Highly potent granules obtained by continuous melt granulation

Abstract

The present invention relates to water-soluble or water-dispersible granules comprising a binder, a filler and an active ingredient. The preferred granules of the present invention are obtained by continuous melt granulation of a mixture comprising 65-70% by weight of the active ingredient, 15-25% by weight of the filler and 5-15% by weight of the binder, based on the total weight of the mixture. Ascorbic acid and its edible salts are the preferred active ingredients.

Description

Detailed Description of the Invention

[0001] [Technical field] The present invention relates to edible water-dispersible powders.

[0002] [Background of the invention] Granulation is a size-enlarging process. Granulation is often carried out by wet granulation, which uses a solvent (water or organic solvent) to initiate bonding between solid particles (e.g., microcapsules). In Examples 9 and 13 of U.S. Pat. No. 4,203,997, a mixture containing 90 parts ascorbic acid is wetted with 8 parts water, then passed through a press, dried, and milled.

[0003] The disadvantage of wet granulation is the need to remove the solvent at the end of the granulation process. In the case of using water as the solvent, a significant amount of energy is required to distill off the water. A further disadvantage of wet granulation is the risk of hydrolysis of the active ingredient. In the case of organic solvents, potentially harmful residues and / or adverse effects on the environment are of concern.

[0004] Dry granulation and melt granulation are known alternatives to wet granulation. Melt granulation works on a similar principle to wet granulation, but uses a molten binder as the granulation fluid to establish liquid bridges between the particles to be granulated. Upon cooling to room temperature, the binder solidifies and forms bridges between the individual powder particles, resulting in a solid final product with a granular structure.

[0005] In most cases, melt granulation is carried out as a batch process, for example in a heated powder bed. Example 1 of WO 2006 / 082499 discloses a batch process in which the mixture is granulated in a Bohle tumbling mixer. The processing of successive batches has to wait until the ongoing batch is completed. This is the main drawback of batch processing. In practice, batch processing results in the production of limited amounts of material.

[0006] The disadvantages of batch processing can be overcome by using a continuous process.

[0007] An example of a continuous process is hot melt extrusion. Hot melt extrusion processes produce solid solutions or solid dispersions. Thus, the particles produced by hot melt extrusion are not granular in the sense that crosslinks between individual powder particles can be seen. Chang et al. disclose a hot melt extrusion process using an extruder with a die head with a die diameter of 3 mm (Dawei Chang et al., "Ascorbic acid encapsulation in a glassy carbohydrate matrix via hot melt extrusion: Preparation and characterization," Food Sci. Technol, Campinas, 39(3):660-666, July-Sept. 2019). The extrudate leaving the die is then ground into a powder (Chang et al., section 2.13). In fact, a drawback of hot melt extrusion is that the extruded strands, upon exiting the die, require cutting, grinding, or other types of comminution. Unacceptably high die head pressures and difficult downstream processing are other drawbacks inherent to hot melt extrusion.

[0008] There is a need for a continuous granulation process that does not have the above mentioned drawbacks. It should be a solvent-free process. The processing temperature should be relatively low. The amount of fines (i.e. non-granulated residues) generated during the process should be low. The granules obtained by the required granulation process should be edible, should have high potency, should have good flow properties and should be water soluble or at least water dispersible.

[0009] [Summary of the Invention] The problem underlying the present invention is solved by continuous melt granulation of the mixture of the present invention. The granules of the present invention comprise or consist of the mixture of the present invention. The present invention also relates to the use of the mixture disclosed herein for continuous melt granulation.

[0010] The mixture of the present invention comprises at least one active ingredient, at least one filler and at least one binder. A preferred mixture comprises at least one polysaccharide (as filler), at least one sugar alcohol (as binder) and ascorbic acid or an edible salt thereof (as active ingredient), the melting temperature of said at least one sugar alcohol being lower than the melting temperature of said at least one polysaccharide.

[0011] The mixture of the present invention is suitable for solvent-free continuous melt granulation. Therefore, the mixture of the present invention is a dry mixture, preferably containing less than 5% by weight of water, based on the total weight of the mixture.

[0012] The mixtures of the present invention are suitable for producing high potency granules by continuous melt granulation. Thus, preferred mixtures of the present invention contain at least 50% by weight of the active ingredient, based on the total weight of the mixture.

[0013] The mixture of the present invention preferably comprises at least 10% by weight of a filler, based on the total weight of the mixture. The most preferred filler is inulin, while the most preferred binder is sorbitol.

[0014] The mixture of the present invention is suitable for continuous melt granulation at relatively low temperatures. When the weight ratio of the filler to the binder is between 4:1 and 1:1, the continuous melt granulation can be carried out at surprisingly low temperatures: preferably below 180°C, more preferably below 110°C, and most preferably below 100°C.

[0015] The process of the invention is a process for producing granules, in which the mixture of the invention is fed into an extruder, preferably having at least one kneading zone.

[0016] The extrusion granulation described herein is carried out in an extruder without a die. In performing continuous melt granulation, a co-rotating twin screw extruder continuously mass produces free-flowing granules (see Figure 1 in N. Kittikunakorn et al., "Twin-screw melt granulation: Current progress and challenges," International Journal of Pharmaceutics, 588, (2020), 119670). Neither a drying step nor a chopping / grinding step is required.

[0017] [Detailed Description of the Invention] The granules of the present invention can be obtained by continuous melt granulation of a dry edible mixture comprising primary particles and at least two edible excipients. During continuous melt granulation, the primary particles are agglomerated. Thus, the granules of the present invention are preferably units formed of a large number of particles. The primary particles of the granules are smaller than the granules.

[0018] Both edible excipients are preferably water-soluble or water-dispersible. The melting temperature of the first edible excipient is low enough to melt or at least soften during continuous melt granulation. When melted or softened, the first edible excipient establishes crosslinks between primary particles. The crosslinks then solidify at room temperature. Thus, the first edible excipient acts mainly as a binder. In the most preferred embodiment of the present invention, the first edible excipient is sorbitol.

[0019] The melting temperature of the second edible excipient is relatively high. The second edible excipient mainly acts as a filler. In the most preferred embodiment, the second edible excipient is inulin.

[0020] The granule of the present invention may contain only one type of primary particle or may contain multiple types of primary particles. The primary particle of the granule of the present invention preferably contains or consists of an active ingredient. An example of a primary particle is vitamin C crystal. Thereby, vitamin C can be ascorbic acid, an edible salt of ascorbic acid or an edible water-soluble ascorbic acid ester.

[0021] The granules of the present invention are preferably water-soluble or water-dispersible. A composition comprising or consisting of such granules is suitable for preparing a beverage. One embodiment of the present invention relates to a beverage obtained by dissolving or dispersing a composition comprising the granules described herein.

[0022] [Filler of the present invention] Fillers are excipients used to increase the volume of the granules of the present invention. Fillers can have additional functions. Some fillers (e.g., dietary fiber) also have health benefits.

[0023] The granules of the present invention are intended for edible use, therefore toxic and non-edible fillers are generally excluded.

[0024] The granules of the present invention are preferably water-soluble or water-dispersible. Thus, fillers having a solubility of less than 1 g / 100 mL water, or less than 0.5 g / 100 mL water, or less than 0.1 g / 100 mL water are not preferred.

[0025] Usually, the melting temperature of the filler is higher than that of the binder. However, this does not exclude the possibility that the filler may also be melted or softened during continuous melt granulation. The melting temperature of the filler is preferably at least 150°C, more preferably at least 155°C, and most preferably at least 160°C, and is preferably 151°C to 240°C, more preferably 160°C to 240°C, and most preferably 180°C to 200°C.

[0026] In the context of the present invention, the bulking agent is preferably a polysaccharide, more preferably a polysaccharide produced by plants, even more preferably a dietary fiber, and most preferably inulin. Examples of alternative bulking agents are human milk oligosaccharides (HMO) and mannitol. 2'-fucosyllactose (2'-FL) is a preferred HMO. An even more preferred bulking agent is a mixture that includes 2'-fucosyllactose and difucosyllactose (DFL).

[0027] [Binder of the present invention] Binders are excipients used to hold the components of a formulation together. To do so, they are melted or softened during continuous melt granulation. Usually, the melting temperature of the binder is lower than that of the filler and often lower than that of any added active ingredient. The melting temperature of the binder is preferably less than 140°C, more preferably less than 130°C, even more preferably less than 120°C, and most preferably less than 110°C. The melting temperature of the binder is preferably between 50°C and 110°C, more preferably between 60°C and 100°C, and most preferably between 70°C and 100°C.

[0028] The granules of the present invention are preferably water-soluble or water-dispersible. Thus, binders with a solubility of less than 1 g per 100 mL of water, or less than 0.5 g per 100 mL of water, or less than 0.1 g per 100 mL of water are not preferred. Possible binders are, inter alia, ribose (such as D-ribose), polyethylene glycol, sorbitol and xylitol. In the context of the present invention, the binder is preferably a polyol, more preferably a sugar alcohol, even more preferably sorbitol or ribose (such as D-ribose), and most preferably sorbitol, which preferably has a melting temperature of 98°C or less. Such sorbitol is commercially available under the trademark Roquette. Sorbitol is a stereoisomer of mannitol.

[0029] [Active ingredient of the present invention] The mixture of the present invention comprises at least one active ingredient.In the context of the present invention, water-soluble and water-dispersible active ingredients are preferred.Water-soluble and water-dispersible vitamins (such as vitamin C, vitamin B1, vitamin B2, vitamin B3, vitamin B6 and vitamin B12) are examples of water-soluble or water-dispersible active ingredients.In one embodiment of the present invention, the active ingredient is a micronutrient, preferably a water-soluble micronutrient, and even more preferably a water-soluble vitamin.

[0030] In a preferred embodiment, the active ingredient of the present invention is vitamin C. The term "vitamin C" may thereby refer to ascorbic acid, edible salts of ascorbic acid or edible esters of ascorbic acid. Fat-soluble esters of ascorbic acid are preferably excluded. A preferred mixture of the present invention comprises ascorbic acid particles. Such particles may be crystalline and / or amorphous. Ascorbic acid particles are commercially available from DSM® Nutritional Products, Switzerland.

[0031] [Mixture of the present invention] The mixture of the present invention is suitable for continuous melt granulation. When performing continuous melt granulation, the mixture of the present invention is fed into an extruder or any other suitable device.

[0032] In contrast to wet granulation, no solvent is required when carrying out continuous melt granulation.Thus, the mixture of the present invention preferably contains less than 10% by weight, more preferably less than 8% by weight, even more preferably less than 5% by weight, and most preferably less than 3% by weight of solvent, based on the total weight of the mixture.This is particularly true, but not exclusively, when the solvent is water.Thus, the preferred mixture of the present invention preferably contains less than 10% by weight, more preferably less than 8% by weight, even more preferably less than 5% by weight, and most preferably less than 3% by weight of water, based on the total weight of the mixture.In the most preferred embodiment, the mixture of the present invention contains only residual moisture.

[0033] A preferred mixture of the present invention is At least one active ingredient at least one edible filler, preferably water-soluble or water-dispersible at least one edible binder, which is preferably water-soluble or water-dispersible, and Possibly residual moisture It comprises or consists of.

[0034] The binders and fillers of the present invention are edible excipients. The mixture of the present invention preferably comprises 20-40% by weight, and more preferably 25-30% by weight, of edible excipients, based on the total weight of the mixture.

[0035] A mixture containing a high concentration of active ingredient is suitable for producing granules with high efficacy. In one embodiment, the mixture of the present invention contains at least 50% by weight, preferably at least 55% by weight, more preferably at least 60% by weight, even more preferably at least 65% by weight, and most preferably at least 70% by weight of active ingredient, based on the total weight of the mixture. With regard to the active ingredient, the above-mentioned priorities apply. Thus, a preferred mixture of the present invention contains at least 50% by weight of water-soluble or water-dispersible vitamin, based on the total weight of the filler, binder, and mixture. A more preferred embodiment of the present invention relates to a mixture composed of a filler, binder, and 50-80% by weight, preferably 65-75% by weight, of ascorbic acid, based on the total weight of the mixture. However, the active ingredient of the present invention is not limited to ascorbic acid. Exemplary alternative active ingredients are listed above. Thus, a preferred embodiment of the present invention also relates to a mixture composed of a filler, binder, and 50-80% by weight of water-soluble or water-dispersible vitamin, based on the total weight of the mixture.

[0036] Fillers are necessary to increase the size: they increase the volume of the granules of the invention. The mixture of the invention preferably comprises at least 10% by weight of fillers, based on the total weight of the mixture. In one embodiment, the mixture of the invention preferably comprises 10% to 40% by weight, more preferably 15% to 25% by weight, and most preferably 20% to 25% by weight, based on the total weight of the mixture, of at least one filler. With regard to the fillers, the above-mentioned priorities apply. Thus, the mixture of the invention preferably comprises at least 10% by weight, based on the total weight of the mixture, of dietary fiber, said dietary fiber being preferably inulin. The mixture of the invention comprises several fillers. However, the invention preferably comprises only one filler. A particularly preferred mixture of the invention comprises crystalline ascorbic acid, a binder, and 10 to 40% by weight, based on the total weight of the mixture, of inulin.

[0037] Usually, the mixture of the invention contains less binder than filler. The weight ratio of filler to binder is preferably 4:1 to 1:1, more preferably 3:1 to 1:1, even more preferably 2:1 to 1:1, and most preferably 2:1. Thereby, the mixture of the invention contains preferably 5% to 15% by weight, more preferably 6% to 14% by weight, and most preferably 8% to 13% by weight of at least one binder, based on the total weight of the mixture. With regard to the binder, the above-mentioned preferences apply. Thus, the mixture of the invention contains preferably 5% to 15% by weight, more preferably 6% to 14% by weight, and most preferably 8% to 13% by weight of at least one polyol, based on the total weight of the mixture. Particularly preferred mixtures of the invention contain inulin and sugar alcohol in a weight ratio of preferably 4:1 to 1:1, more preferably 3:1 to 1:1, even more preferably 2:1 to 1:1, and most preferably 2:1. Sorbitol and ribose are the preferred sugar alcohols.

[0038] [Granules of the present invention] Preferred granules can be obtained by continuous melt granulation (i.e. without solvent) of the mixture of the invention, preferably using a twin-screw extruder. Thus, the granules of the invention comprise or consist of the mixture of the invention.

[0039] The mixture of the present invention comprises primary particles. During continuous melt granulation, bridges are formed between the primary particles of the mixture. Thus, the granules of the present invention are larger than the size of the primary particles. The preferred granules of the present invention have a mass median particle size D50 (volume basis) of 0.5 mm to 6 mm, more preferably 1 mm to 5 mm, even more preferably 1.5 mm to 4.5 mm, and most preferably 2 mm to 4 mm, measured using dynamic image analysis. In the case of crystals consisting of an active ingredient, the granules of the present invention may contain more than 100, more than 1000, more than 5000, or even more than 10000 crystals.

[0040] Each granule may contain various kinds of active ingredients. In a preferred embodiment, however, the granule of the present invention contains only one active ingredient. In one embodiment, the granule of the present invention contains vitamin C, vitamin B1, vitamin B2, vitamin B3, vitamin B6 or vitamin B12. Usually, the granule of the present invention contains less than 1% by weight of fat-soluble active ingredients based on the total weight of the mixture, and preferably does not contain fat-soluble active ingredients.

[0041] In one embodiment, the granules of the present invention comprise a filler, a binder and at least one active ingredient, the mixture comprises at least 50% by weight of the active ingredient, based on the total weight of the mixture; and The mixture comprises at least 10 wt. % of a filler, based on the total weight of the mixture; and The melting temperature of the active ingredient is higher than the melting temperature of the binder, and The melting temperature of the binder is lower than the melting temperature of the filler, and The mixture contains less than 5% by weight of water, based on the total weight of the mixture.

[0042] The granules of the present invention are preferably water-soluble or water-dispersible. This can be achieved by selecting a binder that is water-soluble or water-dispersible, by selecting a filler that is water-soluble or water-dispersible, and by selecting an active ingredient that is water-soluble and / or water-dispersible.

[0043] [Method of Invention] The method of the present invention is continuous melt granulation, and preferably continuous twin-screw melt granulation. The differences between batch melt granulation and continuous twin-screw melt granulation are listed in Table 1 of N. Kittikunakorn et al., "Twin-screw melt granulation: current progress and challenges," International Journal of Pharmaceutics, 588, (2020), 119670. In a preferred embodiment of the present invention, the dry, powder mixture disclosed herein is fed into an extruder suitable for continuous melt granulation. Thereby, a volumetric powder feeder is not preferred. In a preferred method of the present invention, the mixture of the present invention is fed into an extruder described herein using a gravimetric powder feeder. The gravimetric powder feeder provides a controlled and consistent feeding process while taking into account changes in powder properties over time and process deviations.

[0044] In the process of the invention, a twin screw extruder is preferably used. Twin screw extruders with co-rotating screws are particularly preferred. The co-rotating screws of the preferred extruders are modular and can be configured in different setups, resulting in different zones. The purpose of the first zone near the inlet of the extruder is transport. The transport zone is often called the conveying zone. It is also possible that there is one or more kneading zones. The kneading zone is usually located between two conveying zones, and there is preferably a shaping zone at the outlet of the extruder.

[0045] In most cases, each zone has different screw elements. The conveying zone has conveying elements that transport the material towards the exit of the granulator [see section 2.1 in N. Kittikunakorn et al., "Twin-screw melt granulation: current progress and challenges," International Journal of Pharmaceutics, 588, (2020), 119670]. The kneading zone has kneading elements, such as narrow or wide kneading disks. A typical forming zone has at least one size control element that minimizes the amount of oversized granules. An exemplary size control element is shown in Figure 1(f) of J. Vercruysse et al., "Impact of screw configuration on the particle size distribution of granules produced by twin screw granulation," International Journal of Pharmaceutics 479 (2015) 171-180. These size control elements are not knives used to cut the extruded strands. In fact, when performing continuous melt granulation, spaghetti-like strands are not extruded. Extruders that are suitable for continuous melt granulation do not have a die at the exit. The size controlling element is the screw element within the extruder.

[0046] Hot melt extrusion is different from continuous melt granulation as described herein. When performing hot melt extrusion, a strand having, for example, a cylindrical diameter is extruded through a die. The length of the strand is not limited (i.e. it can be unlimited). To obtain separated pellets, the strand obtained by hot melt extrusion must be chopped into pieces. The pellets obtained are not granules consisting of distinguishable primary particles. When performing hot melt extrusion, the chopping step can be performed at any time after extrusion, including directly at the extruder die. Dies with integrated knives are commercially available.

[0047] The above does not apply to the method of the present invention. When performing continuous melt granulation, strands are not extruded. Instead, granules are continuously mass-produced at the end of the extruder. Since no strands are produced, the knife / cutting step is not necessary, greatly simplifying the process. When performing continuous melt granulation, a die at the end of the extruder is not required. In a preferred embodiment of the present invention, the mixture of the present invention is fed into a twin-screw extruder that does not have a die and does not have a knife cutting device.

[0048] In the process of the invention, the screw configuration of the twin-screw extruder is usually selected so that the extruder has at least one kneading zone. Thus, the at least one kneading zone is preferably closer to the powder inlet of the extruder than the end of the extruder. The kneading zone comprises kneading elements. The kneading elements are preferably kneading disks as disclosed in US 2005 / 0041521. The kneading disks may be coincident or non-coincident and are preferably arranged at a stagger angle of 30° to 90°. A stagger angle of about 30° is preferred, as this limits the stress on the powder mixture. In the context of the present invention, "stagger angle" refers to the angle of vertex offset of two directly successive kneading disks, as explained in paragraph

[0007] of US 2005 / 0041521. By way of example, the expression "kneading disks are arranged at a stagger angle of 30°" means that the vertex offset angle of the successive kneading disks is 30°. There may be more than two consecutive kneading discs in the kneading zone of the extruder. Figure 2 of US 2005 / 0041521 shows a side view of a kneading zone with five consecutive kneading discs, the kneading discs being arranged at a staggered angle.

[0049] Temperature control is important when performing continuous melt granulation. In a preferred method of the present invention, the extruder has several zones that can be heated or cooled individually. When continuously melt granulating the mixture disclosed herein, the temperature zone close to the powder inlet of the extruder is usually heated. When selecting a suitable temperature, it is necessary to consider that the material in the extruder moves quite fast so that the contact between the material and the heating element is quite short. In some cases, therefore, it may be recommended to set the temperature of some zones of the extruder at a temperature higher than the melting temperature of the binder of the mixture.

[0050] In a preferred embodiment of the invention, the conveying zone and / or the kneading zone of the extruder are preferably heated to a temperature of from 80°C to 180°C, more preferably to a temperature of from 80°C to 110°C, and most preferably to a temperature of from 90°C to 100°C.

[0051] It is not preferable to mass produce hot granules. Hot granules may still be relatively soft and sticky. As a result, hot granules may form lumps. This should be avoided. Therefore, it is preferable to cool the material in the extruder before it is mass produced by the extruder. In a preferred embodiment of the present invention, at least one zone after the kneading zone is cooled to a temperature of less than 60°C, preferably less than 40°C, and most preferably less than 26°C.

[0052] [Example] [Comparative Example 1 (containing no filler)] In Example 1, a dry mix containing 90% by weight of active ingredient and 10% by weight of binder was continuously melt granulated (solvent-free) using a twin-screw extruder without a die. The dry mix in Example 1 did not contain any filler.

[0053] As an active ingredient, the dry mix of Example 1 contained fine ascorbic acid powder (available from DSM® Nutritional Products, Switzerland). Ascorbic acid is a chemically defined compound with the empirical formula C6H8O6 and a molecular weight of 176.13. The melting point of the active ingredient of Example 1 is approximately 190° C. (with decomposition).

[0054] As a binder, the dry mix of Example 1 contained a polyol (sorbitol, commercially available under the trademark Roquette®). The binder of Example 1 has a melting temperature of about 98° C.

[0055] The dry blend of Example 1 was fed into a ThermoFisher® Eurolab® extruder using a gravimetric loss-in-weight feeder at the powder inlet. The extruder had a length to diameter (L / D) ratio of 25 / 1 and a screw diameter of 16 mm. The co-rotating screws of the extruder were fully modular and could be configured in various setups. The extruder was divided into several zones that could be heated or cooled separately.

[0056] In Example 1, two extrusion runs were carried out using two temperature schemes. The temperature zones close to the powder inlet (zones 2, 3, and 4) were heated to a temperature of 160° C. (first run) or 185° C. (second run). The temperature of the zones close to the end of the extruder (zones 5 and 6) was kept at 25° C. Cooling the end of the extruder allows the binder to solidify early and prevents sticking of the granules coming out of the extruder.

[0057] In Example 1, the extruder had one kneading zone with three kneading disks arranged at a stagger angle of 30° (i.e., the angle of apex misalignment between any two immediately successive kneading disks was 30°).

[0058] In Example 1, it was found that ascorbic acid could not be processed by continuous melt granulation when using a binder as the only excipient at a concentration of 90% by weight: a large amount of fines was generated and the obtained granulated material had poor flow properties.

[0059] [Example 2 (10% by weight of filler)] In Example 2, the experiment of Example 1 was repeated using an extruder with one kneading zone with five kneading discs arranged at a staggered angle of 90°. In contrast to Example 2, however, a given amount of filler was added as a second excipient (i.e. in addition to the binder). The amount of active ingredient was reduced accordingly. As filler, inulin was used (Orafti® GR, average degree of polymerization ≥ 10, available from Beneo, Mannheim, Germany). The melting points of the fillers of Example 1 were measured in the range of 190-195°C. The fillers of Example 2 had a higher melting temperature than the binders of Example 2.

[0060] In Example 2, the amount of filler was 10% by weight based on the total weight of the dry mix: the weight ratio of filler to binder was 1: 1. The composition of the dry mix of Example 2 is shown below.

[0061] [Table 1]

[0062] Similar to Example 1, two extrusion runs were carried out in Example 2 using two different temperature schemes: the temperature zones close to the powder inlet (zones 2, 3, and 4) were heated to a temperature of 160° C. (first run) or 185° C. (second run).

[0063] In Example 2, it was found that ascorbic acid could be processed by continuous melt granulation using additional excipients (in addition to fillers and binders) at a concentration of 80% by weight. However, a large amount of fines was generated and the obtained granulated material had relatively poor flow properties.

[0064] [Example 3 (40% by weight of filler)] In Example 3, the experiment of Example 2 was repeated using an extruder with one kneading zone with three kneading discs arranged at a staggered angle of 30°. In contrast to Example 2, however, the amount of filler was increased. More specifically, the amount of filler was increased from 10% to 40% by weight, but the amount of active ingredient was reduced accordingly.

[0065] In Example 3, the weight ratio of filler to binder was 4: 1. The composition of the dry mix for Example 3 is shown below.

[0066] [Table 2]

[0067] Similar to Examples 1 and 2, two extrusion runs were carried out in Example 3 using two different temperature schemes: the temperature zones close to the powder inlet (zones 2, 3, and 4) were heated to a temperature of 109° C. (first run) or 95° C. (second run).

[0068] At a temperature of 109° C. (first attempt), good quality granules were obtained, which is significantly lower than the temperatures applied in Example 2 (160° C. and 185° C., respectively). However, at a temperature of 95° C. (second attempt), the quality of the obtained granules was significantly reduced.

[0069] [Example 4 (20% by weight of filler)] In Example 4, the experiment of Example 3 was repeated, except that the amount of filler was reduced from 40% to 20% by weight, and the amount of active ingredient was increased accordingly.

[0070] In Example 4, the weight ratio of filler to binder was 2:1. The composition of the dry mix for Example 4 is shown below.

[0071] [Table 3]

[0072] In Example 4, the temperature zones close to the powder inlet of the extruder (zones 2, 3, and 4) were heated to a temperature of only 94° C. Despite this relatively low temperature, and in contrast to the second run of Example 3, good quality granules were obtained. The process was stable and churned out granules continuously for periods of more than 1 hour (long duration).

[0073] Example 4 shows how good quality granules with high potency can be produced continuously at surprisingly low temperatures without the need for any cutting and / or drying steps. The extruder operates at steady state, resulting in a continuous flow that saves costs, energy and time. The process can be adapted to the customer's needs more efficiently than batch processing. Waste can be reduced and / or quality improved, as errors are easier to identify and correct. No complex downstream processing is required.

Claims

1. A mixture comprising an active ingredient, a filler, and a binder, the mixture comprises at least 50% by weight of the active ingredient, based on the total weight of the mixture; and the mixture comprises at least 10 wt. % of a filler, based on the total weight of the mixture; and the melting temperature of the active ingredient is higher than the melting temperature of the binder; and The melting temperature of the binder is lower than the melting temperature of the filler; and The mixture comprises less than 5% by weight of water, based on the total weight of the mixture.

2. 10. The mixture of claim 1, wherein the mixture comprises at least 15% by weight of a filler, based on the total weight of the mixture.

3. 10. The mixture of claim 1, wherein the mixture comprises 15% to 25% by weight of a filler, based on the total weight of the mixture.

4. The mixture according to any one of claims 1 to 3, wherein the active ingredient is not a synthetic drug.

5. 4. The mixture according to claim 1, wherein the active ingredient is a micronutrient.

6. 4. The mixture according to claim 1, wherein the active ingredient is a water-soluble micronutrient.

7. 4. The mixture according to claim 1, wherein the active ingredient is a water-soluble vitamin.

8. The mixture - 50 to 80% by weight of ascorbic acid, based on the total weight of the mixture; - 15 to 25% by weight of a filler, based on the total weight of the mixture; - 5 to 15% by weight of a binder, based on the total weight of the mixture, and less than 2% by weight of water, based on the total weight of the mixture The mixture according to any one of claims 1 to 3, comprising:

9. 4. The mixture of claim 1, wherein the weight ratio of filler to binder is from 4:1 to 1:

1.

10. The mixture according to any one of claims 1 to 3, wherein the filler is a polysaccharide.

11. 4. The mixture according to claim 1, wherein the binder is a sugar alcohol.

12. 4. The mixture according to claim 1, wherein the filler is a polysaccharide and the binder is a sugar alcohol.

13. 4. The mixture according to claim 1, wherein the active ingredient is ascorbic acid, an edible salt thereof, or a water-soluble ester thereof.

14. Granules comprising the mixture according to any one of claims 1 to 3.

15. Granules comprising the mixture according to any one of claims 1 to 3.

16. 15. Granules according to claim 14, wherein the granules have a mass median particle size D50 (volume based) of 0.5 mm to 6 mm, as measured using dynamic image analysis.

17. 15. The granules according to claim 14, wherein the granules are obtained by continuous melt granulation of the mixture.

18. 15. The granules of claim 14, wherein the granules are water-soluble or water-dispersible.

19. Use of the mixture according to any one of claims 1 to 3 for continuous melt granulation.

20. A method for producing granules, comprising feeding the mixture according to any one of claims 1 to 3 into an extruder having at least one kneading zone.

21. 21. The method of claim 20, wherein the extruder is a twin-screw extruder without a cutting device.

22. 21. The method of claim 20, wherein the method does not include cutting the extruded strands.

23. 21. The method of claim 20, wherein the kneading zone has at least two kneading elements arranged at a stagger angle of between 30° and 90°.

24. 21. The method of claim 20, wherein at least one zone of the extruder is heated to a temperature of from 80°C to 180°C.

25. Granules obtainable by the method of claim 20.