Patent Application
20150308017
The present document relates to a method of drying an aqueous suspension of nanofibrillated polysaccharide to obtain an substantially dry nanofibrillated polysaccharide product. More particularly, the present disclosure relates to a nanofibrillated polysaccharide product obtainable by such method and the uses thereof.
Nanofibrillated polysaccharides, such as for instance microfibrillated cellulose, have many end uses, such as in food, composites, paper, paints, plastics, cosmetics, and medical products, in which it would be good to be able to dosage nanofibrillated polysaccharide in a dry form so that the original properties of wet nanofibrillated polysaccharide would be retained.
Microfibrillated cellulose which is added and used in composites is typically in a dry form.
When microfibrillated cellulose is used in composites one should ensure that micro fibrils are clearly separated from each other and that micro fibrils are very well dispersed on the matrix.
A low solid content dispersion of microfibrillated cellulose in water is usually a gel having pseudoplastic or thixotropic viscosity properties because the fibrils are very well dispersed in the matrix (water). Upon drying, however, the properties of microfibrillated cellulose are severely changed. It's dispersibility, hydration and rheological properties are lost or at least substantially reduced or changed, depending on the severity of the drying. Typically after drying, micro and nano fibrils are bound together and substantially less separate micro or nano fibrils are present which hence affects the characteristic property, for instance, as defined by a highly nanofibrillated cellulose can be found via different analysis of the nanofibrillated cellulose.
Conventional drying techniques for drying MFC or nanofibrillated polysaccharides currently used today are e.g. spray drying and freeze drying. Freeze drying produces the best quality MFC in terms of preserving original properties and in re-dispersability. However, both the operating and investment costs are high and the process can be difficult to scale up to industrial processing. Spray drying, which can rather easily be scaled up, has high operation costs and during which process also hornification of fibrils is prone to occur.
The term “hornification” refers to the stiffening of the polymer structure that occurs in lignocellulosic materials when they are dried or otherwise dewatered. Because of structural changes in the wood pulp fibers upon drying the internal fiber shrinks. Often the fibers needs to be rewetted, or re-suspended in water for practical use and due to these structural changes the original properties, i.e. being in a gel form having pseudoplastic or thixotropic viscosity, is not regained. The effect of hornification may be identified in those physical paper or wood pulp properties that are related to hydration or swelling, such as burst or tensile properties. (Hornification—its origin and interpretation in wood pulps, J. M. B. Fernandes Diniz, M. H. Gil, J. A. A. M. Castro, Wood Sci Technol 37 (2004) 489-494).
In articles (e.g. LeCompte T. R. (1931), Papier (34), p. 1193, Jayme, G. (1944) Papier-Fabr (42), p. 187, Lyne, L. M., Gallay, W. (1954) Measurements of wet web strength, Tappi Journal 37(12):694-697, Higgins, H. G., Mckenzie, A. W. (1963) The structure and properties of paper XIV: Effects of drying on cellulose fibers and the problem of maintaining pulp strength) concerning hornification phenomenon and pulp swelling after drying and rewetting there are suggestions made that pulp could be less hornificated if its dried in such a way that fibers do not stick together during drying. According to Lyne and Gallay (1950) rigorous agitation during boiling of pulp neutralizes the dehydrating effect, and that mechanical effect prevents to a large extent the loss in swelling which otherwise occurs.
It is however impractical for pulp and papermakers to dry fibers under e.g. vigorous agitation.
Spray-drying of fibrillated cellulose is described e.g, in WO 2011/139749 A2. An aqueous suspension of nanofibrils (NFC), which are regarded as a category of MFC, is atomized in a drying chamber of a drying apparatus. A drying gas, such as ambient air, may be used as an aid to evaporate the water present in the suspension, yielding dry NFC as the product. The teachings even include coating the NFC particles with sodium silicate prior to the atomizing step.
WO 2011/095335 A1 describes a process, in which MFC is formed by defibrillation of a suspension of cellulose fibers and a liquid, which is miscible with liquid CO2, and then replacing said liquid in the suspension by liquid CO2, and finally removing the CO2 by evaporation so as to yield dry MFC. The process is claimed to overcome the MFC deterioration problems afflicting ordinary oven-drying and freeze-drying processes.
Still there is room for an improved process of drying nanofibrillated polysaccharide comprising composites, which is simpler to carry out while yielding a dry MFC composite material, without loss of important re-dispersibility properties, since, if strong hornifiction or agglomeration occurs during drying the beneficial properties of cellulosic fibrils or fibrillated aggregates are not obtained. It it thus preferable that the dried composite maintains its characteristics when dispersed in aqueous systems, other solvents or e.g. polymeric matrices, It is also necessary to find a solution that prevents hornification without necessary use of chemical additives, which might affect the properties of the final composition.
It is an object of the present disclosure, to provide an improved or alternative method of drying microfibrillated cellulose, which eliminates or alleviates at least some of the disadvantages of the prior art.
The invention is defined by the independent claims. Embodiments are set forth in the appended dependent claims and in the following description and drawings.
According to a first aspect, there is provided a method for drying nanofibrillated polysaccharide to obtain a substantially dry nanofibrillated polysaccharide product, comprising the following steps:
(i) providing an aqueous suspension of nanofibrillated polysaccharide;
(ii) increasing the solid contents said suspension, thereby forming a high solid contents microfibrillated cellulose suspension; and
(iii) drying said high solid contents microfibrillated cellulose suspension, through a simultaneous heating and mixing operation.
By “aqueous suspension of nanofibrillated polysaccharide” (NFP) is meant that the solid contents of the suspension is in the range of 0.01 wt-% to 25 wt-%. This suspensiom or dispersion in water may be in a gel form. The said suspension might also contain functional additives which assist in re-dispersability but they can also have another function such as providing optical effects or improved compoundability in polymers.
The term “nanofibrillated polysaccharide” includes nanofibrous polysaccharides, micro or nano fibrillated cellulose (MFC/NFC), micro or nano crystalline cellulose (MCC/NCC), regenerated cellulose, cellulose whiskers, nanofibers spun from polysacchardies such as starches, cellulose nanoparticles, porous cellulose particles, starch fibrils, or mixtures thereof or mixtures with normal pulp or fibers or with inorganic or organic synthetic fibers. The nanofibrillated polymer can also be surface modified with e.g. one or several polymer layers.
By “substantially dry NFP product” is meant that the water content in the NFP product is reduced to a level where the product may be in a powder form, but still being suitable for re-dispersion in a solvent such as water. As such the solids content of the product may be in the range of 50-99 wt-%.
By this method there is achieved a way of drying NFP without causing hornification problems of the micro fibrils and pulp swelling after drying and rewetting. There is further provided a way of drying the NFP in a energy efficient manner.
By the mixing operation removal of water may be affected by evaporation or using co-solvents, such as ethanol or isopropanol. The co-solvents may be recycled during the mixing and heating operation.
The mixing operation also provides for micro fibrils that are clearly separated from each other and that micro fibrils are very well dispersed in the matrix, which is normally achieved by a refining or homogenizing step a the process for producing e.g. MFC.
According to one alternative of the first aspect the solid contents may, in step (ii), be increased to >15 wt-%, or to >20 wt-%, or to >25 wt-% , or to >30 wt-%.
This solids content is based on the NFP-water ratio, but it may in certain cases contain other substances in which case the solids content may be even higher.
According to another embodiment step (iii) may comprise a grinding operation.
The grinding operation may be performed in a PVC mixer or by any similar method, such as a high speed mixer, where the mechanical energy is converted into heat in the suspension whereby water is caused to evaporate. Alternativley part of the energy may be used to provide for a fibrillation or to cut fibers. Since the solid content, or the dry contents, of the suspension is relativley high at the onset of mixing the shear forces, and friction evolved in the suspension becomes greater thus resulting in an increased temperature. At a solids content of >15-20 wt-% the NFP solution is viscous, thus causing greater friction.
Step (ii) may further comprise any one of a centrifugal force operation, pressing operation and dewatering operation.
The dewatering operation may comprise an electro-osmosis operation or electric field induced dewatering, electric field flow fractionation and the pressing operation may comprise a wet pressing operation.
According to one alternative of the first aspect, the temperature of the suspension, at step (iii) may be in the range of 75-99° C., preferably about 80-85° C.
The temperature is thus kept relativley low, which is advantageous not only in that less energy is consumed, but also in that the effect on hornification of the micro fibrils may be reduced, as hornification is prone to occur at a higher temperature. It may be that the temperature towards the end of the drying process is more important to control, or to keep at a low level in order to prevent hornification of the fibrils, and that the temperature at the beginning of the process, i.e. when the solids content is still relativley low may be higher than the preferred temperature range. This increase in temperature may mainly be created through the mechanical energy provided to the suspension by the mixing operation.
According to an alternative embodiment the suspension may further be heated from about room temperature to the range of 75-99° C.
According to one alternative embodiment, the temperature of the suspension in or at step (iii) may be in the range of from 40 to 50° C., which is a sufficient temperature for the drying to occur. This means that the heat evolved from the mixing operation it self may be sufficient for the drying.
According to one embodiment of the method according to the first aspect there may further be provided a simultaneous heating and mixing operation in step (iii). This means that the suspension may, in step (iii) be actively heated in addition to the heat evolved during the mixing operation. This “active heating” may for instance be used at the onset of the mixing operation to achieve a higher starting temperature and thus a more efficient drying. According to another embodiment this heating operation may be combined with a subsequent cooling operation to ensure the optimal temperature of the suspension as the solid content is increased, i.e. towards the end of the drying operation, in order to prevent any hornification or other harmful structural changes from occuring.
According to another embodiment of the first aspect step (iii) may be performed under vacuum.
By introducing a vacuum, or performing the drying step under vacuum it is further possible to reduce both the energy needed and the drying temperature, which may lead to a further reduction in the hornification of the micro fibrils. If vacuum is introduced the heat developed trough the mechanical energy provided to the suspension may be lower than under normal pressure.
The nanofibrillated polysaccharide may, according to onel alternative of the first aspect of the invention, be a nanofibrillated cellulose or a microfibrillated cellulose.
The nano- och microfibrillated cellulose may be obtained through conventional methos such as mechanical liberation of fibrils or by acid hydrolysis of cellulosic materials, e.g. disclosed in WO 2009021687 A1, or MFC suspension produced by enzymatic hydrolysis of Kraft pulp cellulose, e.g. disclosed in W02011004300 A1 acid hydrolysis followed by high pressure homogenization, e.g. disclosed in US20100279019, or by any other means known to the skilled person. One method of producing nanofibrils is by spinning or e-spinning cellulose or polysaccharides or mixtures thereof.
The concentration of MFC is usually about 1-6% and the remaining part is water or components used to promote e.g. runnability or used for grafting of fibrillated cellulose such as Na-CMC.
According to yet an alternative of the first aspeact there may further be provided a drying additive in step (iii).
By introducing a drying additive the drying process may be event further improved. Such additives are disclosed in CA1208631. A drying additive may also be a solvent.
According to a second aspect there is provided a substantially dry nanofibrillated polysaccharide product obtainable by the method according to the first aspect.
By “substantially dry NFP product” is meant that the water content in the NFP product is reduced to a level where the product may be in a powder form, but still being suitable for re-dispersion, in a solvent such as water or solid phase.
As such the solids content of the product may be in the range of 50-99 wt-%. In a preferred embodiment the solids content is in the range of 75-90 wt-%.
The dry NFP or MFC product obtained through the method described above may have very good and well separated straight individual micro fibrils when re-dispersed in water, i.e. the hornification problems normally associated with drying of NFP has been greatly reduced. The applicability of this dried NFP product may therefore be greatly increased for applications such as composites, paints, food and pharmaceutical uses.
According to a third aspect there is provided a use of a dry nanofibrillated polysaccharide product according to the second aspect in, or for the production of composites.
According to a fourth aspect there is provided a use of a dry nanofibrillated polysaccharide product according to the second aspect, for any one of a rheology application, fixative agent, strength enhancing agent, emulsifying agent, excipient, paper applications, film forming agent, moisture control agent, and in paper or paperboard of products thereof.
The dry product may thus be used in, for instance, textiles, food, pharmaceuticals, paints, concrete, asphalt, rubber, plastic-wood composites, inks, etc.
In the below, a method of drying a nanofibrillated polysaccharide, or as it may be a microfibrillated cellulose is disclosed. These definintions may be used alternately in the below, but is not intended to exclude one or the other. The definitions for nanofibrillated polysaccharide and microfibrillated cellulose may also be found in the below description.
In a preferred embodiment, however, the method is applied to the drying of microfibrillated cellulose or nanofibrillated cellulose, in a pure form or alternativley including additives.
According to one embodiment the method of drying nanofibrillated polysaccharide (NFP), is provided through a process in which an aqueous suspension of NFP is provided. The solid contents of this suspension may be in the range of 0.01 wt-% to 25 wt-%, according to one embodiment the solids content is the range of 0.01 wt-% to 15 wt-% (can be 20-25%).
The solids content or the consistency of this aqueous suspension is then increased to at least 15% by weight. According to one embodiment the solids content of the suspension is raised to 30-35%.
This increase may be performed by a mechanical dewatering. According to one embodiment this dewatering is performed by centrifugation. According to another embodiment it is performed through pressing, such as wet pressing in a paper making machine. According to yet an alternative embodiment the dewatering is performed through electro-osmosis combined with mechanical pressure. Other alternative ways to provide for an increase in the solids content of the suspension may include, but is not limited to any one of a decanter centrifuge, wire press, belt press,extended dewatering nips, and magnetically induced dewatering. The dewatering may also be performed by heating to a suitable temperature, evaporation, or adsorption e.g. into felt or using radiation such as IR, NIR or microwave. When selecting the suitable manner to increase the solids content care must however be taken that the chosen method does not, in a negative way, influence the occurrence of hornification, which the skilled person would readily be able to determine.
According to the method, after the solids content has been increased the suspension is dried. This drying operation is performed through a simultaneous grinding and heating of the suspension, for instance in a mixing apparatus, and thereby effecting removal of water by evaporation.
Alternatively the drying operation is performed under vacuum, i.e. the suspension is treated under vacuum.
According to one alternative the drying is performed through a grinding drying operation, e.g. by PVC mixer similar method where heat and mechanical energy is introduced at the same time as water is allowed to evaporate.
According to one embodiment, at the drying operation, the temperature of the suspension is in the range of 75-99° C., preferably about 80° C. For instance the mixing apparatus may heat the dispersion from about room temperature to the range of 75-99° C.
The effect of the temperature in drying step of the process is critical, which was found here. An optimal temperture, particularly at the end of drying, prevents hornification of the fibers. By optimal temperature is thus meant a temperature which is low enough to prevent the hornification process.
According to one alternative a temperature range of from 40 to 50° C. is a low enough temperature.
According to one embodiment the drying step can be done in presence of different additives, such as those disclosed in CA1208631.
According to one embodiment the suspension may be cooled or kept at a constant temperature by cooling or heating the suspension. The cooling or heating may be performed by conventional means known to the skilled person.
According to one alternative embodiment the temperature of the suspension may be further increased, for instance in the mixing appartus after the NFP suspension has been dried to a water content of at most 10 wt-%.
The total drying time at the drying operation step may be in the range of 15-40 min, preferably about 30 min, thus allowing for a fast and drying operation which may be incorporated into a industrial process. The drying time may be dependent on the initial solids content of the suspension, the energy input, any additives and the batch size.
This definition includes bacterial cellulose or nanocellulose spun with either traditional spinning techniques or membrane technique or then with electrostatic spinning. In these cases, the material is preferably a polysaccharide but not limited to solely a polysaccharide.
Also whiskers, microcrystalline cellulose (MCC) and nanocellulose Crystals (NCC) regenerated cellulose particles or fibers is included in this definition. It can also be a mixture of e.g. MCC and MFC.
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 nanofiber is normally very thin (˜20 nm) and the length is often between 100 nm to 10 μm. However, the microfibrils may also be longer, for example between 10-200 μm, but lengths even 2000 μm 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, whiskers are also included in the definition MFC.
Microfibrillated fibers were dewatered in paper machine type of wire section and subsequent wet pressing to a solids content of about 30-35% by weight. The high solids MFC was dosaged into a PVC mixer and mixed so that the temperature was increased to about 80° C., until the MFC was substantially dry, after which the temperature was further incrased to about 95° C. In this example a PVC mixer having a size of was 200/100 liters was used. The motor was of 50 kW.
The total drying time was about 30 min and the batch size was 25 kg wet MFC dispersion, which gave about 9 kg dry MFC.
After rewetting of micro fibrillated cellulose it was studied under microscope; and very good and well separated straight individual micro fibrils could be seen. This in turn implies that little or no hornification of the micro fibrils has taken place, which was confirmed with water retention value measurements. This type of micro fibrills are very well suitable for composites and other applications where dry micro fibrillated cellulose is preferred instead of wet.
| Number | Date | Country | Kind |
|---|---|---|---|
| 1251280-2 | Nov 2012 | SE | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/IB2013/059778 | 10/30/2013 | WO | 00 |
