The present invention relates to a method for modifying the physical and/or chemical characteristics of a fibrous web, and an apparatus for implementing the method.
Production methods for fibrous material are known, in particular for paper webs or cellulose sheets. They generally consist of pouring a mix of fibrous material and water onto an endless conveyor belt in movement. Here the mix is progressively deprived of its water content and subjected to a series of traditional processes which finally lead to the obtaining of a paper web or, in more general terms, to the obtaining of a web of fibrous material, to be then wound into rolls for subsequent uses.
The production of fibrous webs, in particular papers of the most varied type, requires the use of many types of chemical products as additives to give the different paper types particular properties, or to facilitate the process.
These products are either added directly to the initial fiber suspension (to the cellulose pulp in the case of paper) or are applied onto the surface of the fibrous web under formation by methods known to the expert of the art.
In the first case, part of the additives is lost during the initial fiber draining stage on the flat table, to create problems of recovery and disposal of the liquid effluent, and of obtaining the correct targeted concentration of added product relative to the fibers.
In the second case, penetration of the additives into the centre of the sheet becomes difficult and there is greater lack of uniformity along its thickness.
An object of the present invention is to improve the effectiveness of additive addition to said web.
Another object of the present invention is to reduce energy consumption in the additive addition process for said web.
Another object of the present invention is to optimize the consumption of chemical products for modifying the characteristics of said web, including with products not used traditionally in the paper manufacturing industry.
These and other objects which will be apparent from the ensuing description are attained, according to the invention, by a method for modifying the physical and/or chemical characteristics of a fibrous web as described hereinafter.
The invention also comprises an apparatus for implementing the method as also described hereinafter.
The present invention is further clarified hereinafter with reference to the accompanying drawings, in which:
As can be seen from the figures, the method according to the invention starts from a fibrous material web 2 having a dry content between 1% and 90% and hence a moisture content between 10% and 99%.
This fibrous material web 2, which can also be coupled to a suitably heated polymer film, is deposited on a conveyor belt 4 made of elastic material and having at least one portion subjected to transverse extension by any mechanical action, consisting for example of a transverse traction at its edges or in proximity thereto, or a forced removal from the sliding plane of a portion thereof retained at its edges.
Independently of the method by which the conveyor belt 4 is transversely stretched, the fibrous web 2 can be brought into contact with it either before or after the stretching.
In the first case, if before this stretching begins or before it is completed, the fibrous web 2 is deposited on the belt and which because of its high water content is in a pliable state, as the conveyor belt widens it also drags the fibrous web while widening. Adhesion can be promoted by vacuum. When the elastic belt is released it returns to its original dimensions, to drag and recompact the fibrous web adhering to it and modify the weave of the fibers and hence the morphology of the fibrous web to better incorporate the additives.
In the second case the fibrous web 2 is brought into contact with the elastic belt 4 which has already been transversely stretched. Said belt is then released and returns to its original dimensions, to drag and recompact the pliable fibrous web adhering to it. The elastic belt is then again transversely stretched, dragging with it the fibrous web still adhering to it. In both these two cases, at least one additive is added to the fibrous web either before or during the described dimensional variation.
In the case of deformation and subsequent elastic return, the deformation can be utilized to cause the additive to be absorbed. Obviously in this case the elastic return is essential and the additive addition must preferably take place at maximum stretching.
In
At the moment of transverse stretching, the elastic belt undergoes compaction in the longitudinal direction, due to the simultaneous longitudinal shortening of the elastic belt, if this has a normal Poisson deformation coefficient (for example around 0.5). However the simultaneous longitudinal compaction of the belt 4 can be prevented if this is filled with fibers disposed longitudinally and resistant to axial compression (for example steel, Kevlar, carbon), or if it is made from a material having a Poisson coefficient ideally close to zero.
The elastic conveyor belt can consist of one or more layers of possibly expanded elastomer, or of single or multiple fabric formed of threads which may be elastic, or non-elastic but woven in accordance with an elastic weave, or finally of a composite layer formed from the preceding. It can also be permeable to fluids and contain a sponge layer able to absorb and/or release liquids. Finally, the elastic belt can constitute the belt of the so-called flat table, which in a traditional paper machine receives the mix originating from the head box. In this respect, the web 2 of pliable material can originate directly from the head box of any paper processing machine or can be obtained from an already formed paper web already subjected to wetting, and if a mixed material web or a non-woven fabric or a film of only nanocellulose is to be obtained it can consist of cellulose fibers and/or cellulose nanofibers.
To improve adhesion between the web 2 and the elastic surface of the conveyor belt 4, said surface can be modified such as to present high affinity for cellulose. Possible modifications are for example:
using a mixture of elastic material (rubber) and cellulose (fibers, microcrystals and/or nanofibers) for forming the elastic conveyor belt 4,
covering the elastic belt with a coating formed from cellulose (for example microcrystalline fibers and/or nanofibers) and a binding agent (e.g. lactose) or an adhesion promoter (silicates, titanates),
covering the elastic belt with a coating formed from a rubber latex of low glass transition temperature,
covering the elastic belt with formulations typically used for increasing adhesion of the fibrous web to the yankee cylinder used in the production of tissue paper,
forming the elastic belt with elasticized fabric formed partially of cotton fibers,
covering the elastic belt with microhooks.
In the case of excessive adhesion, to detach the fibrous web 2 from the elastic surface a blade of air or water vapour or possibly a doctor blade can be used. If the elastic belt 4 is permeable to fluids, air can be blown therethrough to detach the fibrous web 2.
The widening caused also widens the pores of the fibrous web and makes the already formed surface layers more permeable, making it easier and less costly to dry the web intermediate layer. Said drying can take place by removing water from the fibrous web by applying pressure or vacuum or heat to said web, or a combination of the preceding simultaneously or in succession. During the local extension of the fibrous web or before or after this extension, various additives (normally used either in the mix or as surface treatment) are applied to the surface in a targeted manner by traditional techniques. The widening facilitates deep penetration of the additives along the thickness of the fibrous web. The subsequent contraction of the elastic layer induces by entrainment a simultaneous transverse compaction in the fibrous web and helps to incorporate the added substance by creating a pressure in the transverse direction.
If the additive is added immediately before the widening, the subsequent deformation of the fibrous web produces a widening of the interstices between the fibers, so facilitating absorption and distribution of the additive within the fibrous mass.
It should be noted that to achieve a higher treatment efficiency, a pressure can be applied from above, for example by presser rollers, felts, shoe-presses etc., and/or a vacuum can be applied below the elastic belt if this is permeable to fluids. Presser rollers and felts can have a peripheral velocity different from the underlying elastic belt.
The transverse widening and recompaction of the fibrous web 2 with relative additive addition and/or drying can be repeated several times as schematically shown in
In
In
Stretching the elastic belt in the system shown in
This web remains stabilized in its width and can have a width equal to the original width with compensation for the width loss which the drying causes.
Moreover, in order to facilitate correct transverse stretching of the elastic conveyor belt 4, which given its function must be in continuous contact with support and drive rollers, the sliding of the elastic belt on these conveyor rollers is advantageously favoured by suitable lubricant substances interposed between the two or by suitably varying the belt thickness and/or by suitably convex-shaping the conveyor rollers or by providing these with ball retainers.
By combining the addition of a modifier product with the transverse widening and recompaction of the fibrous web, the additive addition efficiency can be optimized, so limiting effluent production. For example, costly additives such as titanium dioxide can be saved, hence avoiding the production of large quantities of water effluents to be purified, in contrast with what happens when adding it in quantity to the pulp.
Incompatibility between the additives in solution or suspension (for example because of pH incompatibility or because they would form a gel or a precipitate) can be avoided by adding them in different stages. In this manner for example, a gel could be formed directly within the fibrous web by adding two gelling components separately, such as alginate and calcium ions.
This additive addition can consist of spraying, of deposition by rollers, of impregnation with liquid formulations released from a sponge layer forming part of the elastic belt, or other methods known to the expert of the art.
The degree of dryness of the fibrous web is chosen on the basis of the additive to be added, the uniformity of surface distribution, the penetration along the web thickness and/or the final effect to be obtained. In particular, greater control of the degree of surface distribution, including regulated addition, and of the penetration of the additive along the thickness of the fibrous web can be achieved. The additive additions on the two faces of the fibrous web can obviously be different, for example different colors.
By controlling the porosity and the additive distribution along the web thickness, it is possible, for example, to finely regulate the surface sizing of a paper web, to optimize its properties of liquid penetration and of resistance to delamination or to dust, depending on the type of printing for which the paper is intended.
In a similar manner, in tissue paper, finer adjustment is possible of the softening additives which tend to cause a reduction in mechanical strength and to interfere with adhesion to the yankee cylinder and hence with the crinkling process, so reducing their environmental impact.
Deep coloration of the fibrous material can also be obtained by dyes or pigments.
Again, by controlling the distribution of fillers and additives along the thickness together with more controlled removal of moisture, more uniform drying can be obtained, together with a final material less subjected to hygroscopic deformations and loss of planarity.
Additives in powder form are preferably dispersed in water and mixed with binding agents, such as cationic polymers, nanocellulose, polyglycols, acrylic dispersions, styrene-butadiene dispersions, etc.
Said additives can also be activated by administering energy from the outside (heat, UV or visible radiation, microwaves, electron beam, etc.), and provide the required effect only after activation (including external to the paper machine). In particular, the additives can be encapsulated in microcapsules added to the fibrous web and of which the capsule shell can be broken successively by applying pressure or heat, in order to cause release of the additive at the required moment.
The various additives must be able to perform their function and be activated, if necessary, without mutual interference.
The additives to be added can provide properties such as:
porosity control (surface porosity is essential for determining the capacity to filter ink pigments from their carrier and hence for print quality) along the thickness with additives such as:
barrier towards oxygen and/or water vapor
opacity
antigrease
sizing
softness
perfume/emollient properties
dust control, resistance to delamination, in particular during the printing process
water repellence (including for capacitor insulating papers easily soakable in dielectric oils or resins)
hydrophilicity
ink adhesion
antiadherence
adhesive curing rate, particularly polyurethane based
color
voluminosity
possible heating by induction
rigidity and tensile strength (dry and/or wet)
oxygen scavengers
electrical conductivity
antibacterials
By means of the successive fibrous web recompaction and widening processes, the final degree of fiber cohesion can be controlled as a function of the residual moisture. This can also be useful in the production of cellulose sheets as semi-finished products intended for papermaking plants to produce the pulp by means of redispersion.
Finally, depending on the use for which the product is intended, the
method of the invention can be combined with traditional treatment methods for the final fibrous web, and in particular with coupling methods and/or methods for stretching coupled webs and/or production methods for extensible material webs, such as those described for example in EP 772522, in EP 824619, in EP 876536, in EP 946353, in U.S. Pat. No. 2,624,245 or in U.S. Pat. No. 7,918,966.
From the aforegoing it is apparent that the method according to the invention presents the following advantages:
a greater flexibility and efficiency in adding additives which previously had to be added in bulk,
a greater flexibility and efficiency in adding surface additives,
new effects by the possible interaction of both.
Number | Date | Country | Kind |
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VE2011A0071 | Oct 2011 | IT | national |
Filing Document | Filing Date | Country | Kind |
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PCT/IB2012/002160 | 10/25/2012 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
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WO2013/061147 | 5/2/2013 | WO | A |
Number | Name | Date | Kind |
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1643147 | Angier | Sep 1927 | A |
2535734 | Lage | Dec 1950 | A |
3146159 | Muggleton | Aug 1964 | A |
3471363 | Schmidt | Oct 1969 | A |
3586602 | Schmidt | Jun 1971 | A |
Number | Date | Country |
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2010001564 | Feb 2010 | WO |
2011151705 | Dec 2011 | WO |
Number | Date | Country | |
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20140262096 A1 | Sep 2014 | US |