METHOD FOR HYDROPHOBIZING A CELLULOSE SUBSTRATE BY UTILIZING A FATTY ACID HALIDE
20220010493 · 2022-01-13
Assignee
Inventors
Cpc classification
D21H19/14
TEXTILES; PAPER
D21H27/00
TEXTILES; PAPER
International classification
Abstract
The present invention relates to a method for hydrophobizing a cellulose substrate (1), which comprising a first side and a second side, which faces away from the first side, the method comprising the steps of: —drying the cellulose substrate to a dry content above 80%, preferably above 85%; —providing a fatty acid halide in spray form; —converting said fatty acid halide in spray form into vaporized fatty acid halide; and —guiding said vaporized fatty acid halide to contact the first side of the cellulose substrate, and at least partially penetrate the cellulose substrate.
Claims
1. A method for hydrophobizing a cellulose substrate, which comprises a first side and a second side facing away from the first side, wherein the method comprises the steps of: drying the cellulose substrate to a dry content above 80%; providing a fatty acid halide in spray form; converting said fatty acid halide in spray form into vaporized fatty acid halide; and guiding said vaporized fatty acid halide to contact the first side of the cellulose substrate, and at least partially penetrate the cellulose substrate.
2. The method according to claim 1, further comprising the step of: guiding said fatty acid halide to contact the second side of the cellulose substrate, and at least partially penetrate the cellulose substrate.
3. The method according to claim 1, wherein said guiding of the fatty acid halide is performed by vacuum sucking at the second side of the cellulose substrate, such that the vaporized fatty acid penetrates the cellulose substrate in a predetermined direction through the cellulose substrate.
4. The method according to claim 1, wherein said guiding of the vaporized fatty acid halide is performed by vacuum sucking at the first side of the cellulose substrate, such that the vaporized fatty acid is guided along a surface of the first side of the cellulose substrate in a predetermined direction whereby the fatty acid is brought into contact with the cellulose substrate.
5. The method according to claim 1, wherein the dry content of the cellulose substrate is above 90%.
6. The method according to claim 1, wherein the fatty acid comprises an aliphatic chain length of between 10-22 carbon atoms.
7. The method according to claim 1, wherein the fatty acid comprises palmitoyl chloride, C16, stearoyl chloride, C18, or mixtures thereof.
8. The method according to claim 1, wherein the fatty acid to be sprayed is mixed with at least one solvent or a mixture of solvents, wherein the at least one solvent or a mixture of solvents is preferably selected from a group consisting of: acetone, ethyl acetate, and methyl ethyl ketone.
9. The method according to claim 8, wherein the mixture of fatty acid halide and the at least one solvent or a mixture of solvents comprises 0.1-20 wt %.
10. The method according to claim 1, wherein the cellulose substrate is a paper- or paperboard web.
11. The method according to claim 10, wherein the web is a single- or multilayer web.
12. The method according to claim 1, wherein the cellulose substrate comprises a three-dimensional cellulose-based product.
13. The method according to claim 1, further comprising a step of: heating the substrate, before, or after, or before and after adding the fatty acid halide.
14. The method according to claim 13, wherein the heating step is performed by IR heating.
15. The method according to claim 3, wherein the vacuum sucking is performed by a vacuum box.
16. The method according to claim 1, wherein the vacuum sucking is performed by a rotating vacuum cylinder.
17. The method according to claim 1, wherein the step of converting said spray form fatty acid halide into vaporized fatty acid halide is performed by IR heating.
18. A cellulose based product having been treated by the method according to claim 1.
19. The method according to claim 1, wherein the dry content of the cellulose substrate is above 85%.
20. The method according to claim 8, wherein the mixture of fatty acid halide and the at least one solvent or a mixture of solvents comprises 0.1-10 wt % solvent.
Description
FIGURES
[0034] In the following, the invention will be described further with reference to the drawings, wherein:
[0035]
[0036]
[0037]
[0038]
[0039]
DETAILED DESCRIPTION
[0040] The following detailed description illustrates examples of setups for performing the method according to the invention, which may serve to illustrate the principles of the inventive idea in a non-limiting way.
[0041] In
[0042] The cellulose substrate 1 may thereafter be further dried and heated. The heating is preferably performed in a pre-treatment step by IR heating 2 as illustrated in
[0043] The first side of the dried and heated substrate 1 is then treated with a fatty acid halide, in spray form or in gas-phase, to hydrophobize the substrate, such that the substrate becomes hydrophobic. This is accomplished by means of a device 5 (also referred to as “spray device” 5) for dispersing liquid fatty acid halide into a spray 50, which spray may contact the substrate directly or become vaporized into gas phase where such gas contacts the substrate. Said spray device 5 may be in the form of a spray nozzle used for atomizing the liquid. “Spray atomization” here means the transformation of a liquid into a spray of fine particles by mixing the liquid with compressed air. A spray nozzle generates the atomized spray when being passed through an opening at high pressure and in a controlled manner. A higher pressure will create smaller liquid droplets and a finer spray. Different spray devices 5 are conceivable.
[0044] Another example is electrospraying whereby electrical forces are utilized on a liquid that flows from a nozzle, which can have various shapes and conformation, and thereafter fine, uniform and charged droplets are formed, due to that the electrical force exceeds the surface tension force. It can also be due to mechanical distortions. The general advantages of the electrospraying process are that it can be performed as one step at low cost, low energy input and with a good flexibility. Ambient temperatures and pressures also work.
[0045] Upon that said first side of the dried and heated substrate 1 has been treated with a fatty acid halide, the applied fatty acid halide will at least partially penetrate the cellulose of said substrate 1 and bind covalently to the cellulose therein, increasing the water repellency of the material. In order to enhance the penetration of the spray or gas through the substrate, the second side of the substrate can be subjected to a vacuum suction, simultaneously, during the hydrophobation of the substrate, such that the spray or gas is transported in a predetermined direction through the substrate. This enhances the hydrophobicity of the surface as well as the core of the substrate, so that the substrate will be more resistant against in-plane edge penetration.
[0046] The fatty acid halide is any halide that can be vaporized, however palmitoyl chloride, C16 has, in tests, shown to be particularly suitable. During tests a covalent degree of above 40% and even above 60% has been achieved, compared to conventional AKD sizing where no or just a small percentage of covalent binding can be obtained, which results in low retention, which thereby leads to e.g. migration problems, stains and machine stops etc.
[0047] Another advantage with use of spray combined with gas/vaporization for applying the fatty acid halide is that it is very position specific and hydrophobicity is only achieved where the spray or gas can access the substrate. The reagent will react with the available hydroxyl groups forming HCl as a by-product. The reagent is also highly reactive towards water and the reaction requires dry substrates. Nevertheless, there will always be some presence of water whereupon the corresponding, less reactive, fatty acid also will be formed as an unbound molecule. It is therefore impossible to achieve 100% covalent degree. Yet, other advantages with the use of a gas-phase reaction is that the gas can be penetrated and guided through the substrate more easily, the reaction can be faster and a lower amount of chemical reagents may be needed compared to application of the same reagent in a liquid state.
[0048]
[0049] Liquid fatty acid halide is stored in a separate tank 3 wherefrom it is ejected through a device 5 for dispersing the liquid into a spray 50. Such spray device 5 can for instance be in the form of a spray nozzle used for atomizing the liquid, i.e. breaking up the fluid into droplets 50. In the present example, the droplets are sprayed by means of the device 5 onto a first side 1a of the underlying, running substrate 1. Said first side 1 aside of the substrate 1 is at the same time in contact with a downstream rotating cylinder 6, for instance a heated cylinder that heats the droplets into gas whereby the atomized fatty acid molecules react more efficiently with the cellulose of the substrate. It is conceivable to arrange multiple spraying units positioned after each other in sequences in connection to the running substrate, where each such unit can comprise one or a plurality of spraying nozzles. This would enable for application of fatty acid in consecutive steps, whereby smaller doses can be applied several times instead of one unit applying the whole amount at one occasion. Such procedure may in some cases improve the penetration of the reagent in the thickness of the cellulose web.
[0050] It is also conceivable that a rotating vacuum cylinder with holes (not shown) is arranged in connection with a second side 1b of the substrate and downstream of the spray device 5, arranged to vacuum sucking droplets or vaporized fatty acid halide in a predetermined direction through the cellulose substrate 1. Thereby, the cellulose substrate 1 can be hydrophobized through the complete thickness of the substrate.
[0051] Another arrangement for applying the fatty acid halide is that the substrate 1 is arranged to enter between two nip rolls (not shown), preferably where at least one of the rolls is a heated nip roll, and that the fatty acid halide spray is directed into the nip roll junction whereby the spray droplets are converted into gaseous phase by means of the heated roll/s. In this arrangement, the spray may also be directed to contact the heated nip roll immediately upstream of the nip roll junction, whereby the fatty acid halide is vaporised by the heat of the roll and directly thereafter, i.e. within seconds or milliseconds, applied onto the substrate.
[0052] Yet another arrangement for applying the fatty acid halide is that the fatty acid halide is sprayed directly onto a heating roll arranged to immediately, i.e. within seconds or milliseconds, transfer said fatty acid halide onto a running substrate. Upon contacting the substrate, the heat from the roll will transform the fatty acid halide into gas phase meaning that the vaporization occurs simultaneously with that the fatty acid halide is brought into contact with the substrate. In such embodiment, the heated roll provides several functions: the function of bringing the fatty acid halide into contact with the substrate, the function of vaporizing the fatty acid halide into gas phase and the function of promoting the chemical reaction to covalent bind the fatty acid halide to the substrate. Vaporization of the fatty acid halide can be arranged to occur before the heated roll contacts the substrate, or simultaneously with that the heated roll contacts the substrate depending on where on the heated roll the spray is applied. E.g. if the spray is directed so that the fatty acid halide hits the heated roll a small distance prior to that said roll contacts the substrate the vaporization will take place before contact, whereas in case the spray is directed so that the fatty acid halide hits the heated roll at the nip between the roll and the substrate the vaporization will take place simultaneous to contact. If not all the spray is vaporized, it will still be distributed in a uniform matter on the roll and then be taken up by the board in droplet form.
[0053] Moreover, the HCl by-product and possibly unreacted e.g. palmitoyl chloride and/or unbound C16 can be removed and collected for handling.
[0054] In
[0055] Liquid fatty acid halide is stored in a separate tank 3 wherefrom it is transferred e.g. via a tube 4 (or other transferring means) to a device 5 for dispersing the liquid into a spray 50. Such device 5 can for instance be in the form of a spray nozzle used for atomizing the liquid, i.e. breaking up the fluid into droplets 50. In the present example, the droplets are sprayed via the device 5 into a heating chamber 7 such as a pressurized heating tank 7. The spray droplets are heated inside said tank 7 to vaporize into gas-phase, and said gas 70 is thereafter ejected or deposited through a gas spreading device 71 onto the first surface of said substrate 1. Said first side of the substrate is at the same time in contact with a rotating cylinder 6. Yet another rotating cylinder of vacuum type may be arranged at the second side 1b of the substrate for sucking the gas in a predetermined direction through the cellulose substrate 1. Thereby, the cellulose substrate 1 can be hydrophobized through the complete thickness of the substrate. Any HCl by-product and possibly unreacted e.g. palmitoyl chloride and/or unbound C16 can be removed and collected for handling.
[0056] For both exemplified methods shown in
[0057]
[0058] Referring to
[0059] A fourth embodiment according to the invention is seen in
[0060] The fatty acid halide in the fourth embodiment can be converted from spray form to gaseous form before being guided to contact the substrate 1.
[0061] In
[0062]
[0063] To characterize the success of the reaction, contact angle measurement was utilized to qualitatively analyze how much the cellulose substrate has been hydrophobized by the method. An un-treated cellulose substrate had before a contact angle around 40° and after treatment of the inventive method a contact angle of 110-130° on both the first side and the second side of the substrate, despite only one surface was in direct contact with the reagent. Contact angles greater than 90° (high contact angle) generally means that wetting of the surface is unfavourable, so the fluid will minimize contact with the surface and form a compact liquid droplet.
[0064] In view of the above detailed description of the present invention, other modifications and variations will become apparent to those skilled in the art. For example, the method according to the invention may be used as a complement to other methods of application of fatty acid halide onto a substrate. However, it should be apparent that such other modifications and variations may be affected without departing from the spirit and scope of the invention.