WO2012042116A1

WO2012042116A1 - Method for improving papermaking or board making process, use of a polysaccharide and paper

Info

Publication number: WO2012042116A1
Application number: PCT/FI2011/050843
Authority: WO
Inventors: Matti Hietaniemi; Kristian Salminen; Janne Kataja-Aho; Elias Retulainen
Original assignee: Kemira Oyj
Priority date: 2010-10-01
Filing date: 2011-09-30
Publication date: 2012-04-05
Also published as: CN103140626A; CA2813148C; EP2622131A1; EP2622132A1; ES2791997T3; EP2622131B1; PT2622132T; BR112013007876A2; CN103201426B; BR112013007244A2; FI125713B; BR112013007876B1; FI20106021L; CA2813148A1; ES2674881T3; FI20106021A; WO2012042115A1; CN103201426A; FI20106021A0; EP2622132B1

Abstract

The invention relates to a method for improving papermaking or board making process. The method comprises forming a fibre stock, and leading the fibre stock to a headbox and feeding it to a wire to form a wet fibrous web. A at least one polysaccharide having 1,4-β-anomeric configuration in linkages between saccharide units of the polysaccharide backbone or the main polysaccharide backbone is applied to the fibre stock after machine chest or on the wet fibrous web. The invention relates also to paper made by the method and to the use of polysaccharide.

Description

METHOD FOR IMPROVING PAPERMAKING OR BOARD MAKING PROCESS, USE OF A POLYSACCHARIDE AND PAPER

The present invention relates to a method for improving papermaking or board making process, use of a polysaccharide and a paper according to the preambles of the enclosed claims.

BACKGROUND OF THE INVENTION Economical production of paper and board requires a good runnability of a paper machine. The paper machine runnability is often evaluated by the number of web breaks in proportion to production speed. To attain good runnability, the paper must run well with a low number of web breaks in each sub-process along the entire paper machine line. For example, the fluttering of the paper web in the drying section should be minimised in order to avoid the possible web breaks. In order to avoid fluttering and web breaks, the paper web should preferably have a good tensile strength and good residual tension after strain.

Strength of wet paper web is one of the important factors in making of paper or board. Machines producing paper grades whose strength before drying is a critical factor may have high efficiency but their average production speed may be significantly lower than their nominal speed. The speed of these paper machines could be raised if the strength of the wet paper web could be increased. Common dry strength agents do not improve strength of the wet paper web. One example of such dry strength agents is starch, which has a 1 ,4-a-anomeric structure. Typical starches include amylose, which is a linear 1 ,4-a-glucan polymer and amylopectin, which has branched structure. The amylopectin backbone is 1 ,4- a-glucan polymer and the branches are linked to the backbone with 1 ,6-a- glycosidic bonds.

Fillers, such as clay, calcium carbonate, calcium sulphate or talc are used in paper and board making to reduce costs and to improve optical properties of paper or board. Fillers are added to the stock before the headbox of the paper machine. For coated paper grades coating pigments, which comprise the same minerals, may partly enter to the paper via the broke, which is recycled back to paper making process. The content of fillers and coating pigments is typically measured through ash content measurement by burning the stock or paper sample in 525 °C. The base paper for uncoated fine paper and for coated fine paper is made from softwood and hardwood and its ash content is typically 18 - 24 %. The base paper for 100 % softwood based uncoated fine paper and for coated fine paper has an ash content typically 10 - 17 %. An important limiting factor preventing the increase of filler content in fine papers is the reduced strength properties of the paper and reduced web runnability.

An object of this invention is to minimise or even eliminate the disadvantages existing in the prior art.

An object of the present invention is to provide an effective and simple method for improving tensile strength of a paper web or the like.

An object of the present invention is to increase filler content of paper in order to reduce papermaking costs.

These objects are attained with the present invention having the characteristics presented below in the characterising parts of the independent claims. Typical method according to the present invention for improving papermaking or board making process comprises

- forming a fibre stock,

- leading the fibre stock to a headbox and feeding it to a wire to form a wet fibrous web, and

- applying at least one polysaccharide having 1 ,4- -anomeric configuration in linkages between saccharide units of the polysaccharide backbone or the main polysaccharide backbone to the fibre stock after machine chest or on the wet fibrous web. Typical paper according to the present invention is produced by using the method according to the invention. Typical use according to the present invention of a polysaccharide which has 1 ,4- β-anomeric configuration in linkages between saccharide units of the polysaccharide backbone or the main polysaccharide backbone is for increasing filler content of the paper or board, for reducing basis weight, and/or improving runnability of a wet paper or board web.

Now it has been surprisingly found out that the tensile strength of the wet paper or board is clearly improved when a polysaccharide having 1 ,4- -anomeric configuration in the linkages between saccharide units is brought into a contact with fibres in the stock or with fibres in a wet paper web. The improved tensile strength of the wet web, as well as the improved dry tensile strength of the paper that may be achieved with the present invention enables an increase in the filler content of paper. When the residual tension after strain is improved by the use of the present invention, a high filler content in the base paper may be used, corresponding to ash content e.g. over 25 % both for uncoated fine paper and for coated fine paper base paper made from softwood and hardwood mixture. Correspondingly, a high filler content in the base paper may be used for 100 % softwood based uncoated fine paper and for coated fine paper base paper, the high filler content corresponding to an ash content over 18 %. An improvement in tensile strength may enable an ash content increase also for other paper and board grades, such as ash content increase to over 15 % for newsprint grades, or ash content increase over 12 % coated mechanical base paper, or ash content increase over 34 % for SC paper. Improvement in tensile strength also may be utilised by changing to a cheaper raw material mixture for the stock. For example, less old corrugated container (OCC) and more collected paper from households to make test liner or fluting board grade. The ash content of recycled fibre based fluting or test liner board may be increased over 1 5%. Fillers, which are used in making or paper or board, which are suitable for use in the present invention, and the content of which may be increased, are preferably clay, calcium carbonate, calcium sulphate, titanium dioxide or talc, or their mixtures. Often the used filler has an anionic net charge.

According to one embodiment of the invention the polysaccharide having 1 ,4-β- anomeric configuration in the linkages between saccharide units of the polysaccharide backbone or the main polysaccharide backbone is selected from the group comprising water soluble cellulose derivatives; galactomannans, such as guar gum or locust bean gum; galactoglucomannans; carboxymethyl cellulose; xylan and substituted glucans, such as xyloglucans; other suitable hydrocolloids, such as tamarind gum; chitosan; chitin; or their derivatives. According to one preferred embodiment the polysaccharide having 1 ,4- -anomeric configuration in the linkages between saccharide units is selected from the group comprising water soluble cellulose derivatives; galactomannans, such as guar gum or locust bean gum; galactoglucomannans; carboxymethyl cellulose; xylan and substituted glucans, such as xyloglucans; other suitable hydrocolloids, such as tamarind gum; or their derivatives. According to another preferred embodiment the polysaccharide, which has 1 ,4- -anomeric configuration in the linkages between saccharide units of the polysaccharide backbone or the main polysaccharide backbone, is guar gum. In this context guar gum is understood as a carbohydrate polymer containing galactose and mannose structural building blocks, especially containing one galactose unit for every two mannose units. The backbone is a linear chain of β 1 ,4-linked mannose residues to which galactose residues are 1 ,6- linked at every second mannose, forming short side-branches. Guar gum is typically obtained as an extract of guar bean. It may be used in native form or it may be used in cationised or anionised form.

According to one embodiment of the present invention, anionised guar gum is applied to the fibre stock or on the wet fibre web after application of cationic strength agent to the fibre stock and/or on the wet fibre web. The cationic strength agent may be cationic or amphoteric polyacrylamide, polyvinylamide, polyamidoamine, epichlorohydrin, starch, cationic guar gum or derivative of these. For example, cationic wet strength agent may be applied on the wet fibre web by spraying, after which anionised guar gum is applied by spraying. More typically, cationic wet strength agent is applied into the fibre stock, after which anionised guar gum is applied by spraying on the wet fibre web. Anionised guar gum has typically a charge density < 2 meq/g.

According to another embodiment of the invention the polysaccharide having 1 ,4- β-anomeric configuration in the linkages between saccharide units of the polysaccharide backbone or the main polysaccharide backbone is carboxymethyl cellulose, CMC. Carboxymethyl cellulose is understood here as an anionic polymer, which is produced by introducing carboxyl methyl groups to the cellulose chain, the degree of substitution and the chain length of the cellulose backbone affecting the properties of CMC, such as water solubility. When the degree of substitution exceeds 0.3, carboxymethyl cellulose becomes water soluble.

According to another embodiment of the invention the polysaccharide having 1 ,4- β-anomeric configuration in the linkages between saccharide units of the polysaccharide backbone or the main polysaccharide backbone is a polysaccharide with high degree of polymerisation (DP). This means polysaccharides which comprise > 500 anhydroglucose units. Size exclusion chromatography, SEC, may be used for determination of the polymerisation degree. It has been observed that the tensile strength of the wet paper or board is further improved when these polysaccharides are used. Polysaccharide having 1 ,4- -anomeric configuration in the linkages between saccharide units of the polysaccharide backbone or the main polysaccharide backbone and used in the present invention is water soluble. In case a derivative of the polysaccharide is used, the derivative is also water soluble. The viscosity (Brookfield) of the polysaccharide solution is < 5000 mPas, preferably < 2000 mPas. Solution may be diluted in order to achieve the desired concentration.

The polysaccharide having 1 ,4- -anomeric configuration in the linkages between saccharide units is applied as a solution to the wet fibre web in any suitable manner. Preferably the solution is obtained by dissolving the polysaccharide in powder form into a solvent, typically water. Preferably the polysaccharide solution is free from discrete polysaccharide particles. The polysaccharide solution may comprise one polysaccharide or it may comprise a mixture of different polysaccharides, for example a mixture of two or three polysaccharides. Thus, according to one embodiment a mixture of different polysaccharides may be applied to the fibre stock after machine chest or on the wet fibrous web. Typically the concentration of the polysaccharide(s) in the polysaccharide solution is < 60 weight-%, more typically 0.02 - 5 weight-%, preferably 0.05 - 3 weight-%, more preferably 0.05 - 2 weight-%. Concentration of polysaccharides with high degree of polymerisation (DP) in the solution may be even < 1 weight-%, more typically 0.05 - 1 weight-%, even more typically 0.2 - 0.6 weight-%.

According to one embodiment of the invention the polysaccharide is applied to the fibre stock between the last pump preceding the paper or board machine headbox and the outlet of the paper or board machine headbox. Preferably, the polysaccharide is added to the stock as near the headbox as possible, or the polysaccharide may be added directly to the headbox, if adequate mixing to the stock can be secured. Addition of the polysaccharide near the headbox improves the bonding of the fibres together with the polysaccharide, as the polysaccharide remains in outstretched form due to short residence time in the stock and the adsorption of the polysaccharide over the fibre surface is reduced. Also, when the polysaccharide is added to the stock after the last pump, the risk for breaking the flocks generated by the polysaccharide and fragmentation of the polysaccharide backbone due to shear forces is minimised. Thus, the activity of the polysaccharide remains in a high level, and it dosage may be reduced or better tensile strength values may be obtained by using the same dosage.

According to one embodiment of the invention the polysaccharide is applied into the fibre stock together with a retention or drainage agent. The polysaccharide and the retention agent are added to the fibre stock typically near the headbox, for example by dosing at the machine filter. The retention or drainage agent may be any suitable retention agent. The retention agent may be selected from a group comprising anionic or cationic polyacrylamide, polyvinylamine, polyethyleneimine, cationic starch, bentonite or silica. Especially the retention agent may be anionic or cationic polyacrylamide, polyvinylamine or polyethyleneimine. The retention agent and the polysaccharide may be added as separate solutions, or they may be added as single solution, comprising both the retention agent and the polysaccharide. Polymeric retention agent dosage may be 50 - 1000 g/t, preferably 100 - 600 g/t, given as dry polymer, and the polysaccharide dosage may preferably be 200 - 4000 g/t, preferably 500 - 2500 g/t, given as dry polymer. According to another embodiment of the invention the polysaccharide is applied into the fibre stock together with an anionic, cationic or amphoteric dry strength agent. The dry strength agent is selected from the group comprising polyacrylamides, glyoxylated polyacrylamides, polyvinylamines, polyamine epichlorohydrine co-polymers (PAAE), starch derivatives, and carboxymethyl cellulose. The dry strength agent may be applied in amount of 0.1 - 4 kg/t paper, typically in amount 0.2 - 2 kg/t, given as active substance.

According to one preferred embodiment of the invention the polysaccharide is applied on the wet fibre web between the headbox and the last nip of a press section. According to one preferred embodiment of the invention the polysaccharide is applied on the wet fibre web by spraying, by coating, by film transfer or by foam layer application. It may be applied by using film transfer to a press belt, or by feeding of polysaccharide solution from a separate headbox. Preferably the application of the polysaccharide solution is performed by spraying. It has been found out that the spraying of the polysaccharide solution onto the fibre web provides many surprising advantages. Spraying of the polysaccharide solution does not influence the formation of the paper web, whereby there is no negative effects to be noticed in the final paper properties. On the other hand, it has also been noticed that the retention of the polysaccharide to the web is improved. This means that the used amount of the polysaccharide can be kept low, and chemical losses may be minimised. It has been observed that when the polysaccharide solution is added by spraying, the polysaccharide is evenly distributed through the whole web. No significant difference in amount of the polysaccharide can be observed between the surfaces and the core part of the web.

Preferably, the polysaccharide is applied by spraying onto the wet paper web. It has been observed that the polysaccharide amount, which is applied, may be reduced when the application is done by spraying, and still the improved tensile strength characteristics of the paper web are obtained. A polysaccharide solution suitable for use in the spraying may be obtained, for example, by dissolving a polysaccharide in powder form into water in order to form a 0.2 - 20 weight-%, preferably 0.3 - 3 weight-% solution.

According to still another embodiment, the polysaccharide is applied by foam layer application or foam coating. The polysaccharide may be applied by foam coating, whereby the polysaccharide is applied as a foam, which has an air content of 60 - 95 %, onto the wet paper web.

Irrespective of the method of application of the polysaccharide, the polysaccharide is applied in amount < 0.1 - 10 kg/(ton paper), preferably 0.3 - 3 kg/(ton paper). When the polysaccharide is applied by spraying, it may be applied in amount < 2 g/m², typically 0.05 - 1 .5 g/m², more typically < 1 g/m², most typically 0.05 - 1 g/m², preferably 0.05 - 0.5 g/m², more preferably 0.05 - 0.3 g/m² on the wet paper web.

According to one embodiment of the invention the polysaccharide solution is applied on the wet paper web when the dryness of the web is < 50 %, typically < 40 %, more typically < 30 %, preferably 8 - 15 %. When the pulp suspension enters the headbox and thus the paper machine, its dryness level is typically more or equal to 0.3 % and less than 2 %. The first water removal from the web is driven by gravity when the web enters the wire section from the headbox. As paper travels further in the wire section, water removal is assisted by different vacuum units. After the wire section, the dryness of the paper is typically 14 - 22 %. The dryness of paper increases to 40 - 55 % during wet pressing. The applying of the polysaccharide solution is preferably conducted before the last vacuum zone of the wire section, preferably by spraying.

According to one embodiment of the invention two or more polysaccharides may be applied on the wet fibre web after each other by spraying. Thus layers of different polysaccharides may easily be applied on top of each other in order to obtain desired properties.

According to one embodiment an anionic or cationic polymer solution may be applied to the wet paper web before or after the addition of the polysaccharide. The application of the anionic polymer is performed to the wet paper web before press section of a paper machine. For example, the application of the polysaccharide to the wet paper web may be preceded or followed by application of cationic or anionic polymer solution. This kind of sequential application of polysaccharide and one or more polymers to the wet paper web, preferably through spraying, may produce a marked improvement of dry and wet paper web strength. Anionic and cationic polymer solutions may also be pre-mixed together before their application, preferably by spraying, to the wet paper web. The present invention is advantageous for improving strength of the wet paper web when producing wood-free uncoated and coated paper grades. The present invention is also suitable for improving runnability of a wet paper or board web by improving strength of the wet paper web when producing paper grades including wood-free uncoated paper, wood-free coated paper, super calendered (SC) paper, ultralight weight coated (ULWC) paper, light weight coated (LWC) paper or newsprint paper, but not limited to these. Especially paper webs that are to be used for making recording substrates for the inkjet printing are suitable to be treated according to the method of the present invention. The paper web may comprise fibres from hardwood trees or softwood trees or a combination of both fibres. The fibres may be obtained by any suitable pulping or refining technique normally employed in paper making, such as thermomechanical pulping (TMP), chemimechanical (CMP), chemithermomechanical pulping (CTMP), groundwood pulping, alkaline sulphate (kraft) pulping, acid sulphite pulping, and semichemical pulping. The paper web may comprise only virgin fibres or recycled fibres or a combination of both. The weight of the final paper web is 30 - 800 g/m², typically 30 - 600 g/m², more typically 50 - 500 g/m², preferably 60 - 300 g/m², more preferably 60 - 120 g/m², even more preferably 70 - 100 g/m².

In some embodiments the paper web may comprise fibres originating from non- wood material, such as bamboo, sugar cane bagasse, hemp, wheat or rice straw.

According to one embodiment of the invention the filler content of the paper or board is increased, whereby the ash content in the wet paper or board web is >25 % for wood-free uncoated paper, >25 % for wood-free coated paper base paper, >34 % for super calendered (SC) paper, >13 % for coated mechanical base paper, >15 % for newsprint paper, fluting board or testliner board, the ash content being measured by burning the stock sample completely in 525 °C.

One or more layers of chemical solutions may be applied to the wet paper web before the press section or drying section. The addition of a cationic polymer to the stock of fibres is not compulsory, but it may be performed. The chemical solutions are preferably applied to the wet paper web by spraying, as described in the application, but they may be applied by coating, film transfer, foam layer application or feeding from a separate headbox. The chemical solution that is applied to the web, e.g. by spraying, may be a solution of carboxymethyl cellulose (CMC), polyvinyl alcohol (PVA), chitosan or guar gum. Guar gum is here understood as a galactomannan. It is a polysaccharide comprising galactose and mannose. The backbone of the guar gum is a linear chain of β 1 ,4-linked mannose residues to which galactose residues are 1 ,6-linked at every second mannose, forming short side-branches. Guar gum may be applied to the web in form of native guar gum, anionic guar gum or cationic guar gum. For example, native, cationic or anionic guar gum may be applied to the wet paper web, which is formed without using addition of a cationic polymer to the stock. In another example, native or anionic guar gum may be applied to the wet paper web, which is formed from stock into which cationic polymer, such as cationic guar gum, is added. EXPERIMENTAL Example 1

Elementary Chlorine Free-bleached pine pulp was obtained from a Finnish pulp mill. The pulp was refined and dewatered at the mill. The pulp was packed as never-dried into airtight polyethylene bags, and kept at -18°C until used for testing. The Schopper-Riegler (SR) value of the pulp after dewatering and freezing was 20, measured according to ISO 5267-1 . Native dissolved guar gum (Sigma G4129), carboxymethyl cellulose (DS 0.7, DP 140) and chitosan (Mw 400,000 g/mol) was added to the thick stock pulp 30 - 90 min before sheet preparation as a 0.5 weight-% solution.

Wet and dry handsheets were prepared according to SCAN-C 26:76 standard. Grammage of handsheets was 60 g/m². After wet pressing the handsheets were stored at cold storage room in airproof packages before measurements in order to maintain constant moisture in the sheets.

For the spraying of chemicals at laboratory, formed wet handsheets were placed onto the wire and attached using vacuum. Vacuum usage enhanced also the penetration of chemicals into the paper during spraying. The experimental unit comprised a vacuum box, moving sample sledge with wire, and spraying unit. The amount of the chemical sprayed was adjusted by the speed of the moving sample sledge, while the spray remained constant and was immobilized. The samples were wet pressed with 350 kPa and 50 kPa for 5+2 minutes after spraying. The higher pressure gives higher dryness for test sheet. Chemical consistency during spray tests was 0.5%.

Measurements

Tensile strength was measured according to ISO 1924-2:2008. The dryness of the paper samples was determined by using a Mettler Toledo HR73 infra-red dryer. Results

Figure 1 shows results of laboratory tests (Example 1 ) for guar gum, which was added to thick stock pulp or sprayed on wet web. It can be seen that it is advantageous to add guar gum for wet web strength later at paper machine process rather than to thick stock pulp.

Figure 2 shows results for laboratory tests (Example 1 ) for CMC, chitosan and guar gum, each of which was sprayed on wet web. The effect of different polysaccharides on wet web strength can be seen. Guar gum is most effective. Chitosan and carboxymethyl cellulose (CMC) improved also wet web strength. As reference were used a spraying of water or handsheet without any spraying.

Example 2

Pulp containing 70% hardwood with SR-value 24 and 30 % softwood with SR- value 28 was acquired from a Finnish pulp mill. SR-value was measured according to ISO 5267-1 . Precipitated calcium carbonate was used as filler. Filler was added to the pulp and target level for addition was 20 % filler content in the final web.

Retention chemical was Fennopol K3400R (Kemira Oyj) with dosage 200 g/t and it was added to the headbox feed flow. Tests were made with a small fourdrinier type of wire section. Grammage of formed web was 70 g/m². Chemicals were sprayed on the wet web at the wire. The samples were wet pressed with 350 kPa and 50 kPa for 5+2 minutes after spraying.

Measurements

Tensile strength was measured according to ISO 1924-2:2008. The dryness of the paper samples was determined by using a Mettler Toledo HR73 infra-red dryer.

Results

Figure 3 shows results for tensile strength in semipilot test (Example 2) for sprayed guar gum and Figure 4 shows tensile energy adsorption in semipilot test (Example 2) for sprayed guar gum. The effect of guar gum wet web spraying dosage levels on wet web strength can be observed in the Figures. Spraying dosages were 0.1 g/m² (1 .4 kg/t), 0.3 g/m² (4.2 kg/t) and 0.5 g/m² (7.1 kg/t). Dosages of 0.1 g/m² and 0.3 g/m² improved both wet web tensile and solids content after wet pressing. Dosage of 0.5 g/m² improves strength further, but solids content in wet pressing is reduced. Therefore optimum dosage may be between 0.1 g/m² and 0.5 g/m², at least under these experimental conditions. Tensile strength is needed for web to keep enough tension at paper machine dryer section to allow high operation speed. If the tension of the web is not high enough, the sheet does not follow dryer fabric and sheet fluttering may cause web break due to wind effect caused by high speed. Tensile energy adsorption T.E.A. improvement helps to avoid web break, if web has fault such as a hole, slime spot, sticky particle or locally lower basis weight, because higher strength reduces risk that web tears apart beging from the fault position.

Example 3

Test furnish was a mixture of softwood and hardwood kraft pulp for fine paper, containing 40 weigth-% scalenohedric precipitated calcium carbonate (PCC) filler. In some tests additional PCC was applied. Chemicals were added to furnish under stirring with magnetic stirrer before sheet preparation. Dosing time of cationic polyacrylamide (C-PAM) retention aid and guar gum was typical for paper machine retention system, see Table 1 . Guar gum and C-PAM were premixed as powder in proportion 1 :1 , and then dissolved to 0.5 weight-% concentration with water, giving a final concentration of 0.25 weight-% guar gum and 0.25 weight-% C-PAM.

Chemicals used in the tests were: cationic potato starch (DS 0.035), guar gum (Sigma G4129) and cationic polyacrylamide, C-PAM, Fennopol K 3400 R (Kemira Oyj). All were dissolved to 0.5 weight-% solution except starch was cooked to 1 weight-% solution.

Handsheets were prepared with Rapid Kotchen semi-automatic sheet former to 80 g/m2 basis weight according to ISO 5269-2:2004. Ash content was measured according to ISO 1762:2001 .

Wet web sheets were wet pressed according to ISO 5269-1 :2005, but pressing time was 1 min at 2 bar pressure between 2 plotters on top and 2 plotters under. In tests D and E the wet pressing was 2 min at 4 bar pressure. Wet web tensile measurements were performed at the dry content after wet pressing.

Dry tensile handsheets were vacuum dried according to Rapid-Kotchen method. Tensile indexes were measured according to ISO 1924-2:2008. The results can be seen in the Table 1 .

Table 1 . The wet web tensile index and dry tensile index result for different handsheets.

From the results it can be seen that the wet web tensile index was improved in test B compared to test A; also ash content increased, which reduced the dry tensile index. In test C significantly higher ash content was achieved with guar gum and C-PAM blend with similar wet web tensile compared to test A. In test E cationic starch was used as strength agent in high filler containing pulp. Starch decreased wet web strength compared to test D.

Even if the invention was described with reference to what at present seems to be the most practical and preferred embodiments, it is appreciated that the invention shall not be limited to the embodiments described above, but the invention is intended to cover also different modifications and equivalent technical solutions within the scope of the enclosed claims.

Claims

1 . Method for improving papermaking or board making process, comprising

- forming a fibre stock,

- leading the fibre stock to a headbox and feeding it to a wire to form a wet fibrous web,

characterised in

applying at least one polysaccharide having 1 ,4- -anomeric configuration in linkages between saccharide units of the polysaccharide backbone or the main polysaccharide backbone to the fibre stock after machine chest or on the wet fibrous web.

2. Method according to claim 1 , characterised in selecting the polysaccharide from a group comprising water soluble cellulose derivatives; galactomannans, such as guar gum or locust bean gum; galactoglucomannans; carboxymethyl cellulose; xylan and substituted glucans, such as xyloglucans; other suitable hydrocolloids, such as tamarind gum; chitosan; chitin; or their derivatives.

3. Method according to claim 1 or 2, characterised in applying the polysaccharide as a solution.

4. Method according to claim 1 or 2, characterised in that the concentration of the polysaccharide in the polysaccharide solution is < 60 weight-%, more typically 0.02

- 5 weight-%, preferably 0.05 - 3 weight-%, more preferably 0.05 - 2 weight-%.

5. Method according to any of preceding claims 1 - 4, characterised in applying a mixture of different polysaccharides to the fibre stock after machine chest or on the wet fibrous web.

6. Method according to claim 1 , characterised in that the at least one polysaccharide having 1 ,4- -anomeric configuration in linkages between saccharide units of the polysaccharide backbone or the main polysaccharide backbone is guar gum.

7. Method according to claim 1 , characterised in that the at least one polysaccharide having 1 ,4- -anomeric configuration in the linkages between saccharide units of the polysaccharide backbone or the main polysaccharide backbone is a polysaccharide with high degree of polymerisation (DP).

8. Method according to claim 1 , characterised in applying the polysaccharide in amount < 0.1 - 10 kg/(ton paper), preferably 0.3 - 3 kg/(ton paper).

9. Method according to any of preceding claims, characterised in applying the polysaccharide to the fibre stock between the last pump preceding the paper machine headbox and the outlet of the paper machine headbox.

10. Method according to claim 9, characterised in applying the polysaccharide into the fibre stock together with a retention or drainage agent.

11 . Method according to claim 10, characterised in selecting the retention agent from a group comprising anionic or cationic polyacrylamide, polyvinylamine, polyethyleneimine, cationic starch, bentonite or silica, especially from anionic or cationic polyacrylamide, polyvinylamine or polyethyleneimine.

12. Method according to claim 10 or 11 , characterised in adding the polysaccharide and the retention agent as single solution.

13. Method according to any of claims 1 - 8, characterised in applying the polysaccharide on the wet fibre web between the headbox and the last nip of the press section.

14. Method according to claim 13, characterised in applying the polysaccharide on the fibre web by spraying, by coating, by film transfer or by foam layer application.

15. Method according to claim 14, characterised in applying the polysaccharide by spraying as a solution with a concentration in the range of 0.2 - 20 weight-%, preferably 0.3 - 3 weight-%.

16. Method according to claim 14 or 15, characterised in applying the polysaccharide by spraying in amount < 2 g/m², most typically 0.05 - 1 .5 g/m², preferably 0.05 - 0.5 g/m², on the wet paper web.

17. Method according to claim 14, characterised in applying the polysaccharide by foam coating, whereby the polysaccharide is applied as a foam having an air content of 60 - 95 %.

18. Method according to any of claims 14 - 17, characterised in applying the polysaccharide solution on the wet paper web when the dryness of the web is < 50 %, preferably 8 - 15 %.

19. Paper or board produced by using method according to any of claims 1 to 18.

20. Use of a polysaccharide which has 1 ,4- -anomeric configuration in linkages between saccharide units of the polysaccharide backbone or the main polysaccharide backbone for increasing filler content of the paper or board, for reducing basis weight, and/or improving runnability of a wet paper or board web.

21 . Use according to claim 20, characterised in that the filler, content of which is increased, is clay, calcium carbonate, calcium sulphate, titanium dioxide or talc, or their mixtures.

22. Use according to claim 20, characterised in improving runnability of a wet paper or board web by improving strength of the wet paper or board web when producing wood-free uncoated paper, wood-free coated paper, super calendered (SC) paper, ultralight weight coated (ULWC) paper, light weight coated (LWC) paper or newsprint paper.

23. Use according to claim 20, characterised in increasing filler content of the paper or board, whereby the ash content in the wet paper or board web is

- >25 % for wood-free uncoated paper,

- >25 % for wood-free coated paper base paper,

- >34 % for super calendered (SC) paper,

- >13 % for coated mechanical base paper,

- >15 % for newsprint paper, fluting board or testliner board,

the ash content being measured by burning the stock sample in 525 °C