 1 bis 8, dadurch gekennzeichnet, dass die Enzym-Behändlung an einem Zellstoff durchgeführt wird, der eine Konsistenz von 0.5 bis 25%, einen pH-Wert von 4 bis 10 und eine Temperatur von 20 bis 90 °C aufweist.

10. Verfahren gemäß einem der Ansprüche 1 bis 9, dadurch gekennzeichnet, dass die Enzym-Behandlung bei Atmosphärendruck durchgeführt wird.

11. Verfahren nach einem der Ansprtiche 1 bis 10, dadurch gekennzeichnet, dass der Zellstoff ungebleichter oder halbgebleichter Sulfat-Zellstoff, neutraler halbchemischer Sulfit-Zellstoff oder wiederaufbereiteter Zellstoff von alten Wellpappe-Behältern ist.

12. Verfahren nach Anspruch 11, dadurch gekennzeichnet, dass der wiederaufbereitete Zellstoff von alten Wellpappe-Behältern ein ungebleichter Sulfat-Zellstoff ist.

13. Verfahren zur Herstellung von Wellpappe oder Wellpappe-Behältern, umfassend die Herstellung von Decklagen-Pappe und/oder Decklagen-Wellpappe durch das Verfahren gemäß Anspruch 1 und Zusammenführen der Decklagen-Pappe und der Decklagen-Wellpappe zur Herstellung der Wellpappe oder der Wellpappe-Behälter.

Revendications

1. Procédé pour produire des matériaux de type papier ayant une résistance à l'état humide améliorée, comprenant :

(a) la préparation d'une suspension de pâte chimique ou semi-chimique non blanchie ou semi-blanchie ou d'une pâte provenant de fibres recyclées ;

(b) le traitement de la pâte avec une enzyme oxydant les phénols et un médiateur ;

(c) la déshydratation de la pâte traitée dans une machine de fabrication du papier pour retirer l'eau de traitement et produire le matériau de type papier, et

(d) le séchage thermique du matériau de type papier.

2. Procédé selon la revendication 1 où le médiateur est l'acide 10-phénothiazine-propionique (PPT) ou le 2,2'-azino-bis(3-éthylbenzothiazoline-6-sulfonate (ABTS).

3. Procédé selon la revendication 2 où le chauffage est réalisé à une température supérieure à 100°C.

4. Procédé selon la revendication 3 où le chauffage est réalisé à une température supérieure à 150°C.

5. Procédé selon l'une quelconque des revendications 1-4 où au moins une partie de l'eau de traitement provenant de l'étape (c) est recyclée, et l'étape (a) comprend la dilution de la pâte avec l'eau de traitement recyclée.

6. Procédé selon l'une quelconque des revendications 1-5 où l'enzyme est une oxydoréductase, de préférence une laccase.

7. Procédé selon la revendication 6 où la laccase est dérivée de Polyporus pinsitus.

8. Procédé selon les revendications 6 ou 7 où l'oxydoréductase est présente en une quantité de 10-10000 PODU par gramme de matière sèche ou 0,001-1000 LACU par gramme de matière sèche.

9. Procédé selon l'une quelconque des revendications 1-8 où le traitement enzymatique est mis en oeuvre sur une pâte ayant une consistance de 0,5-25 %, un pH de 4-10 et une température de 20-90°C.

10. Procédé selon l'une quelconque des revendications 1-9 où le traitement enzymatique est mis en oeuvre à la pression atmosphérique.

11. Procédé selon l'une quelconque des revendications 1-10 où la pâte est de la pâte kraft non blanchie ou semi-blanchie, de la pâte semi-chimique au sulfite neutre ou de la pâte recyclée provenant de vieux récipients ondulés.

12. Procédé selon la revendication 11 où la pâte recyclée provenant de vieux récipients ondulés est une pâte kraft non blanchie.

13. Procédé pour produire du carton ondulé ou des récipients ondulés comprenant la production de carton de couverture et/ou de carton de couverture ondulé par le procédé selon la revendication 1 et la combinaison de carton de couverture et de carton de couverture ondulé pour produire le carton ou récipient ondulé.

Drawing