Method for producing nanofibrillar cellulose and nanofibrillar cellulose product

Abstract

In a method for producing nanofibrillar cellulose, cellulose based fibre material, in which internal bonds in cellulose fibres have been weakened by 5 preliminary modification of cellulose, is subjected to disintegration treatment in form of pulp comprising fibres and liquid. The fibre material is supplied at a consistency higher than 10 wt-%, preferably at least 15 wt-%, to a disintegration treatment where fibrils are detached from the fibre material by joint effect of repeated impacts to the fibre material by fast moving 10 successive elements and the weakened internal bonds of the cellulose fibres. The nanofibrillar cellulose is withdrawn from the disintegration treatment at dry matter which is equal or higher than the consistency of the fibre material.

Claims

1. A nanofibrillar cellulose product, which is in the form of moist powder containing particles formed of cellulose nanofibrils wherein a dry matter content of the moist nanofibrillar cellulose powder is between 16-60 wt-% based on the dry matter of nanofibrils, where a cellulose in a fibrous starting material is chemically modified cellulose and the median particle diameter of the nanocellulose powder by laser diffraction analysis is 100-1000 micrometers, wherein the cellulose is oxidized cellulose having carboxylate content of at least 0.8 mmol/g or higher, carboxymethylated cellulose having degree of substitution above 0.1, or cationized cellulose having degree of substitution of at least 0.1 or higher; wherein the nanofibrillar cellulose product is obtained directly after a disintegration treatment of cellulose.

2. The nanofibrillar cellulose product according to claim 1, wherein when dispersed to a concentration of 0.1 wt-% in water, the turbidity of the nanofibrillar cellulose aqueous dispersion is lower than 80 NTU, measured by nephelometry.

3. The nanofibrillar cellulose product according to claim 1, wherein when dispersed to a concentration of 0.1 wt-% in water, the turbidity of the nanofibrillar cellulose aqueous dispersion is from 10 to 60 NTU, measured by nephelometry.

4. The nanofibrillar cellulose product according to claim 1, wherein the dry matter content of the nanofibrillar cellulose powder is between 20-35 wt-% based on the dry matter of nanofibrils.

5. The nanofibrillar cellulose product according to claim 1, wherein the dry matter content of the nanofibrillar cellulose powder is between 22-30 wt-% based on the dry matter of nanofibrils.

6. The nanofibrillar cellulose product according to claim 1, wherein the cellulose is ionically charged cellulose.

7. The nanofibrillar cellulose product according to claim 1, wherein the cellulose is oxidized cellulose having carboxylate content of at least 0.95 mmol/g or higher, carboxymethylated cellulose having degree of substitution of at least 0.12 or higher, or cationized cellulose having degree of substitution of at least 0.15 or higher.

8. The nanofibrillar cellulose product according to claim 1, wherein the cellulose is oxidized cellulose having carboxylate content of at least 1.00 mmol/g or higher, carboxymethylated cellulose having degree of substitution in the range of 0.12-0.2, or cationized cellulose having degree of substitution in the range of 0.1-0.6.

9. The nanofibrillar cellulose product according to claim 1, wherein the cellulose is oxidized cellulose having carboxylate content in the range 0.8-1.8 mmol/g, or cationized cellulose having degree of substitution between 0.15-0.35.

10. The nanofibrillar cellulose product according to claim 1, wherein the cellulose is oxidized cellulose having carboxylate content between 0.95-1.65 mmol/g.

11. The nanofibrillar cellulose product according to claim 10, wherein when dispersed to a concentration of 0.5% in water, it has a yield stress is between 3 to 20 Pa.

12. The nanofibrillar cellulose product according to claim 1, wherein the cellulose is oxidized cellulose having carboxylate content between 1.00-1.55 mmol/g.

13. The nanofibrillar cellulose product according to claim 1, wherein when dispersed to a concentration of 0.5% in water, it has a zero shear viscosity of 1,000 to 50,000 Pa.Math.s and a yield stress of 1 to 50 Pa.

14. The nanofibrillar cellulose product according to claim 1, comprising fibrils or fibril bundles having a number-average diameter below 200 nm and a length exceeding one micrometer.

15. A medical product comprising the nanofibrillar cellulose product according to claim 1.

16. A cosmetic product comprising the nanofibrillar cellulose product according to claim 1.

17. The nanofibrillar cellulose product according to claim 1, wherein when dispersed to a concentration of 0.5% in water, it has a zero shear viscosity of 5,000 to 50,000 Pa.Math.s and a yield stress of 3 to 30 Pa.

18. The nanofibrillar cellulose product according to claim 1, wherein in the moist powder the fibrils of the nanofibrillar cellulose are gathered to moist cellulose particles aggregated due to moisture dependent stickiness of the particles.

19. The nanofibrillar cellulose product according to claim 1, wherein the nanofibrillar cellulose is obtained by a method comprising: preparing cellulose based fibre material, in which internal bonds in cellulose fibres have been weakened by preliminary chemical modification of cellulose, in form of pulp suspension comprising fibres and liquid, wherein cellulose based fibre material, in which internal bonds in cellulose fibres have been weakened by preliminary chemical modification of cellulose, is subjected to disintegration treatment in form of pulp suspension comprising fibres and liquid supplying the pulp suspension at a consistency higher than 10 wt-% based on the proportion of the fibres in the pulp suspension, to a disintegration treatment; detaching fibrils from the fibre material in course of said disintegration treatment by joint effect of repeated impacts to the fibre material by fast moving successive elements and the weakened internal bonds of the cellulose fibres; and withdrawing the nanofibrillar cellulose from the disintegration treatment at dry matter which is equal or higher than the consistency of the fibre material.

20. The nanofibrillar cellulose product according to claim 17, wherein the fibre material supplied to the disintegration treatment is ionically charged cellulose having one of the following properties: oxidized cellulose having carboxylate content of at least 0.8 mmol/g pulp or higher, carboxymethylated cellulose having degree of substitution above 0.1, or cationized cellulose having degree of substitution of at least 0.1 or higher.

21. The nanofibrillar cellulose product according to claim 17, wherein the pulp suspension is subjected to the disintegration treatment having a content of gas of greater than 10 volume percent.

22. The nanofibrillar cellulose product according to claim 17, wherein the disintegrating treatment, the fibre material is subjected to repeated impacts successively from opposite directions.

Description

DESCRIPTION OF THE DRAWINGS

(1) In the following, the invention will be described in more detail with reference to the appended drawings, in which:

(2) FIG. 1 shows the device used in the invention in a sectional plane A-A coinciding with the axis of rotation of the rotors,

(3) FIG. 2 shows the device of FIG. 1 in a partial horizontal section, and

(4) FIG. 3 shows viscosity of various product samples.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

(5) Fibre Material

(6) The starting material subjected to the disintegration treatment is fibre raw material which is at a high consistency. The cellulose of the fibre material is chemically modified to high degree to enhance the separation of the fibrils (fibrillation) at high consistency.

(7) The fibre raw material for the chemical modification of cellulose is obtained normally from cellulose raw material of plant origin. The raw material can be based on any plant material that contains cellulosic fibers, which in turn comprise microfibrils of cellulose. The fibers may also contain some hemicelluloses, the amount of which is dependent on the plant source. The plant material may be wood. Wood can be from softwood tree such as spruce, pine, fir, larch, douglas-fir or hemlock, or from hardwood tree such as birch, aspen, poplar, alder, eucalyptus or acacia, or from a mixture of softwoods and hardwoods. Non-wood material can be from agricultural residues, grasses or other plant substances such as straw, leaves, bark, seeds, hulls, flowers, vegetables or fruits from cotton, corn, wheat, oat, rye, barley, rice, flax, hemp, manila hemp, sisal hemp, jute, ramie, kenaf, bagasse, bamboo or reed.

(8) One preferred alternative is fibers form non-parenchymal plant material where the fibrils of the fibers are in secondary cell walls. The fibrils originating in secondary cell walls are essentially crystalline with degree of crystallinity of at least 55%. The source can be wood or non-wood plant material. For example wood fibres are one abundant fibrous raw material source. The raw material can be for example chemical pulp. The pulp can be for example softwood pulp or hardwood pulp or a mixture of these.

(9) The common characteristic of all wood-derived or non-wood derived fibrous raw materials is that nanofibrillar cellulose is obtainable from them by disintegrating the fibers to the level of microfibrils or microfibril bundles.

(10) The modification treatment to the fibers can be chemical or physical. In chemical modification the chemical structure of cellulose molecule is changed by chemical reaction (“derivatization” of cellulose), preferably so that the length of the cellulose molecule is not affected but functional groups are added to β-D-glucopyranose units of the polymer. The chemical modification of cellulose takes place at a certain conversion degree, which is dependent on the dosage of reactants and the reaction conditions, and as a rule it is not complete so that the cellulose will stay in solid form as fibrils and does not dissolve in water. In physical modification anionic, cationic, or non-ionic substances or any combination of these are physically adsorbed on cellulose surface. The modification treatment can also be enzymatic. In enzymatic modification, enzymes that act on cellulose are added to the fibre starting material.

(11) The cellulose in the fibers can be especially ionically charged after the modification, because the ionic charge of the cellulose weakens the internal bonds of the fibers and will later facilitate the disintegration to nanofibrillar cellulose. The ionic charge can be achieved by chemical or physical modification of the cellulose. The fibers can have higher anionic or cationic charge after the modification compared with the starting raw material. Most commonly used chemical modification methods for making an anionic charge are oxidation, where hydroxyl groups are oxidized to aldehydes and carboxyl groups, and carboxymethylation. A cationic charge in turn can be created chemically by cationization by attaching a cationic group to the cellulose, such as quaternary ammonium group.

(12) One preferred modification method is the oxidation of cellulose. In the oxidation of cellulose, the primary hydroxyl groups of cellulose are oxidized catalytically by a heterocyclic nitroxyl compound, for example 2,2,6,6-tetramethylpiperidinyl-1-oxy free radical, “TEMPO”. These hydroxyl groups are oxidized to aldehydes and carboxyl groups. Thus, part of the hydroxyl groups that are subjected to oxidation can exist as aldehyde groups in the oxidized cellulose, or the oxidation to carboxyl groups can be complete.

(13) So that the fibre material can be fibrillated at high consistency, the preceding chemical modification of the cellulose must proceed to a sufficiently high level. Fibre material modified by catalytic oxidation has carboxylate content of at least or above 0.8 mmol/g, preferably at least or above 0.95 mmol/g, and most preferably at least or above 1.00 mmol/g, based on weight dried pulp. The carboxylate content is preferably in the range of 0.8-1.8, more preferably 0.95-1.65 and most preferably 1.00-1.55 mmol/g. In fibre material where the cellulose is carboxymethylated, the degree of substitution is above 0.1, preferably at least or above 0.12. The degree of substitution is preferably in the range of 0.12-0.2 in the carboxymethylated cellulose. In fibre material where the cellulose is cationized, the degree of substitution is at least or above 0.1, preferably at least or above 0.15. The degree of substitution is preferably in the range of 0.1-0.6, more preferably 0.15 0.35 in the cationized cellulose.

(14) Cellulose modified physically by adsorbing anionic or cationic substances on cellulose surface contains the adsorbed substances in sufficiently high amounts, 20-1000 mg/g, preferably 40-500 mg/g and most preferably 90-250 mg/g, based on weight of dried pulp. The substances added are preferably water-soluble. For example sodium carboxymethyl cellulose (CMC) is a substance that can be added to make anionically charged physically modified cellulose.

(15) The anionic or cationic substances are preferably adsorbed in an amount corresponding to the preferable amounts of cationization or anionization (chemical modification) which can be expressed as molar equivalents (eq/g or meq/g), that is, in an amount representing the same amount of ionic charge as obtained by chemical modification per 1 g pulp.

(16) Nanofibrillar Cellulose

(17) In this application, nanofibrillar cellulose (NFC) refers to collection of isolated cellulose nanofibrils (also called microfibrils) or nanofibril bundles derived from cellulose based fibre material. Nanofibrillar cellulose has typically a high aspect ratio (length/diameter): the length might exceed one micrometer while the number-average diameter is typically below 200 nm. The diameter of nanofibril bundles can also be larger but generally less than 5 μm. The smallest nanofibrils are similar to so called elementary fibrils, which are typically 2-12 nm in diameter. The dimensions of the fibrils or fibril bundles are dependent on raw material and disintegration method. The nanofibrillar cellulose may also contain some hemicelluloses; the amount is dependent on the plant source. Nanofibrillar cellulose is characterized by a large specific surface area and a strong ability to form hydrogen bonds. In water dispersion, nanofibril cellulose typically appears as either light or almost colourless gel-like material. Depending on the fibre raw material, nanofibrillar cellulose may also contain small amounts of other wood components, such as hemicellulose or lignin. Often used parallel names for nanofibrillar cellulose include nanofibrillated cellulose (NFC), which is often simply called nanocellulose, and microfibrillated cellulose (MFC).

(18) The nanofibrillar cellulose can also be characterized through some rheological values. NFC forms a viscous gel, “hydrogel” when dispersed in water already at relatively low concentrations (1-2 wt-%). A characteristic feature of the NFC is its shear thinning behaviour in aqueous dispersion, which is seen as a decrease in viscosity with increasing shear rate. Further, a “threshold” shear stress must be exceeded before the material starts to flow readily. This critical shear stress is often called the yield stress. The viscosity of the NFC can be best characterized by zero-shear viscosity, which corresponds to the “plateau” of constant viscosity at small shearing stresses approaching zero.

(19) Disintegration Treatment

(20) In this application, the term “disintegration treatment” or “fibrillation” generally refers to comminuting material mechanically by work applied to the particles, which work may be based on various effects, like grinding, crushing or shearing, or a combination of these, or another corresponding action that reduces the particle size. The energy taken by the refining work is normally expressed in terms of energy per processed raw material quantity, in units of e.g. kWh/kg, MWh/ton, or units proportional to these.

(21) The disintegration treatment is performed at a high consistency for the mixture of fibre raw material and water, the fibre suspension. Hereinbelow, the term pulp will also be used for the mixture of fibre raw material and water subjected to the disintegration treatment. The fibre raw material undergoing such treatment may refer to whole fibres, parts separated from them, fibril bundles, or fibrils, and typically the pulp is a mixture of such elements, in which the ratios between the components are dependent on the treatment stage, for example number of runs or “passes” through the treatment of the same batch of fibre material.

(22) Particularly in the case presented in this application, the “disintegration treatment” or “fibrillation” takes place by means of impact energy utilizing a series of frequently repeated impacts. These impacts have varying directions of action because of the construction of the device where the disintegration treatment is performed.

(23) The device shown in FIG. 1 is preferably used in the disintegration treatment where the chemically modified fibre material at high consistency is subjected to repeated impacts at high frequency. The device comprises several counter-rotating rotors R1, R2, R3 . . . placed concentrically within each other so that they rotate around a common rotation axis RA. The device comprises a series of rotors R1, R3 . . . rotating in the same direction, and rotors R2, R4 . . . rotating in the opposite direction, wherein the rotors are arranged pairwise so that one rotor is always followed and/or preceded in the radial direction by a counter-rotating rotor. The rotors R1, R3 . . . rotating in the same direction are connected to the same mechanical rotating means 5. The rotors R2, R4 . . . rotating in the opposite direction are also connected to the same mechanical rotating means 4 but rotating in a direction opposite to the direction of the aforementioned means. Both rotating means 4, 5 are connected to their own drive shaft which is introduced from below. The drive shafts can be located concentrically with respect to the rotation axis RA, for example in such a way that the outer drive shaft is connected to a lower rotating means 4, and the inner drive shaft placed inside it and rotating freely with respect to it, is connected to an upper rotating means 5.

(24) The figure does not show the fixed housing for the device, inside which the rotors are placed to rotate. The housing comprises an inlet, through which material can be supplied from above to the inside of the innermost rotor R1, and an outlet located by the side, oriented approximately tangentially outwards with respect to the peripheries of the rotors. The housing also comprises through-holes for the drive shafts down below.

(25) In practice, the rotors consist of vanes or blades 1 placed at given intervals on the periphery of a circle whose geometric centre is the rotation axis RA, and extending radially. In the same rotor, flow-through passages 2 are formed between the vanes 1, through which passages the material to be refined can flow radially outwards. Between two successive rotors R1, R2; R2, R3; R3, R4; etc., several blade spaces or gaps are formed repeatedly and at a high frequency during the rotary movement of the rotors in the opposite direction. In FIG. 2, reference numeral 3 denotes such blade gaps between the blades 1 of the fourth and fifth rotors R4, R5 in the radial direction. The blades 1 of the same rotor form narrow gaps, i.e. blade gaps 3, with the blades 1 of the preceding rotor (having the narrower radius on the periphery of the circle) in the radial direction and with the blades 1 of the next rotor (placed on the periphery of the circle with the greater radius) in the radial direction. In a corresponding manner, a large number of changes in the impact direction are formed between two successive rotors when the blades of the first rotor rotate in a first direction along the periphery of the circle, and the blades of the next rotor rotate in the opposite direction along the periphery of a concentric circle.

(26) The first series of rotors R1, R3, R5 is mounted on the same mechanical rotating means 5 that consists of a horizontal lower disc and a horizontal upper disc, connected to each other by the blades 1 of the first rotor R1, innermost in the radial direction. On the upper disc, in turn, are mounted the blades 1 of the other rotors R3, R4 of this first series, with the blades 1 extending downwards. In this series, the blades 1 of the same rotor, except for the innermost rotor R1, are further connected at their lower end by a connecting ring. The second series of rotors R2, R4, R6 is mounted on the second mechanical rotating means 4 which is a horizontal disc placed underneath said lower disc, and to which the blades 1 of the rotors of the series are connected, to extend upwards. In this series, the blades 1 of the same rotor are connected at their upper end by a connecting ring. Said connecting rings are concentric with the rotation axis RA. The lower discs are further arranged concentrically by an annular groove and a matching annular protrusion on the facing surfaces of the discs, also placed concentrically with the rotation axis RA and being equally spaced from it.

(27) FIG. 1 shows that the vanes or blades 1 are elongated pieces parallel to the rotation axis R1 and having a height greater than the width l (the dimension in the radial direction). In the horizontal section, the blades are quadrangular, in FIG. 2 rectangular. The fibre material is passed crosswise to the longitudinal direction of the blades, from the centre outwards, and the edges at the sides of the surfaces facing the radial direction in the blades 1 form long and narrow blade gaps 3 extending in the longitudinal direction of the blade, with the corresponding edges of the blades 1 of the second rotor.

(28) The rotors R1, R2, R3 . . . are thus, in a way, through-flow rotors in the shape of concentric bodies of revolution with respect to the rotation axis, wherein their part that processes the fibre material consists of elongated vanes or blades 1 extending in the direction of the rotation axis RA, and of flow-through passages 2 left therebetween.

(29) FIG. 1 also shows that the heights h1, h2, h3 . . . of the rotor blades 1 increase gradually from the first, i.e. the innermost rotor R1 outwards. As a result, the heights of the flow-through passages 2 limited by the rotor blades 1 also increase in the same direction. In practice, this means that when the cross-sectional area of the radial flow increases outwards as the peripheral length of the rotors increases, the increase in the height also increases this cross-sectional area. Consequently, the travel speed of a single fibre is decelerated in outward direction, if the volume flow is considered to be constant.

(30) By the centrifugal force caused by the rotational movement of the rotors, the material to be processed is passed through the rotors with a given retention time.

(31) As can be easily concluded from FIG. 2, during a single whole rotation of a pair of rotors (from a position in which given blades 1 are aligned, to the position in which the same blades 1 are aligned again), several blade gaps 3 are formed when successive blades 1 in the peripheral direction encounter successive blades 1 of the second rotor. As a result, the material transferred through the passages 2 outward in the radial direction is continuously subjected to shear and impact forces in the blade gaps 3 between different rotors and in the flow-through passages 2 between the blades 1 on the periphery of the rotor, when the material is passed from the range of the rotor to the range of an outer rotor, while the movement of the blades in peripheral direction and the directional changes of the movement caused by the rotors rotating in different directions prevent the through-flow of the material too fast out through the rotors by the effect of the centrifugal force.

(32) Blade gaps 3 and, correspondingly, encounters of blades 1 and respective changes in the impact directions in two rotors successive in the radial direction are generated at a frequency of [1/s] which is 2×f.sub.r×n.sub.1×n.sub.2, where n.sub.1 is the number of blades 1 on the periphery of the first rotor, n.sub.2 is the number of blades on the periphery of the second rotor, and f.sub.r is the rotational speed in revolutions per second. The coefficient 2 is due to the fact that the rotors rotate at the same rotational speed in opposite directions. More generally, the formula has the form (f.sub.r(1)+f.sub.r(2))×n.sub.1×n.sub.2, where f.sub.r(1) is the rotational speed of the first rotor and f.sub.r(2) is the rotational speed of the second rotor in the opposite direction.

(33) Furthermore, FIG. 2 shows how the number of blades 1 may be different in different rotors. In the figure, the number of blades 1 per rotor increases starting from the innermost rotor, except for the last rotor R6 where it is smaller than in the preceding rotor R5. As the rotational speeds (rpm) are equal irrespective of the location and direction of rotation of the rotor, this means that the frequency at which the blades 3 pass a given point and, correspondingly, the frequency of formation of the blade gaps 3 increases from the inside outwards in the radial direction of the device.

(34) In FIG. 1, the dimension l of the blades in the direction of the radius r is 15 mm, and the dimension e of the blade gap 3 in the same direction is 1.5 mm. Said values may vary, for example from 10 to 20 mm and from 1.0 to 2.0 mm, respectively. The dimensions are influenced by, for example, the consistency of the fibre material to be treated.

(35) The diameter d of the device, calculated from the outer rim of the outermost rotor R6, can vary according to the capacity desired. In FIG. 1, the diameter is 500 mm, but the diameter can also be greater, for example greater than 800 mm. When the diameter is increased, the production capacity increases in a greater proportion than the ratio of the diameters.

(36) It has been found that a decrease in the rotation speed of the rotors impairs fibrillation. Similarly, a decrease in the flow rate (production) clearly improves fibrillation; in other words, the greater the retention time of the material to be processed during which it is subjected to the impact and shear forces of the blades i.e. ribs, the better the fibrillation result.

(37) The cellulose-based fibre material of sufficient modification degree can also be processed to nanofibrillar cellulose at high consistencies with other devices that cause repeated impacts by fast moving successive elongated elements. Such devices include medium-consistency and high-consistency refiners (MC refiners, HC refiners) and the processes are medium-consistency and high-consistency refining, respectively. In these types of refiners fast moving elements are bars on the opposite refining surfaces and the fibrillation takes place in gaps formed between the bars during bar crossings (as the opposite bars pass each other), due to the relative rotation movement of the opposite refining surfaces (rotor and stator). Conical refiners and disc refiners are common types of such refiners.

(38) In the above described process, the fibre material to be processed for producing nanofibril cellulose is a mixture of water and cellulose based fibres which have been separated from each other in the preceding manufacturing processes of mechanical pulp or chemical pulp, where the starting material is preferably wood raw material. In the manufacture of nanofibrillar cellulose, it is also possible to use cellulose fibres from other plants, where cellulose fibrils are separable from the fibre structure. The fibres obtained from any of the above-mentioned sources are then subjected to the chemical modification. A suitable consistency of the high-consistency pulp to be fibrillated is over 10 wt-%, preferably at least 15 wt-%. The preferable consistency ranges are higher than 10 wt-% and 50 wt-% at the most, especially 15-50 wt-%, more preferably 15-40 wt-%, and most preferably 15-30 wt-%. The liquid medium where the fibre material is suspended to the desired consistency is preferably aqueous medium. It is also possible that the material is fibre material that has already passed the same process once or more times, and from which fibrils have already been separated. When the material is already partly fibrillated as a result of the preceding processing runs, it tends to become more or less “sticky”, but it can still be treated at the same high consistency or concentration in the device because of the robust structure of the device which is not sensitive to the material properties.

(39) Fibre material at a given consistency in water is supplied in the above-described way through the rotors R1, R2, R3 . . . until it has reached the desired degree of fibrillation, which can be seen as viscosity values and shear-thinning behaviour typical of nanofibrillar cellulose when the product is diluted to form a gel. If necessary, the processing is repeated once or several times by running the material through the rotors again, or through another similar series of rotors, wherein the device comprising two or more of the above described sets of rotors can be coupled in series.

(40) As the final result, the product obtained after several refining runs exists as moist powdery material where the fibrils of the nanofibrillar cellulose are gathered to moist particles or granules which can be distinguished visually. The particle size is 0.1-1 mm. These particles can be aggregated to larger granular aggregates due to the stickiness of the moist particles, depending on the moisture of the product. The number-based median diameter (d50) of the particles is 100-1000 μm, preferably 150-500 μm, as gently dispersed in water to separate the particles and measured by laser-diffraction particle-size analyzer. The product is also characterized by the same chemical structure and degree of modification of the cellulose as the fibre material used as the starting material, which can be expressed as amount of chemical groups or equivalents/g nanofibrillar cellulose (dry matter) or as degree of substitution (DS). The product after the disintegration of the pulp can be dried further, or packed as such, that is, at the water content at which it exits the disintegration treatment.

(41) By the above-presented method, it is possible to obtain nanofibrillar cellulose product, in which the viscosity of an aqueous dispersion made of the product increases as a function of the specific energy (energy consumption), that is, as the specific energy used for the fibrillation increases. Consequently, the viscosity of the diluted product and the specific energy used in the method have a positive correlation. It has also been found that nanofibrillar cellulose can be obtained, whereby the turbidity and the content of fibre particles reduces as a function of specific energy (energy consumption).

(42) Typically in the method, the aim is to obtain, as the final product, nanofibrillar cellulose product whose Brookfield viscosity, measured at a consistency of 0.8% (10 rpm), is at least 5,000 mPa.Math.s, for example between 5,000 and 20,000 mPa.Math.s. In addition to the high viscosity, the aqueous nanofibrillar cellulose dispersions obtained by diluting the product are also characterized by so-called shear thinning; that is, the viscosity decreases as the shear rate increases.

(43) Furthermore, the aim is to obtain nanofibrillar cellulose whose turbidity is typically lower than 80 NTU, advantageously from 10 to 60 NTU, at a consistency of 0.1 wt-% (aqueous medium), measured by nephelometry.

(44) Furthermore, the aim is obtain shear thinning nanofibril cellulose having a zero shear viscosity (“plateau” of constant viscosity at small shearing stresses) in the range of 1,000 to 50,000 Pa.Math.s and a yield stress (shear stress where shear thinning begins) in the range of 1 to 50 Pa, advantageously in the range of 3 to 20 Pa, preferably 6-15 Pa, measured at a consistency of 0.5 wt-% (aqueous medium).

EXAMPLES

(45) In the following, the method is described by some examples which do not restrict the method.

Examples—Production of Nanofibrillar Cellulose in High Consistency

(46) Cellulose birch pulp was anionically modified by “TEMPO” oxidation. Two modification levels: 0.77 mmol COOH/g pulp (22% dry solids) and 1.07 mmol COOH/g pulp (18% dry solids). The carboxylate content was determined by conductometric titration.

Reference Example (REF)

(47) The anionic pulp (1.07 mmol COOH/g pulp) was dispersed to water to form 2.5% (w/w) dispersion. The dispersion was fed into a homogenizer (GEA Niro Soavi Panther) at 600 bar. As a result, viscous nanofibrillar cellulose gel was formed.

Comparative Example

(48) Anionic pulp (0.77 mmol COOH/g) in high consistency (starting consistency 22%) was run 3 times through a disperser (Atrex), through its series of counter-rotating rotors. The disperser used had a diameter of 850 mm and rotation speed used was 1800 rpm. As a result, moist cellulose powder-like product was obtained.

Example 1

(49) Anionic pulp (1.07 mmol COOH/g) in high consistency (starting consistency 18%) was run 3 times through a disperser (Atrex), through its series of counter-rotating rotors. The disperser used had a diameter of 850 mm and rotation speed used was 1800 rpm. As a result, moist cellulose powder-like product was obtained.

Example 2

(50) Anionic pulp (1.07 mmol COOH/g) in high consistency (starting consistency 18%) was run 3 times through a disperser (Atrex), through its series of counter-rotating rotors. The disperser used had a diameter of 850 mm and rotation speed used was 1800 rpm. After that, formed cellulose powder was dispersed to water to form 3.0% (w/w) dispersion. The dispersion was run 1 pass through the Atrex device. As a result, viscous nanofibrillar cellulose gel was formed.

(51) To verify the success of fibrillation, rheological measurements of the product in the form of nanofibrillar cellulose hydrogels were carried out with a stress controlled rotational rheometer (ARG2, TA instruments, UK) equipped with four-bladed vane geometry. Samples were diluted with deionised water (200 g) to a concentration of 0.5 w % and mixed with Waring Blender (LB20E*, 0.5 L) 4×10 sec (20 000 rpm) with short break between the mixing. Rheometer measurement was made for the sample. The diameters of the cylindrical sample cup and the vane were 30 mm and 28 mm, respectively, and the length was 42 mm. The steady state viscosity of the hydrogels was measured using a gradually increasing shear stress of 0.001-1000 Pa. After loading the samples to the rheometer they are allowed to rest for 5 min before the measurement is started. The steady state viscosity is measured with a gradually increasing shear stress (proportional to applied torque) and the shear rate (proportional to angular velocity) is measured. The reported viscosity (=shear stress/shear rate) at a certain shear stress is recorded after reaching a constant shear rate or after a maximum time of 2 min. The measurement is stopped when a shear rate of 1000 s−1 is exceeded. The method is used for determining zero-shear viscosity.

(52) Viscosity as a function of shear stress for the four nanofibrillar cellulose product samples in 0.5% dilution are presented in FIG. 3. As can be seen from the results, the sample with high degree of modification, where the carboxylate group content was above 1.00 mmol COOH/g pulp (1.07 mmol COOH/g) reached even higher zero-shear viscosity values (over 2000 Pa.Math.s) as the reference which was prepared at low consistency (2.5%), whereas the sample with lower degree of modification (carboxylate content below 0.8 mmol/g pulp) had very low viscosity values with no distinguishable yield point (yield stress value).

(53) Particle Size

(54) Particle size of moist cellulose powder of Example 1 was measured by Beckman Coulter LS320 (laser-diffraction particle size analyzer). 4 g of the powder was dispersed to 500 ml of water with hand mixer. Particles were fed into particle analyser until there were enough particles in a circulation. Water was used as a background liquid. Coulter LS Particle size Median diameter, 292 μm was measured. (Note: due to high solid fibrillation, nanofibrils are in the form of aggregated granules. For particle size analysis, these aggregated granules are dispersed by gentle mixing only; to make nanofibrillar cellulose for rheological measurement and before the use, powerful dispergation is needed.

(55) Turbidity

(56) Turbidity of samples was measured at 0.1 wt-% by nephelometry.

(57) In the method, a nanofibrillar cellulose sample is diluted in water, to the measuring concentration of 0.1 wt-%. HACH P2100 Turbidometer with a 50 ml measuring vessel is used for turbidity measurements. The dry matter of the nanofibrillar cellulose sample is determined and 0.5 g of the sample, calculated as dry matter, is loaded in the measuring vessel, which is filled with tap water to 500 g and vigorously mixed by shaking for about 30 s. Without delay the aqueous mixture is divided into 5 measuring vessels, which are inserted in the turbidometer. Three measurements on each vessel are carried out. The mean value and standard deviation are calculated from the obtained results, and the final result is given as NTU units (nephelometric turbidity units). The characteristics of the samples obtained from the examples 1 and 2 were as follows:

Example 1 24 NTU

Example 2 19 NTU

(58) Thanks to its rheological properties, fibril strength properties, as well as the translucency of the products made from it, the nanofibril cellulose obtained by the method can be applied in many uses, for example as a rheological modifier and a viscosity regulator, and as elements in different structures, for example as a reinforcement. Nanofibril cellulose can be used, among other things, in oil fields as a rheological modifier and a sealing agent. Similarly, nanofibril cellulose can be used as an additive in various medical and cosmetic products, as reinforcement in composite materials, and as an ingredient in paper products. This list is not intended to be exhaustive, but nanofibril cellulose can also be applied in other uses, if it is found to have properties suitable for them.