Manufacturing method for a film or product comprising an amphiphilic polymer

10358772 ยท 2019-07-23

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Inventors

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Abstract

A method for manufacturing of a film, wherein said film is manufactured in a paper or paper board machine, wherein the method comprises the steps of providing a solution of a nanofibrillated poly-saccharide, wherein said solution comprises from 0.01 to 50 weight-% nanofibrillated polysaccharide, and wherein the nanofibrillated polysaccharide is any one of microfibrillated cellulose, nanofibrillated cellulose, nanocrystalline cellulose, microcrystalline cellulose, cellulose whiskers and cellulose derivative or a combination or mixture thereof, wherein the method further comprises the steps of providing an amphiphilic polymer; and providing a mixture of said amphiphilic polymer and said solution comprising nanofibrillated polysaccharide, whereby an intermediate solution is obtained; bringing said intermediate solution into a foam; providing said foam in the paper or board machine.

Claims

1. A method for manufacturing of a film, wherein said film is manufactured in a paper or paper board machine, wherein the method comprises the steps of providing a solution of a nanofibrillated polysaccharide, wherein said solution comprises from 0.01 to 50 weight-% nanofibrillated polysaccharide, and wherein the nanofibrillated polysaccharide is any one of microfibrillated cellulose, nanofibrillated cellulose, cellulose whiskers and cellulose derivative or a combination or mixture thereof, wherein the method further comprises the steps of providing an amphiphilic polymer; providing a mixture of said amphiphilic polymer and said solution comprising nanofibrillated polysaccharide, whereby an intermediate solution is obtained; bringing said intermediate solution into a foam; and providing said foam in the paper or board machine.

2. The method as claimed in claim 1, wherein the method further comprises the steps of: supplying the foam to a forming fabric, for forming a foam web; dewatering the foam web on the forming fabric; subjecting the foam web to drying to form a paper or paper board product.

3. The method as claimed in claim 1, wherein the method further comprises the step of applying said foam as a coating in said paper or board making machine.

4. The method as claimed in claim 1, wherein the amphiphilic polymer is selected from any one of a octenyl succinic anhydride (OSA) starch, dodecyl succinic anhydride (DDSA) starch, hydrophobic modified ethylhydroxyethyl cellulose (HM-EHEC), hydrophobic modified hydroxyethyl cellulose (HM-HEC), hydrophobic modified carboxy methyl cellulose (HM-CMC), hydrophobic modified starch (HM-starch), hydrophobic modified nanocrystalline cellulose, hydrophobically modified polyvinyl alcohol, or a combination or mixture thereof.

5. The method as claimed in claim 4, wherein the surface active polymer is octenyl succinic anhydride (OSA) starch.

6. The method as claimed in claim 5, wherein the OSA starch is provided in an amount of 1 to 10 weight-% based on the amount of fibers in the solution of nanofibrillated polysaccharide.

7. The method as claimed in claim 1, wherein the method further comprises the step of cooking the amphiphilic polymer in the presence of said microfibrillated polysaccharide.

8. The method as claimed in claim 1, wherein the method further comprises the step of forming said nanofibrillated polysaccharide in the presence of said amphiphilic polymer.

9. The method as claimed in claim 1, wherein the method comprises providing said foam as an additive to a wet end said paper or board making machine.

10. A paper or paper board product obtained by the method comprising the steps of, providing a solution of a nanofibrillated polysaccharide, wherein said solution comprises from 0.01 to 50 weight-% nanofibrillated polysaccharide, and wherein the nanofibrillated polysaccharide is any one of microfibrillated cellulose, nanofibrillated cellulose, cellulose whiskers and cellulose derivative or a combination or mixture thereof; providing an amphiphilic polymer; providing a mixture of said amphiphilic polymer and said solution comprising nanofibrillated polysaccharide, whereby an intermediate solution is obtained; bringing said intermediate solution into a foam; and providing said foam in the paper or board machine.

11. The paper or paper board product as claimed in claim 10, wherein said product is a barrier film or barrier coating having an oxygen transmission rate (OTR) of less than 20 cm3/m2/d measured at 50% relative humidity.

12. The paper or paper board product as claimed in claim 11, wherein the product is a base paper and wherein the base paper has a basis weight or in the range of from 10 to 100 g/m2.

13. The paper or paper board product as claimed in claim 11, wherein the product is a base paper and wherein the base paper has a basis weight or in the range of from 10 to 40 g/m2.

14. The paper or paper board product as claimed in claim 11, wherein the product is a base paper and wherein the base paper has a basis weight or in the range of from 10 to 30 g/m2.

15. The paper or paper board product as claimed in claim 11, wherein the product is a base paper and wherein the base paper has a basis weight or in the range of from 10 to 25 g/m2.

16. The paper or paper board product as claimed in claim 10, wherein said product is a barrier film or barrier coating having an oxygen transmission rate (OTR) of less than 15 cm3/m2/d measured at 50% relative humidity.

17. The paper or paper board product as claimed in claim 10, wherein said product is a barrier film or barrier coating having an oxygen transmission rate (OTR) of less than 10 cm3/m2/d measured at 50% relative humidity.

18. The paper or paper board product as claimed in claim 10, wherein said product is a barrier film or barrier coating having an oxygen transmission rate (OTR) of less than 5 cm3/m2/d measured at 50% relative humidity.

Description

DESCRIPTION OF EMBODIMENTS

(1) This invention relates to a manufacturing method, applicable in a conventional paper making or paperboard making machine or process, known to the skilled person.

(2) According to one embodiment a solution of a nanofibrillated polysaccharide is provided.

(3) The solution comprises the nanofibrillated polysaccharide in a range of from, 0.01 to 50 weight-%, or from 0.1 to 15 weight-%, or from 0.1 to 2.5 weight-%.

(4) The nanofibrillated polysaccharide may be any one of microfibrillated cellulose (MFC), nanofibrillated cellulose, cellulose whiskers and cellulose derivative or a combination or mixture thereof.

(5) The definition of nanofibrillated polysaccharide includes bacterial cellulose or nanocellulose spun with either traditional spinning techniques or with electrostatic spinning. In these cases, the material is preferably a polysaccharide but not limited to solely a polysaccharide. A polysaccharide can be e.g. starch, protein, cellulose derivatives, etc. Also microfibrillated cellulose as defined more in detail below is included in this definition. The microfibrillated cellulose (MFC) is also known as nanocellulose. It is a material typically made from wood cellulose fibers, both from hardwood or softwood fibers. It can also be made from microbial sources, agricultural fibers such as wheat straw pulp, bamboo or other non-wood fiber sources. In microfibrillated cellulose the individual microfibrils have been partly or totally detached from each other. A microfibrillated cellulose fibril is normally very thin (20 nm) and the length is often between 100 nm to 10 m. However, the microfibrils may also be longer, for example between 10-200 m, but lengths even 2000 m can be found due to wide length distribution. Fibers that has been fibrillated and which have microfibrils on the surface and microfibrils that are separated and located in a water phase of a slurry are included in the definition MFC. Furthermore, cellulose whiskers may also be included in the definition MFC. The fibrils may also be polymer coated fibrils, i.e. a modified fibril either chemically or physically.

(6) The method according to the present invention further comprises providing a amphiphilic polymer, and then mixing the said amphiphilic polymer with the solution comprising the nanofibrillated polysaccharide. This means that a second solution comprising the nanofibrillated polysaccharide, in the amounts as stated above, the amphiphilic polymer and the remaining part water is formed. The amount of the amphiphilic polymer is chosen such that the solution comprises the nanofibrillated polysaccharide, the amphiphilic polymer, other possible additives and water up to 100%. According to one embodiment the solution of amphiphilic polymer comprises 1-100% amphiphilic polymer (w/w), more preferably 1-50%, and most preferably 1-10%.

(7) According to one embodiment the amount of amphiphilic polymer may be in the range of from 1 to 10%, based on the amount of nanofibrillated polysaccharide, or based the amount of fibers, in a stock solution. By amphiphilic polymer is meant a polymer which has both hydrophilic and hydrophobic (or lipophilic) groups. The terms amphiphilic polymer and surface active polymer are both used in the present description.

(8) The amphiphilic polymer or surface active polymer may be a so called hydrophobic surface active polymer. Among those surface active polymers useful for the present invention are for instance, ethyl hydroxyethyl cellulose (EHEC), hydrophobic modified (HM) ethylhydroxyethyl cellulose (HM-EHEC), hydroxyethyl cellulose (HEC), hydrophobic modified hydroxyethyl cellulose, HM-HEC, hydroxyproylated cellulose (HPC), hydrophobic modified carboxymethyl cellulose (HM-CMC), HM-starch, hydroxypropylated starch and so on. The amphiphilic polymer may also be any one of a octenyl succinic anhydride (OSA) starch, dodecyl succinic anhydride (DDSA) starch, carboxymethyl cellulose (CMC) having hydrophobic properties. According to one embodiment the amphiphilic polymer is an hydrophobically modified polyvinyl alcohol (PVOH), such as ethylene modified PVOH. According to yet another embodiment, the surface active polymer may be a polyvinyl alcohol containing >2% acetate groups, or more preferably more than 10% acetate groups, even more preferably >15% acetate groups.

(9) The amphiphilic polymer may also be a charged amphiphilic polymer. The charge may facilitate the retention.

(10) The amphiphilic polymer or surface active polymer may also be a mixture of different amphiphilic polymers or surface active polymers or derivatives of the above mentioned amphiphilic polymers or surface active polymers.

(11) According to one embodiment the amount of OSA starch may be in the range of from 1 to 10%, based on the amount of nanofibrillated polysaccharide, or based the amount of fibers, in a stock solution.

(12) The amphiphilic polymer may have a specific cloud temperature. The process temperature, including the drying may be performed at this specific cloud temperature, thus activating the polymer. Amphiphilic polymers may be activated either by a specific pH, temperature or additive. By regulating the temperature accordingly it may thus be possible to control, i.e. induce or collapse for instance foam formed by the mixture.

(13) According to one preferred embodiment the amphiphilic polymer is OSA starch or n-OSA starch.

(14) Through this mixture an intermediate product or solution is obtained which can then further be used in the paper or paperboard manufacturing process.

(15) According to one embodiment the intermediate solution can be brought into foam. This can be done by any conventional means, such as mechanically, i.e. agitation, or chemically, by adding foam forming chemicals. It can also be done by adding for instance macro-, micro- or nano-bubbles of gas into the intermediate solution.

(16) The foam may then subsequently be used in different manner in the paper making or board making process. According to one embodiment the foam may be used in a foam forming process, i.e. foam forming of a web, which web is then subsequently pressed and dried to form a sheet or film product. The sheet or film can be used as a single ply paper or as a barrier, barrier laminate or coating of, for instance, a board or other paper product.

(17) According to another embodiment the foam may be used as a coating in the process or as a wet end additive.

(18) According to one embodiment the process includes the fibrillation of the cellulose fibers in the presence of the amphiphilic polymer. This may facilitate the dissolution of amphiphilic polymers, since these substances may have limited or at least low solubility. Performing the fibrillation of the fibers in the presence of the amphiphilic polymer may also stabilize the fibrils formed through the fibrillation process.

(19) According to another embodiment the amphiphilic polymer, e.g. OSA starch, is cooked or heated together with the nanofibrillated polysaccharide, e.g. a microfibrillated cellulose, prior to forming a foam or supplying the mixture in a head-box.

(20) Through the above method it is thus possible to form a paper or paperboard product having wherein the product comprises or constitutes a sheet or film, which in turn has been formed by using the intermediate solution, i.e. mixture of nanofibrillated polysaccharide and surface active polymer as foam.

(21) The sheet or film formed through the process may be, or be applied as, a barrier for moisture, and for aroma, or grease or other fatty substances. According to one embodiment the sheet or film said product is a barrier film or barrier coating having an oxygen transmission rate (OTR) of less than 20 cm.sup.3/m.sup.2/d measured at 50% relative humidity, or less than 15 cm.sup.3/m.sup.2/d measured at 50% relative humidity, or less than 10 cm.sup.3/m.sup.2/d measured at 50% relative humidity, or less than 5 cm.sup.3/m.sup.2/d measured at 50% relative humidity. According to one embodiment the OTR is in the range of 1 to 5 cm.sup.3/m.sup.2/d measured at 50% relative humidity, or in the range of 2 to 4 cm.sup.3/m.sup.2/d measured at 50% relative humidity. The OTR value is measured at 23 C.

(22) According to one embodiment the basis weight or grammage of the paper or film formed through the process may be in the range of from 10 to 100 g/m.sup.2, or in the range of from 10- to 40 g/m.sup.2, or in the range of from 10, to 30 g/m.sup.2, or in the range of from 10 to 25 g/m.sup.2 for a base paper.

(23) In view of the above detailed description of the present invention, other modifications and variations will become apparent to those skilled in the art. However, it should be apparent that such other modifications and variations may be effected without departing from the spirit and scope of the invention.