METHOD OF PRODUCING EDIBLE PET CHEW PRODUCT AND PRODUCT PRODUCED THEREBY

Abstract

The present invention relates to a method for producing a pet chew product by a single injection molding cycle, comprising the steps of providing a thermoplastic starch mixture; converting said mixture into a thermoplastic starch-based melt; injecting the resulting thermoplastic melt comprising said optional blowing agent in a mould cavity while partially opening the mould during melt injection; allowing the thermoplastic melt in contact with the mould cavity wall to at least partially cool and set thereby forming the outer skin of a first density or hardness; partially opening the mould during melt cooling to allow gas expansion in the non-cooled core of the injected thermoplastic melt and formation of a foamed core of a second density or hardness; allowing the melt to cool and set, and ejecting the pet chew product from the mould cavity.

Claims

1. A method for producing a pet chew product by a single injection molding cycle, comprising the steps of: a) providing a thermoplastic starch mixture comprising 95-30 wt. % based on dry solid weight of the mixture of a starch or a starch derivative, 5-40 wt. % based on dry solid weight of the mixture of a plasticizer, and 0-30 wt. % based on dry solid weight of the mixture of a fibrous material; b) converting said mixture into a thermoplastic starch-based melt by subjecting the mixture to a step wherein the starch is destructurized; c) optionally mixing a blowing agent into the thermoplastic starch-based melt; d) injecting the resulting thermoplastic melt comprising said optional blowing agent in a mould cavity while partially opening the mould during melt injection; e) allowing the thermoplastic melt in contact with the mould cavity wall to at least partially cool and set thereby forming the outer skin of a first density or hardness; f) partially opening the mould during melt cooling to allow gas expansion in the non-cooled core of the injected thermoplastic melt and formation of a foamed core of a second density or hardness; g) allowing the melt to cool and set, and h) ejecting the pet chew product from the mould cavity.

2. A method for producing a pet chew product by a single injection molding cycle, comprising the steps of: a) providing a first thermoplastic starch mixture having a first density or hardness comprising 95-30 wt. % based on dry solid weight of the mixture of a starch or a starch derivative, 5-40 wt. % based on dry solid weight of the mixture, of a plasticizer, and 0-30 wt. % based on dry solid weight of the mixture of a fibrous material; b) converting said first mixture into a first thermoplastic starch-based melt by subjecting the mixture to step wherein the starch is destructurized; c) providing a second thermoplastic starch mixture having a second density or hardness, lower than the first mixture, said second mixture comprising 95-30 wt. % based on dry solid weight of the mixture of a starch or a starch derivative, 5-40 wt. % based on dry solid weight of the mixture of a plasticizer, and 0-30 wt. % based on dry solid weight of the mixture of a fibrous material; d) converting said second mixture into a second thermoplastic starch-based melt by subjecting the mixture to step wherein the starch is destructurized, and optionally adding a blowing agent to the mixture; e) injecting the first and second melt in a mould cavity using a two shot or sandwich moulding process for combining the first and second thermoplastic starch melts in the mould cavity while partially opening the mould during melt injection, wherein the first thermoplastic melt is injected to be in contact with the mould cavity wall and wherein the second thermoplastic melt is injected with respect to the first thermoplastic melt so as to be enveloped by it, whereby the partial opening the mould during melt injection may be during the first and/or second melt injection, preferably during the second melt injection; f) allowing the first and second melt to cool and set, optionally while partially opening the mould during the cooling step, and g) ejecting the pet chew product from the mould cavity.

3. Method according to claim 1 or 2, wherein the thermoplastic starch-based melt comprises a blowing agent selected from super critical fluids, nitrogen gas, carbonates, bicarbonates, nitrites, hydrides, peroxides, and oxygen-containing acid derivatives, preferably bicarbonates.

4. Method according to any one of the preceding claims, wherein the step of partially opening the mould during the injection step comprises opening the mould for between 1-15 mm.

5. Method according to any one of the preceding claims, wherein the step of partially opening the mould during the cooling step comprises opening the mould for between 1-15 mm.

6. Method according to any one of the preceding claims, wherein the moisture content of the thermoplastic starch mixture or the first and second thermoplastic starch mixtures is conditioned to 5 to 20 wt. %, preferably from 6 to 15 wt. %, more preferably from 7 to 10 wt. %, based on the total weight of the thermoplastic starch.

7. Injection moulded pet chew product produced by the method according to any one of claims 1-6.

8. Injection moulded pet chew product according to claim 7, whereby the pet chew is expanded as compared to a product produced with thermoplastic starch-based materials of the same composition in the same mould using the same method from which the step of partially opening the mould during melt injection has been omitted.

9. Injection moulded pet chew product according to claim 8, whereby the pet chew is additionally expanded as compared to a product produced with thermoplastic starch-based materials of the same composition in the same mould using the same method, wherein the method of the product for comparison comprises step f) of claim 1, and wherein the method of the product for comparison does not comprise the step of partially opening the mould during melt injection.

10. Injection moulded pet chew product according to any one of claims 7-9, wherein the thickness of the product is at least 8 mm, or wherein the thickness of the skin is between 0.3-8 mm, preferably 2-8 mm.

11. Injection moulded pet chew product according to any one of claims 7-10, wherein the thermoplastic starch-based material(s) have a protein content of less than 4 wt. % based on dry solid weight of the mixture.

12. Injection moulded pet chew product according to any one of claims 7-11, wherein the difference in hardness between the skin and the core is between 1-50 Shore D hardness units, and preferably wherein the Shore D hardness of the skin is >22 and wherein the Shore D hardness of the core is <40.

13. Injection moulded pet chew product according to any one of claims 7-12, wherein the thermoplastic starch-based material(s) comprise an abrasive agent, preferably in particle form, preferably having a Mohs hardness of between 0.5 and 8, preferably between 1 and 7, preferably selected from the group consisting of carbonates, hydrated magnesium silicates, phyllosillicates, apatite-like materials, silica's, and combinations thereof, preferably wherein the abrasive agent is present in an amount of between 0 and 20 wt. %, based on the dry weight of the mixture.

14. Injection moulded pet chew product according to any one of claims 7-13, wherein the at least partial opening of the mould plates during the injection phase is the result of a partial separation of the mould plates for between 1-10 mm, and wherein the at least partial opening of the mould during the cooling phase is the result of a partial separation of the mould plates for between 1-10 mm.

15. Injection moulded pet chew product comprising a skin of a first thermoplastic starch-based material enveloping a core of a second thermoplastic starch-based material, wherein the first and second thermoplastic starch-based materials may be the same or different, the core having a density or hardness lower than the skin, wherein the pet chew product is produced in a single injection moulding cycle using a first mould decompression step during the injection phase and a second mould decompression step during the cooling.

16. Injection moulded pet chew according to claim 15, wherein the skin comprises a non-cellular thermoplastic starch-based material, and wherein the core comprises a foamed or cellular thermoplastic starch-based material.

17. Injection moulded pet chew according to claim 15 or 16, wherein the first, second or both thermoplastic starch-based materials have a protein content of less than 4 wt. % based on the total weight of the starch.

18. Injection moulded pet chew according to any one of claims 15-17, wherein the pet chew has a thickness of at least 10 mm.

19. Injection moulded pet chew according to any one of claims 15-18, wherein the difference in hardness between the skin and the core is between 1-50 Shore D hardness units, and preferably wherein the Shore D hardness of the skin is >22 and wherein the Shore D hardness of the core is <40.

20. Injection moulded pet chew according to any one of claims 15-19, wherein the composition of the first and/or second thermoplastic starch materials comprise 95-30 wt. %, preferably 89-40 wt. %, based on dry solid weight of the composition, of a starch or a starch derivative, 5-40 wt. %, preferably 10-35 wt. %, based on dry solid weight of the composition, of a plasticizer, and 0-30 wt. %, preferably 1-25 wt. %, based on dry solid weight of the composition, of a fibrous material, preferably consisting of fibers having a length of between 23 and 2000 μm.

Description

DESCRIPTION OF THE DRAWINGS

[0110] FIG. 1 shows details of a section of a partly cellular injection moulding product according to the invention (A), and a cellular product made with help of microwave heating (B) prepared in accordance with methods as inter alia described in U.S. Pat. No. 6,180,161.

[0111] FIG. 2 shows overall appearance of an injection moulded product having a cellular core as produced in Example 2. Cross Section along flow direction (A), cross section along flow direction (higher magnification) (B), cross section perpendicular to flow direction (C).

[0112] FIG. 3 shows overall appearance of an injection moulded product having a cellular core as produced in Example 3. Cross Section along flow direction (A), cross section along flow direction (higher magnification) (B), cross section perpendicular to flow direction (C).

[0113] FIG. 4 shows overall appearance of an injection moulded product having a dense non-cellular core as produced in Example 4. Product overview (A), cross perpendicular to flow direction (B).

[0114] FIG. 5 shows overall appearance of an injection moulded products as produced in Example 5. A-C: Sample 5-1: Anti-Pragen: free distance. Cross Section along flow direction (A), cross section along flow direction (higher magnification) (B), cross section perpendicular to flow direction (C). Sample is irregular in shape and size. The skin is irregular in thickness. D-F: Sample 5.2: Anti-Pragen max 3 mm. Cross Section along flow direction (D), cross section along flow direction (higher magnification) (E), cross section perpendicular to flow direction (F). Material is rather regular in shape and size. The outside layer is rather regular in thickness. G-I: Sample 5.3: Anti-Pragen max 2 mm. Cross Section along flow direction (G), cross section along flow direction (higher magnification) (H), cross section perpendicular to flow direction (I). Material is maximal regular in shape and size. The outside layer is completely regular in thickness.

[0115] FIG. 6 shows overall appearance of an injection moulded products as produced in Example 6. A-B: Sample 6-1: Material composition A without chemical blowing agent; no anti-prägen. Interior is not expanded. The outside of the sample product is regularly shaped. C-D: Sample 6-2: Material composition A without chemical blowing agent; anti-prägen, but not limited (free way); Interior is slightly expanded due to moisture/steam expansion; The outside of the sample is irregularly shaped. E-F: Sample 6-3: Material composition A with chemical blowing agent; anti-prägen, max 2 mm; Interior is highly and homogeneously expanded due to the chemical blowing agent; the outside of the sample is regularly shaped.

[0116] FIGS. 7A and 7B show the appearance of an injection moulded products as produced in Example 8, test series 8-1, where the anti-prägen function was not active during the injection and cooling phase. Products of test series 8-1 have a somewhat foamy appearance (white spots on the surface) and product details are somewhat vague. FIGS. 7C and 7D show the overall appearance and thickness of products as produced in Example 8, test series 8-2, respectively. In series 8-2, anti-prägen function was active during the injection phase, but not during the cooling phase. Products of test series 8-2 have a more homogeneous appearance (without white spots). In 8-2, mould details are accurately copied into the moulded product.

[0117] FIGS. 8A and 8B show the thickness and the cross-sectional appearance of a product produced in Example 9, test series 9-1, respectively. Anti-prägen function was active during the injection phase, but not during the cooling phase. Products of test series 9-1 consist of solid, non cellular products. FIGS. 8C and 8D show the thickness and the cross-sectional appearance of a product produced in Example 9, test series 9-2, respectively. In 9-2, the anti-prägen function was active during both the injection phase and the cooling phase. Products of series 9-2 consist of a skin-core product, in which the skin consist of a non-cellular material and the core consist of a homogeneous foamed material. In 9-2, the (outer) shape and dimensions are smooth and regular (no blisters). In FIG. 8D, the upper product is a product of test series 9-1, and the lower product is of test series 9-2.

[0118] FIG. 9A shows the cross-sectional appearance of a product as produced in Example 10, test series 10-1. Anti-prägen function was active during the injection phase, but not during the cooling phase. FIG. 9B shows the cross-sectional appearance of a product as produced in Example 10, test series 10-2. In series 10-2, anti-prägen function was active during both the injection phase and the cooling phase. Products of product series 10-1 consist of skin-core and non cellular structure. Products of product series 10-2 consist of a skin-core product, in which the skin consist of a non-cellular material and the core consist of a homogeneous foamed material. In products of 10-2, (outer) shape and dimensions are smooth and regular (no blisters). In addition, mould details are accurately copied into the moulded product.

[0119] FIG. 10 shows the thickness and the cross-sectional appearance of a representative B1 test product (panel A), and a representative B2 reference product (panel B), as well as the length (ca. 20 cm) of both products (panel C, wherein B1-test product is top and B2 reference product is bottom) as used in Example 11.

[0120] FIG. 11 shows the average consumption of the B1-test product (bottom line) and B2-reference product (top line) as described in Example 12.

[0121] FIG. 12 shows the teeth of one of the dogs receiving the B1-test product of the invention as described in Example 12 with dental-plaque-disclosing agent after 0 days (panel A), 14 days (panel B) and 28 days (panel C).

DETAILED DESCRIPTION OF THE INVENTION

[0122] Thermoplastic starch has very beneficial material characteristics, making it very suitable for the production of edible pet chews. Essentially, materials with a variety of densities and hardness values can be produced depending on the amount of fiber and the amount of plasticizer used. Although fiber is not necessary for preparing a soft and low density material, it is preferred that fiber is present at least in the outer skin. Hence, the material is very suited for producing pet chews of different densities and hardness values.

[0123] It is an advantage of a pet chew product of the present invention that the specific combination of a hard thermoplastic starch with a soft thermoplastic starch comes very close to the natural diet of the pet. After all, the wild ancestors of our modern pets did not eat processed foods. They ate natural materials comprising combinations of hard and soft elements. Especially the carnivorous animals, would spend much time shredding soft tissue from hard bones. This natural diet has a tendency to clean the teeth of the animal by a mechanical cleaning action.

[0124] It is another advantage of a pet chew product of the present invention that the specific combination of a hard thermoplastic starch with a soft thermoplastic starch provides a hard sin with a soft core, wherein the thickness of the skin is adapted to allow piercing or fracturing by a pet's teeth when chewed. This allows penetration of the teeth whereby the outer layer will fracture, break or rupture when chewed, resulting in indentations or cavities in the hard outer skin having the profile of the pet's teeth. The soft core allows further penetration of the teeth into the underlying material and the resulting friction between tooth surface and pet chew skin results in strong mechanical interaction with the surface of the pet's teeth over its entire length. A pet chew product of the present invention is therefore very effective in removing plaque, or even tartar and stain from the teeth of an animal, even at the difficult-to-reach locations at the base of the teeth.

[0125] Chewable articles for pets such as dogs are well known in the art. These articles are of a flexible nature and serve as a toy for the pet as well as a means of keeping the pet's dentures in good condition. This type of article can be manufactured of different materials. Mainly, they can be divided in non-edible and edible variants. Most edible pet chews are based on starch, protein, or mixtures thereof.

[0126] U.S. Pat. No. 6,379,725 and WO 01/45517 disclose protein-based products.

[0127] U.S. Pat. No. 5,827,565 discloses a dog chew based on a thermoplastic potato starch.

[0128] US 2003/168020 discloses starch containing pet chews wherein mixtures comprising wheat flour, rice flour or tapioca flour in combination with a small amount of extra protein are extruded.

[0129] It is a feature of the product of the present invention that it combines a hard or dense skin (i.e. a skin portion having a higher density or hardness than the core portion) with a soft or cellular core (i.e. a core having a lower density or harness than the skin portion). Nonetheless, the product is preferably prepared in a single processing cycle. This means that, now that the product is based on thermoplastic starch, the skin and core are preferably fused and inseparable. Moreover, the density or hardness of skin and core differ. Yet, the skin and core are preferably cooled together and form a single product matrix. This facilitates that the cracked or fractured hard skin remains attached to the product as it is chewed by the pet. These hard skin fragments provide mechanical cleaning to the surface of the pet's teeth.

[0130] A single processing cycle, as defined herein, refers to a process wherein the skin and core are produced through a mechanical manufacture process using a piece of manufacture equipment that receives thermoplastic starch mixture(s) for skin and core at one and, and provides ready, finalized cooled products at another end using a single melting and cooling cycle. Examples of single processing cycles include moulding process involving only a single closing and opening of the mould.

[0131] A pet's chew according to the invention is based on starch. In principle, the starch may be of any origin. Suitable examples are potato, wheat, corn, tapioca, rice and pea starches. The starch can be used in native form, but may also be physically or chemically modified. Of course, it is also possible to use combinations of native starch and modified starch, or combinations of different modified starches. Chemically modified starches which may be used are oxidized starches, carboxymethylated starches, hydroxyalkylated starches, acetylated starches, (partially) hydrolysed starches, and other derivatized starches. An example of a suitable physically modified starch is a starch which has been subjected to ion exchange with, for instance, sodium or potassium ions.

[0132] The mixture that is to be converted into a thermoplastic starch according to the invention preferably comprises an amount of 30-95 wt %, preferably from 40-89 wt % based on dry solid weight of the mixture of a starch or a starch derivative.

[0133] A preferred example of a modified starch is a starch hydrolysate. This is a native (or already otherwise modified) starch which has been subjected to a partial chemical or enzymatic hydrolysis. The extent of hydrolysis can be expressed in terms of the dextrose equivalent (DE). Starch which has not been subjected to hydrolysis has a DE of 0, whereas a completely hydrolysed starch has a DE of 100. In order to improve the flowing characteristics of a mixture from which a thermoplastic starch is prepared according to the invention, it is preferred to incorporate a starch hydrolysate having a DE up to 40, more preferably between 1 and 20. It has been found that the use of a partially modified starch in the preparation of a pet's chew according to the invention results in a product having superior characteristics.

[0134] The molecular mobility of the mixture to be converted into a thermoplastic starch is increased by usage of starch hydrolysates), leading to an improved relaxation of the stress present in the material. As a result an increased dimensional stability in conjunction with an improved flexibility are achieved.

[0135] If desired, the starch may be mixed with other natural and biodegradable polymers such as cellulose and derivatives thereof, proteins such as zein or wheat proteins, or other polysaccharides such as gums (Arabic gum, guar gum and the like), pectin, or dragant. It is also possible to use a natural mixture of starch and proteins, such as flour, as a starting material.

[0136] The mixture that is to be converted into a thermoplastic starch according to the invention preferably comprises an amount of less than 10 wt. %, preferably less than 5 wt. %, even more preferably less than 4, 3, 2, or 1 wt. % of protein based on dry solid weight of the mixture, preferably based on the dry weight of the starch material. It is a preferred embodiment in aspects of this invention that the mixture that is to be converted into a thermoplastic starch is essentially free of protein.

[0137] In order to prepare a pet's chew of a starch material according to the invention, the starch is first converted into a thermoplastic starch melt. To that end, a mixture of the starch with suitable additives is prepared, which mixture is then preferably subjected to extrusion in order to destructurize the starch in the mixture.

[0138] The starch used in aspects of this invention is destructurized, preferably by extrusion.

[0139] In aspects of this invention, the starch or starch derivative is mixed with a plasticizer. Although water also has plasticizing qualities in a process of producing a pet's chew according to the invention, an additional plasticizer is present in the starch mixtures in aspects of this invention. A preferred class of plasticizers is the class of polyols. This class comprises, amongst others, glycol, diethylene glycol, alkylene glycols, polyalkylene glycol, sorbitol, glycerol, glycerol mono-esters, and the like. Other suitable classes of plasticizers include esters of citric acid, and urea. The amount of plasticizer that is preferably present in the starting mixtures to prepare a pet's chew according to the invention is from 5-40 wt. %, preferably from 10-35 wt. %, based on the dry solid weight of the mixture. It has been found that these amounts of plasticizer lead to a very flexible product, while the dimensional stability of the final product, the pet's chew, is not endangered.

[0140] The amount of water that is preferably present in the starting mixture to prepare a pet's chew according to the invention is from 7 to 35 wt. %, based on dry solid weight of the mixture.

[0141] The mixture may further comprise other additives such as an emulsifier. Suitable examples of emulsifiers include lecithin and monoglycerides. An emulsifier will be preferably be present in an amount of from 0 to 5 wt. %, based on dry solid weight of the mixture.

[0142] Flow property enhancers/lubricants result in an increased processability (products with lower stress) of the thermoplastic starch. Examples of flow property enhancers are animal and vegetable oils and fats, especially hydrogenated oils and fats, and fatty acids and fatty acid derivatives such as mono- and diglycerides, fatty acid amides, metal salts and sorbitanesters of these fatty acids. Also fosfatides can be used as flow property enhancer. Ricinus oil and lecithin are examples of flow property enhancers/lubricants with a particular good performance. The amount of flow property enhancer in the mixture to be converted to a thermoplastic starch can be up to 10 wt. %, more preferably between 0 and 5 wt. % based on dry solid weight.

[0143] A further suitable, but optional ingredient in the mixture is a fiber. Preferably, a pet food-grade fibrous material of natural origin is used. Preferred examples include cellulose, hemp, coconut, grass, flax, potato and other natural fibers. The fibers preferably have a length between 23 and 2000 μm, more preferably between 60 and 300 μm. The amount in which the fiber is preferably used is chosen in the range of from 0-30 wt. %, preferably from 1-25 wt. % based on dry solid weight of the mixture of a fibrous material.

[0144] A further suitable, but optional ingredient in the mixture is an abrasive agent. Preferably, the abrasive agent is in particle form. In order to have abrasive effect on the teeth of pets, the abrasive agent preferably has a Mohs hardness of between 0.5 and 8, preferably between 1 and 7, preferably selected from the group consisting of calcium carbonate or other carbonates, hydrated magnesium silicates, phyllosillicates, apatite like materials and/or various silica's. Other possibilities for abrasive agents are sodium alginate, powdered cellulose, cellulose fibers, pyrophosphates, and combinations thereof, preferably wherein the abrasive agent is present in an amount of between 0 and 20 wt. %, based on the dry weight of the mixture.

[0145] It is further possible to incorporate an organic or inorganic filler material, such as chalk or titanium oxide. A filler is preferably added in an amount of from 0 to 10 wt. %, based on the weight of dry solid mixture.

[0146] Other additives, such as pH regulators, health ingredients, vitamins coloring agents, enzymes, aromas or palatability enhancers can also be incorporated at this stage. For example, as pH regulator sodium bicarbonate or a phosphate buffer can be used. As health ingredients, vitamins or conjugated linoleic acid (CLA) can be used. As aroma or palatability enhancer, chicken, beef, or vegetable (e. g. mint or vanilla) aromas are often employed. As coloring agents, red, yellow, orange (iron oxide), green (chlorophyll) or white (titanium oxide) colorants are often employed. Typically, these additives will be added in an amount in the range of from 0 to 10 wt. %, based on dry solid weight of the mixture.

[0147] In order to prepare a thermoplastic starch of the above described mixture, it is preferably subjected to an extrusion step. During the extrusion, the starch will be gelatinized or destructurized. It is preferred to use a twin-type extruder operated at a temperature of from 95 to 180° C., more preferably from 100 to 150° C. As the mixture will undergo a thorough homogenisation during extrusion, it is not of crucial importance that all ingredients of the mixture are mixed so rigorously as to obtain a homogeneous mixture prior to extrusion. During the extrusion, the starch will be converted from a ordered structure into an unordered, amorphous structure (destructurizing), which yields a thermoplastic, very well processable material or melt.

[0148] In aspects of the present invention, it is preferred that a single injection mould cycle step, defined herein as a single processing cycle, is a final stage production cycle that follows the production of an intermediate granulate, wherein the granulate for the inner core and outer skin may be the same or different.

[0149] When preparing foamed inner cores in aspects of this invention, use can be made of a blowing agent (e.g. a super critical fluid (SCF), gas (e.g. nitrogen) or other blowing agent) that is mixed with the thermoplastic starch melt during or after extrusion, but prior to injection moulding, and a microcellular structure is created during injection moulding in the core of the product by gas expansion in the moulding cavity. A suitable process is the MuCell® process (Trexel, Inc., Wilmington, Mass. 01887 USA), wherein a single phase solution of thermoplastic melt and blowing agent is created by injecting the blowing agent into the thermoplastic melt during screw recovering of the extruded melt, and whereby the blowing agent is subsequently fully dissolved into the melt by mixing. Formation of the foamed inner core occurs during injection into the mould, whereby low pressure in the mould causes the blowing agent to form cells that grow in size until the material cools and sets or the mould cavity is full.

[0150] Another suitable blowing agent for use in aspects of this invention is water, or moisture, intrinsically present in the thermoplastic starch based mixtures. Moisture present in the mixture may suitably be used as a blowing agent when injection temperatures during injection moulding above 110° C. are used. In aspects of this invention injection moulding temperatures are usually about 130° C.

[0151] Highly preferred blowing agents include chemical blowing agents. Chemical blowing agents are organic and inorganic compounds that decompose thermally into gases not reacting with the polymer matrix. This process is usually exothermic and irreversible; however, certain compounds that decompose through thermal dissociation, such as bicarbonates, evolve gas in a reversible and endothermic reaction. The characteristic property of these compounds is their decomposition temperature, which determines their practical use as blowing agents for a given thermoplastic material and for its processing conditions. Chemical blowing agents may be based on carbonates and bicarbonates, nitrites, hydrides, peroxides, oxygen-containing acid derivatives, azo compounds, urea derivatives, hydrazines, semicarbazides, azides, N-nitroso compounds, and triazols. Highly preferred blowing agents in aspects of this invention are sodium bicarbonate based additives (e.g PlastronFoam®), for instance PlastronFoam F01-17 (Plastron SAS, France). The blowing agent is preferably food grade. Blowing agents may be added in an amount od between 0.01-10 wt. %, preferably 0.5-2 wt. %, more preferably about 1 wt. %, based on the weight of the mixture, and may be added to the mixture by dry blending.

[0152] In aspects of this invention, the pet's chew is moulded by injection moulding. The starting thermoplastic starch mixture (suitable for producing the first and second melts in aspects of this invention) is preferably conditioned to a moisture content of from 5 to 20 wt. %, more preferably from 6 to 15 wt. %, even more preferably from 7 to 10 wt. %, based on the weight of the mixture.

[0153] The moisture content can be controlled by using a vacuum zone in the extruder for preparing the mixture or by drying the mixture with hot air, a blowing agent can be added thereafter if needed.

[0154] During injection moulding, it is preferred to employ a processing temperature ranging from 80 to 200° C., more preferably from 110 to 170° C. If no, or not all additives like vitamins, coloring agents, aromas or taste enhancers have been added prior to extrusion, they can also be added to the thermoplastic starch granulate directly prior to injection moulding.

[0155] The injection moulding is preferably performed using a pressure in the barrel of the apparatus of below 2000 bar. The rate of injection is preferably kept relatively low and the injection channels are preferably relatively wide in order to keep the shear, that the material is exposed to, low.

[0156] In methods comprising injection molding, the skilled person will appreciate that thermoplastic starch exposed to temperatures in excess of 100° C. will have an inherent tendency to foam as it contains a certain amount of moisture. The moisture or water can serve as a blowing agent. In order to make use of this phenomenon in injection moulding, the material should be allowed to produce a foam. This means that the water in the material must be allowed to undergo gas expansion. As long as a thermoplastic starch material with a temperature over 100° C. is maintained under pressure, no foam will be formed. During the injection of the thermoplastic starch material in the mould, pressure is therefore preferably maintained. When the mould cavity is completely filled, the injected material will take a certain period before it is completely cooled and set, starting from the walls of the mould inward. At a certain time point prior to complete cooling, the temperature in the material in the mould ranges from a cooled outer layer to an inner layer that is still warm. If the mould cavity is opened for a small distance during cooling (anti-prägen) the outer layer will be unable to withstand the internal pressure, which exists in the (hot) core of the injected mass; the material will have the opportunity to produce a foam by gas expansion. This process can be further supported by the aid of an additional (gaseous) blowing agents, for instance in the form of a gas, including, but not limited to CO.sub.2 and N.sub.2, as described above. CO.sub.2 can suitably be in added in preferred amounts of 0-5%; N.sub.2 can suitably be in added in preferred amounts of 0-3%, based on the volume of the mould.

[0157] Modification of the injection moulding process may lead to an improved dimensional stability of the final product. In order to achieve this, the process should be designed in such a way that the lowest amount of stresses is frozen in the matrix. This can be realized by increasing the processing temperature, by using low backpressure profiles and using high mould temperatures, in combination with a low injection speeds. As a result, cycle times will increase.

[0158] The mould into which the starch melts are injection moulded, preferably has the shape of a conventional dog chew, such as the form of a bar, stick, or a hollow or other natural shape, for instance mimicking the shape of a bone. Other shapes that are contemplated are of a marrow bone, pig's ear, tooth brush, or a combination of shapes such as a dog chew which is shaped like a bone on one side and like a tooth brush on the other. The final product is preferably packaged in a water, moisture and air proof packaging material.

[0159] It is to be noted that it is contemplated that the above described embodiment of injection moulding may be preceded by extrusions steps, for instance by making use of a twin-screw extruder mounted on an injection moulding apparatus.

[0160] The pet chew product according to the present invention can be described by its hardness parameters. The pet chew product of the present invention combines a hard material on the outside with a softer material on the inside. The hardness of both the outer skin and inner core is suitably expressed in Shore D-scale (measured according to ISO 7619 and/or 868, preferably ISO 868).

[0161] Under the definition of the present invention, a hard outer skin may have a hardness higher than 22 Shore D, such as 25, 30, 35, 40, 45, 50, 55, 60, 65, 70 or 75 whereas a soft inner core may have a hardness lower than 30 Shore D, such as 25, 20, 25, 10, or 5. The shore D hardness of the outer skin may be in the range of 22-75, preferably 22-50, more preferably 25-30, while the shore D hardness of the inner core may be in the range of 5-30, preferably 15-25, more preferably 18-22. Although the above ranges overlap, the hardness of the inner core is lower than that of the outer skin. Preferably, the difference in hardness between the outer skin and the inner core may be between 1 and 30 Shore D hardness units, more preferably between 10 and 20 Shore D. The difference in hardness between the outer skin and the inner core may be between 1-10 Shore D hardness units, wherein the Shore D hardness of the outer skin is preferably >22 and wherein the Shore D hardness of the inner core is preferably <30.

[0162] Alternatively, under the definition of the present invention, a hard outer skin may have a hardness higher than 22 Shore ID, such as 25, 30, 35, 40, 45, 50, 55, 60, 65, 70 or 75 whereas a soft inner core may have a hardness lower than 40 Shore D, such as 35, 30, 25, 20, 25, 10, or 5. The shore D hardness of the outer skin may be in the range of 22-75, preferably 22-50, more preferably 25-30, while the shore D hardness of the inner core may be in the range of 5-40, preferably 15-37, more preferably 18-35. Although the above ranges overlap, the hardness of the inner core is lower than that of the outer skin. Preferably, the difference in hardness between the outer skin and the inner core may be at least between 1 and 50 Shore D hardness units. The difference in hardness between the outer skin and the inner core may be between 1-40 Shore D hardness units, wherein the Shore D hardness of the outer skin is preferably >22 and wherein the Shore D hardness of the inner core is preferably <40.

[0163] The invention will now be further elucidated by the following, nonrestrictive examples.

EXAMPLES

General

Production of a Thermoplastic Starch Granulate.

[0164] A powder/fluid mixture according to various specified formulations (see table 1) were extruded on a Buhler Twin Screw extruder DNDF-93 (L/D=48) extruder (12 barrel elements). The temperature profile along the barrel was: zone 1: 15-25° C.; zone 2: 15-25° C.; zone 3: 115-120° C.; zone 4: 135-145° C.; zone 5: 135-145° C.; zone 6: 100-105° C.; zone 7: 95-105° C.; zone 8: 70-90° C.; zone 9: 60-90° C. (incl. vacuum); zone 10: 60-90° C.; zone 11: 60-90° C. (incl. vacuum); zone 12: 50-60° C. Set point of the die temperature was 85-95° C. Screw speed was 125 rpm. The extrudate was granulated (pellet dimensions were about 4 mm) and dried to a moisture content of 9.3%-10.2%.

TABLE-US-00001 TABLE 1 Various starch based formulations used in Examples 2 to 6. Palatibility Composition Starch Glycerol Lecithin Fibre additive Filler A 51.1% 17.0% 3.2% 16.1% 2.6% 10% B 56.7% 18.9% 3.6% 17.9% 2.9% — C 62.6% 27.0% 4.0%  2.9% 3.4% —

Remarks:

[0165] All percentages mentioned are based on the dry solid weight of the total mixture; [0166] Starch: Food grade native potato starch obtained from AVEBE, Veendam, The Netherlands; [0167] Glycerol: type 1.26 glycerol vegetable obtained from Triconor, Soest, The Netherlands; [0168] Lecithin: ADLEC DNGM obtained from Brenntag Nederland, The Netherlands; [0169] Fibre: Arbocell BWW40 obtained from Rettenmaier Benelux, Zutphen, The Netherlands; [0170] Filler: Omyacare S70-KP obtained from Omya SA/NV, Brussels, Belgium. [0171] Palatibility additive: a mixture of potato starch, lupin flour and inactivated yeast.

Description of Injection Moulding Machine

[0172] For injection moulding an Engel DUO 1100 (Schwertberg, Austria) was used with a clamping force of 1100 ton. This machine was equipped with 3 injection units: [0173] Mucell unit. [0174] For sandwich moulding two injection units with a screw diameter of 80 mm are available. Both units were equipped with general purpose plasticating screws. For sandwich moulding this machine was moreover equipped with an Engel sandwich hot-runner module.

Mould

[0175] The mould, a 16-fold test chew mould (each product has a rectangular shape (cavity dimensions: length 230 mm, width 20 mm, thickness 5 mm) and should have a weight of 30 grams (final weight is dependent on exact material density) was provided by Verbi Gereedschappen B.V., Helmond, The Netherlands. This mould was equipped with a cold runner system. A maximum “Anti-Pragen” distance of 5 mm could be applied.

Example 1. Foamed Skin-Core Product According to Invention Vs. Non-Stratified Foamed Product of Prior Art Microwave Method

[0176] FIG. 1 (A) shows details of a section of a partly cellular injection moulding product produced in accordance with the invention as outlined in Example 2 (below), compared to a cellular product made by using the step of microwave heating of a starch composition prepared in accordance with methods as inter alia described in U.S. Pat. No. 6,180,161 in FIG. 1 (B).

Example 2. Moulding of a Foamed Skin-Core Product Out of One Material

[0177] An injection moulding test was performed with the material composition A of Table 1. To this composition 1% of PlastronFoam F01-17 of Plastron SAS, France was added as a blowing agent by dry blending.

[0178] Injection moulding was performed with one of the injection units of the sandwich module. Temperature profile along the cylinder of the injection moulding machine was: feeding zone: 50° C.; zone 2: 50° C.; zone 3: 60° C.; zone 4: 80° C.; zone 5: 100° C.; zone 6: 120° C.; zone 7: 130° C.; zone 8: 130° C. The sandwich hot-runner module was tempered at 130° C. The fixed mould half (including cold runner) had a temperature of 35° C., the movable mould half was tempered at 25° C. Anti-präg distance (which was applied during the first part of the cooling phase) was maximized at 2 mm. Total cycle time was about 50 sec.

[0179] Obtained products can be characterized as a skin-core product, in which the skin (thickness 1.8 mm) consist of a non-cellular material (shore D value is 39.8) and the core consist of a homogeneous foamed material (shore D value is 33.0). (Outer) shape and dimensions are smooth and regular (no blisters) (see FIGS. 2 A and B) (length 220 mm, width 20 mm, thickness 7.3 mm). Products from different moulding cycles are identical to each other in terms of texture, shape, dimension and appearance.

[0180] Product characteristics are displayed in the table below.

TABLE-US-00002 TABLE 2 Product characteristics of skin-core product Example 2 Composition blowing product agent Anti-Prägen Shore D skin Shore D core Composition 1% yes, max 2 39.8 [0.8] 33 [0.9] A mm

Example 3. Sandwich Moulding with 2 Different Materials Resulting in a Foamed Skin-Core Product

[0181] A sandwich injection moulding test was performed with material composition A (skin material) and material composition B (core material). To the core material 1% of PlastronFoam F01-17 of Plastron SAS, France was added by dry blending.

[0182] Injection moulding was performed with both injection units of the sandwich module. Temperature profile along both cylinders of the injection moulding machine were: feeding zone: 50° C.; zone 2: 50° C.; zone 3: 60° C.; zone 4: 80° C.; zone 5: 100° C.; zone 6: 120° C.; zone 7: 130° C.; zone 8: 130° C. The sandwich hot-runner module was tempered at 130° C. The fixed mould half (including cold runner) had a temperature of 35° C., the movable mould half was tempered at 25° C.

[0183] First material composition A was injected into the mould. After 40% of the total volume to be injected into the mould, the material supply switched over to material composition B (plus the Plastron additive). During the first part of the cooling phase “anti-prägen” was applied (mould opening distance was maximized at 2 mm). Total cycle time was about 50 sec.

[0184] Obtained products can be characterized as a skin-core product, in which the skin consist of a non-cellular material (shore D value is 33.4) and the core consist of a homogeneous foamed material (shore D value is 23.6). (Outer) shape and dimensions are smooth and regular (no blisters) (see FIG. 3). Final thickness of the product is 7 mm. Products from different moulding cycles are identical to each other.

[0185] Product characteristics are displayed in the table below.

TABLE-US-00003 TABLE 3 Product characteristics of skin-core product Example 3 Composition Composition blowing Anti- Shore Shore D skin core agent Prägen D skin core Composition Composition 1% yes, 2 33.4 [1.3] 23.6 [0.5] A B mm

Example 4. Sandwich Moulding with 2 Different Materials Resulting in a Non-Foamed Skin-Core Product

[0186] A sandwich injection moulding test was performed with material composition A (skin material) and material composition C (core material).

[0187] Injection moulding was performed with both injection units of the sandwich module. Temperature profile along both cylinders of the injection moulding machine were: feeding zone: 50° C.; zone 2: 50° C.; zone 3: 60° C.; zone 4: 80° C.; zone 5: 100° C.; zone 6: 120° C.; zone 7: 130° C.; zone 8: 130° C. The sandwich hot-runner module was tempered at 130° C. The fixed mould half (including cold runner) had a temperature of 35° C., the movable mould half was tempered at 25° C.

[0188] First composition A was injected into the mould. After 47% of the total volume to be injected into the mould, the material supply switched over to composition C. No “Anti-prägen” was applied. Total cycle time was about 50 sec.

[0189] Obtained products can be characterized as a skin-core product, in which both skin and core consist of a non-cellular material (shore D value of the skin is 34.8 and shore D value of the core is 23.2). (Outer) shape and dimensions are smooth and regular (no blisters) (see FIG. 4). Products from different moulding cycles are identical to each other.

[0190] Product characteristics are displayed in the table below.

TABLE-US-00004 TABLE 4 Product characteristics of skin-core product Example 4, Composition Composition blowing Anti- Shore D Shore D skin core agent Prägen skin core Composition Composition 0% no 34.8 [0.8] 23.2 [1.3] A C

Example 5. Effect of Anti-Präg Parameters on Product Properties

[0191] A series of sandwich injection moulding test were performed with material composition A (skin material) and material composition B (core material). To the core material 1% of PlastronFoam F01-17 of Plastron SAS, France was added by dry blending.

[0192] Injection moulding was performed with both injection units of the sandwich module. Temperature profile along both cylinders of the injection moulding machine were: feeding zone: 50° C.; zone 2: 50° C.; zone 3: 60° C.; zone 4: 80° C.; zone 5: 100° C.; zone 6: 120° C.; zone 7: 130° C.; zone 8: 130° C. The sandwich hot-runner module was tempered at 130° C. The fixed mould half (including cold runner) had a temperature of 35° C., the movable mould half was tempered at 25° C.

[0193] First material composition A was injected into the mould. After 40% of the total volume to be injected into the mould, the material supply switched over to material composition B (plus the Plastron additive). Total cycle time was about 50 sec.

[0194] Three tests were performed: [0195] Sample 5-1: During the first part of the cooling phase “anti-prägen” was applied (no maximum was applied; free distance (resulting in a distance of about 4 mm)). Obtained products can be characterized as a skin-core product, in which the skin consist of a non-cellular material (shore D value is 37) and the core consist of a irregular foamed material (shore D value is 23.6). The product is irregular in shape (not straight; cross section perpendicular to the flow direction has a more of less round shape instead of rectangular) and dimensions. Some blisters can be detected at the surface. Product is still rather hot when it is ejected out of the mould (see FIG. 5 A-C). [0196] Sample 5-2: During the first part of the cooling phase “anti-prägen” was applied (mould opening distance was maximized at 3 mm). Obtained products can be characterized as a skin-core product, in which the skin consist of a non-cellular material (shore D value is 36.4) and the core consist of a rather homogeneous foamed material (shore D value is 21.6). The product is rather regular in shape and dimensions (see FIG. 5 D-F). Final thickness of the product is about 7.7 mm. When ejected the temperature of the product is significantly lower than sample 5-1. [0197] Sample 5-3: During the first part of the cooling phase “anti-prägen” was applied (mould opening distance was maximized at 2 mm). Obtained products can be characterized as a skin-core product, in which the skin consist of a non-cellular material (shore D value is 33.4) and the core consist of a homogeneous foamed material (shore D value is 23.6). The product is more regular in shape and dimensions than sample 5-1 and 5-2. Mould dimensions are exactly copied to the product (see FIG. 5 G-I). Final thickness of the product is 7 mm. Due to the intense contact between mould and product cooling process is very efficient, resulting in lowest product temperatures when it is ejected.

[0198] Product characteristics are displayed in the table below.

TABLE-US-00005 TABLE 5 Product characteristics of skin-core product Example 5 Shore Shore Composition Composition blowing Anti- D D Example skin core agent Prägen skin core 5-1 Composition Composition 1% yes, no 37   23.6 A B limit [1.9] [0.5] 5-2 Composition Composition 1% yes, 36.4 21.6 A B max 3 [0.5] [0.9] mm 5-3 Composition Composition 1% yes, 33.4 23.6 A B max 2 [1.3] [0.5] mm

Example 6. Combined Effects of Anti-Präg Parameters and Addition of Blowing Agents on Product Properties

[0199] Injection moulding was performed with one of the injection units of the sandwich module. Temperature profile along the cylinder of the injection moulding machine was: feeding zone: 50° C.; zone 2: 50° C.; zone 3: 60° C.; zone 4: 80° C.; zone 5: 100° C.; zone 6: 120° C.; zone 7: 130° C.; zone 8: 130° C. The sandwich hot-runner module was tempered at 130° C. The fixed mould half (including cold runner) had a temperature of 35° C., the movable mould half was tempered at 25° C. Total cycle time was about 50 sec. [0200] Sample 6-1: samples have been injection moulded from material composition A. No “Anti-prägen” was applied. Obtained products can be characterized as an almost homogeneous, non-cellular product (shore D value of the skin is 47.2 and shore D value of the core is 46.2). The product is regular in shape and dimensions (see FIG. 6, A-B). [0201] Sample 6-2: samples have been injection moulded from material composition A. During the first part of the cooling phase “anti-prägen” was applied (no maximum was applied; free distance (resulting in about 4 mm)). Obtained products can be characterized as an irregular, skin-core product (shore D value of the skin is 40.2 and shore D value of the core is 35.4). Due to the effect that there is no additional blowing agent except from water, the foamed core is rather small, foam structure is coarse. The product is irregular in shape and dimensions (see FIG. 6, C-D). [0202] Sample 6-3: samples have been injection moulded from material composition A. To this composition 1% of PlastronFoam F01-17 of Plastron SAS, France was added by dry blending. Anti-präg distance (which was applied during the first part of the cooling phase) was maximized at 2 mm. Obtained products can be characterized as a skin-core product, in which the skin consist of a non-cellular material (shore D value is 39.8) and the core consist of a homogeneous foamed material (shore D value is 33.0). (Outer) shape and dimensions are smooth and regular (no blisters) (see FIG. 6, E-F). Products from different moulding cycles are identical to each other.

[0203] Product characteristics are displayed in the table below.

TABLE-US-00006 TABLE 6 Product characteristics of skin-core product Example 6. Composition blowing Anti- Shore D Shore Example Product agent Prägen skin D core 6-1 Composition 0% no 47.2 [0.8] 46.2 [0.8] A 6-2 Composition 0% yes, 40.2 [1.8] 35.4 [1.1] A free way 6-3 Composition 1% yes, 39.8 [0.8] 33 [0.9] A max 2 mm

TABLE-US-00007 TABLE 7 Overview Shore tests in the examples 2-6 Shore D was tested according to ISO 868 Composition Plastron Shore D Sample Material 1 Material 2 F01-17 Anti-Prägen Skin Core Example 2 Composition — 1% yes, max 2 mm 39.8 [0.8]   33 [0.9] A Example 3 Composition Composition 1% yes, max 2 mm 33.4 [1.3] 23.6 [0.5] A B Example 4 Composition Composition 0% no 34.8 [0.8] 23.2 [1.3] A C Example 5-1 Composition Composition 1% yes, no limits   37 [1.9] 23.6 [0.5] A B Example 5-2 Composition Composition 1% yes, max 3 mm 36.4 [0.5] 21.6 [0.9] A B Example 5-3 Composition Composition 1% yes, max 2 mm 33.4 [1.3] 23.6 [0.5] A B Example 6-1 Composition — 0% no 47.2 [0.8] 46.2 [0.8] A Example 6-2 Composition — 0% yes 40.2 [1.8] 35.4 [1.1] A Example 6-3 Composition — 1% yes, max 2 mm 39.8 [0.8]   33 [0.9] A

Example 7. Production of a Further Thermoplastic Starch Granulate

[0204] A powder/fluid mixture according to various specified formulations (see table below) were extruded on a Buhler Twin Screw extruder DNDF-93 (L/D=48) extruder (12 barrel elements). The temperature profile along the barrel was: zone 1: 15-25° C.; zone 2: 15-25° C.; zone 3: 115-120° C.; zone 4: 135-145° C.; zone 5: 135-145° C.; zone 6: 100-105° C.; zone 7: 95-105° C.; zone 8: 70-90° C.; zone 9: 60-90° C. (incl. vacuum); zone 10: 60-90° C.; zone 11: 60-90° C. (incl. vacuum); zone 12: 50-60° C. Set point of the die temperature was 85-95° C. Screw speed was 125 rpm. The extrudate was granulated (pellet dimensions were about 4 mm) and dried to a moisture content of 9.3%-10.2%.

TABLE-US-00008 TABLE 8 Various starch based formulations used in Examples 7 to 11. Palatibility Composition Starch Glycerol Lecithin Fibre additive Filler D 51.1% 17.0% 3.2% 16.1% 2.6% 10% B 56.7% 18.9% 3.6% 17.9% 2.9% — C 62.6% 27.0% 4.0%  2.9% 3.4% —
Compared to Table 1, composition D replaces composition A and differs in the type of Filler used.

Remarks:

[0205] All percentages mentioned are based on the dry solid weight of the total mixture [0206] Starch: Food grade native potato starch obtained from AVEBE, Veendam, The Netherlands [0207] Glycerol: type 1.26 glycerol vegetable obtained from Triconor, Soest,

[0208] The Netherlands [0209] Lecithin: ADLEC DNGM obtained from Brenntag Nederland, The Netherlands [0210] Fibre: Arbocell BWW40 obtained from Rettenmaier Benelux, Zutphen, The Netherlands [0211] Filler: Sibelite M72 obtained from SCR Sibelco NV, Dessel, Belgium. [0212] Palatibility additive: as for Table 1.

[0213] The injection moulding machine as described above in the general Material and Methods section.

Moulds:

[0214] The mould, a 16-fold test chew mould (each product has a rectangular shape (cavity dimensions: length 220 mm, width 20 mm, thickness 5 mm) was provided by Verbi Gereedschappen B.V., Helmond, The Netherlands. This mould was equipped with a cold runner system. Maximum “Anti-Pragen” distance of 6 mm is possible.

Example 8. Effect of Anti-Prägen During Injection Phase

Description Injection Moulding Process

[0215] A sandwich injection moulding test was performed with material composition D (skin material) and material composition C (core material) as indicated in Example 7.

[0216] Injection moulding was performed with both injection units of the sandwich module. Temperature profile along both cylinders of the injection moulding machine were: feeding zone: 50° C.; zone 2: 50° C.; zone 3: 60° C.; zone 4: 80° C.; zone 5: 100° C.; zone 6: 120° C.; zone 7: 130° C.; zone 8: 130° C. The sandwich hot-runner module was tempered at 130° C. The fixed mould half (including cold runner) had a temperature of 35° C., the movable mould half was tempered at 25° C.

[0217] First, composition D was injected into the mould. After 49.4% of the total volume to be injected into the mould, the material supply switched over to composition C. Anti-präg distance (which was applied during the injection phase) was maximized at 3 mm.

Test 8-1: The mould was closed and subsequently opened for 3 mm (before injection; so total cavity height is 8 mm). A total amount of 750 cm.sup.3 material (no gas was dosed into the melt) was injected into the mould with an injection speed of 200 cm.sup.3/s; after injection of the material, no holding phase was applied. After the holding phase, a cooling time of 30 sec was applied (the anti-prägen function during injection and/or cooling was not active during this cycle). Finally, the mould was opened and the products were ejected from the mould.
Test 8-2: The mould was closed and locked with a clamping force of 2500 kN. An amount of 750 cm.sup.3 material (no gas was dosed into the melt) was injected into the mould with an injection speed of 200 cm.sup.3/s; during injection the mould was opened for 3 mm. After injection of the material, no holding phase was applied. After the holding phase, a cooling time of 30 sec was applied. Finally the mould was fully opened and the products were ejected from the mould.

Description of Produced Products

[0218] Products are displayed in FIG. 7. Weight of the products produced in test 8-1 (FIGS. 7A and 7B; no anti-prägen function) and test 8-2 (FIGS. 7C and 7D; anti-prägen function active during the injection phase) is comparable and between 50 and 51 gram/product. Both products series consist of solid, non cellular products. The essential difference between both products can be seen when viewing product surface details (see FIG. 7A vs. FIG. 7C): e.g. when the letter “W” on the right-hand side of the product and product number on products of test 8-1 have a somewhat foamy appearance (white spots on the surface) and product details are somewhat vague. On the other hand, products of test 8-2 have a more homogeneous appearance (without white spots). Mould details are accurately copied into the moulded product. Shore D hardness of product from test 8-1: between 44 and 46 for skin and between 36 and 38 for core. Shore D hardness of product from test 8-2: between 44 and 46 for skin, and between 37 and 40 for core. The average density of both products is between 1.44 and 1.50 gram/cm.sup.3. The thickness of product 8-2 is 8.0 mm.

Example 9. Effect of Anti-Prägen During Injection Phase and Cooling Phase

Description Injection Moulding Process

[0219] Two injection moulding tests were performed with material composition C as described in Example 7. To this material 1% of PlastronFoam F01-17 of Plastron SAS, France was added by dry blending.

[0220] Injection moulding was performed with one of the injection units of the sandwich module. Temperature profile along the cylinder of the injection moulding machine was: feeding zone: 50° C.; zone 2: 50° C.; zone 3: 60° C.; zone 4: 80° C.; zone 5: 100° C.; zone 6: 120° C.; zone 7: 130° C.; zone 8: 130° C. The sandwich hot-runner module was tempered at 130° C. The fixed mould half (including cold runner) had a temperature of 35° C., the movable mould half was tempered at 25° C. Total anti-präg distance (which could be applied during both the injection phase and the cooling phase) was maximized at 5 mm (3+2 mm, for “during injection” and “during cooling” “anti-prägen, respectively).

Test 9-1: The mould was closed and locked with a clamping force of 2500 kN. An amount of 750 cm.sup.3 material was injected into the mould with an injection speed of 200 cm.sup.3/s; during injection the mould was opened for 3 mm. After injection of the material, a holding pressure of 750 bar was applied for 1 sec. After the holding phase, a cooling time of 30 sec was applied. Finally the mould was fully opened and the products were ejected from the mould.
Test 9-2: The mould was closed and locked with a clamping force of 2500 kN. An amount of 750 cm.sup.3 material was injected into the mould with an injection speed of 200 cm.sup.3/s; during injection the mould was opened for 3 mm. after injection of the material, a holding pressure of 750 bar was applied for 1 sec. Moreover after the holding phase and during the cooling phase (of 30 sec) the mould was further opened for 2 mm. Finally the mould was fully opened and the products were ejected from the mould.

Description of Produced Products

[0221] Products are displayed in FIG. 8. Weight of the products produced in test 9-1 and test 9-2 is slightly different 50-51 gram/product (test 9-1) resp. 54-55.5 gram/product (test 9-2). Products of products series 9-1 (FIGS. 8A and 8B; anti-prägen function during injection phase) consist of solid, non cellular products having no hardness stratification between skin and core and a thickness of 8.1 mm. Products of product series 9-2 (FIGS. 8C and 8D; anti-prägen function during injection phase and cooling phase) consist of a cellular core consisting of a homogeneous foamed material (shore D value 28-30) with a non-cellular skin material (shore D value 40-41) and a thickness of 10.0 mm. (Outer) shape and dimensions are smooth and regular (no blisters) (see FIGS. 8C and 8D). The average density of products from test 9-1 is between 1.44 and 1.48 grams/cm.sup.3; the average density of products from test 9-2 is between 1.18-1.21 grams/cm.sup.3.

[0222] A product thickness of at least 10 mm for an injection moulded pet chew product can be obtained in this process wherein a single plasticized starch matrix is injected into the injection mould using anti-prägen function during both injection and cooling phases in a single melt and cooling cycle.

Example 10. Sandwich Moulding with 2 Different Materials Resulting in a Foamed Skin-Core Product

Description Injection Moulding Process

[0223] A sandwich injection moulding test was performed with material composition D (skin material) and material composition C (core material). To material composition C, 1% of PlastronFoam F01-17 of Plastron SAS, France was added by dry blending.

[0224] Injection moulding was performed with both injection units of the sandwich module. Temperature profile along both cylinders of the injection moulding machine were: feeding zone: 50° C.; zone 2: 50° C.; zone 3: 60° C.; zone 4: 80° C.; zone 5: 100° C.; zone 6: 120° C.; zone 7: 130° C.; zone 8: 130° C. The sandwich hot-runner module was tempered at 130° C. The fixed mould half (including cold-runner) had a temperature of 35° C., the movable mould half was tempered at 25° C.

[0225] First, composition D was injected into the mould. After 49.9% of the total volume to be injected into the mould, the material supply switched over to composition C (+1% of PlastronFoam). Total anti-präg distance (which could be applied during both the injection phase and the cooling phase) was maximized at 5 (3+2 mm) mm.

Test 10-1: The mould was closed and locked with a clamping force of 2500 kN. An amount of 750 cm.sup.3 material was injected into the mould with an injection speed of 200 cm.sup.3/s; during injection the mould was opened for 3 mm. After injection of the material, no holding phase was applied. After the holding phase, a cooling time of 30 sec was applied. Finally the mould was fully opened and the products were ejected from the mould.
Test 10-2: The mould was closed and locked with a clamping force of 2500 kN. An amount of 750 cm.sup.3 material was injected into the mould with an injection speed of 200 cm.sup.3/s; during injection the mould was opened for 3 mm. After injection of the material, no holding phase was applied. Moreover, during the cooling phase (of 30 sec) the mould was further opened for 2 mm. Finally, the mould was fully opened and the products were ejected from the mould.

Description of Produced Products

[0226] Products are displayed in FIG. 9. Weight of the products produced in test 10-1 and test 10-2 is slightly different 50-51 gram/product (test 10-1) resp. 54-55.5 gram/product (test 10-2). Products of products series 10-1 (FIG. 9A; anti-prägen function during the injection phase) consist of skin-core and non cellular structure. Products of product series 10-2 (FIG. 9B; anti-prägen function during both the injection and cooling phase) consist of a skin-core product, in which the skin consist of a non-cellular material (shore D value is 44-46) and the core consist of a homogeneous foamed material (shore D value is 35-38) (FIG. 9B). (Outer) shape and dimensions are smooth and regular (no blisters). Mould details are accurately copied into the moulded product. The average density of products from test 10-1 is between 1.41 and 1.44 gram/cm.sup.3; the average density of products from test 10-2 is between 1.36-1.38 gram/cm.sup.3.

Example 11. Sandwich Moulding with 2 Different Materials Resulting in a Foamed Skin-Core Product for Use in Kennel Tests

Description Production Procedure of the Test and Reference Products

[0227] The mould as described in example 7 was modified to a allow a maximum “anti-prägen” distance of 10 mm (7+3 mm).

Sample B1 (Skin-Core Test Product)

[0228] A sandwich injection moulding procedure was performed with material composition D (skin material) and material composition B (core material). To material composition B, 1% of PlastronFoam F01-17 of Plastron SAS, France was added by dry blending.

[0229] Injection moulding was performed with both injection units of the sandwich module. Temperature profile along both cylinders of the injection moulding machine were: feeding zone: 50° C.; zone 2: 50° C.; zone 3: 60° C.; zone 4: 80° C.; zone 5: 100° C.; zone 6: 120° C.; zone 7: 130° C.; zone 8: 130° C. The sandwich hot-runner module was tempered at 130° C. The fixed mould half (including cold runner) had a temperature of 35° C., the movable mould half was tempered at 25° C.

[0230] First, composition D was injected into the mould. After 27.4% of the total volume of 935 cm.sup.3 to be injected (at 200 cm.sup.3/s) was injected into the mould, the material supply switched over to composition B (+1% of PlastronFoam F01-17). Total anti-präg distance (which could be applied during both the injection phase and the cooling phase) was maximized at 10 mm: during injection the mould was opened under “anti-prägen” for 6 mm. After injection of the material, no holding phase was applied. Moreover, during the cooling phase (of 40 sec) the mould was further opened under “anti-prägen” for 3 mm. Finally, the mould was fully opened and the products were ejected from the mould. A total of 200 products was produced.

Sample B2

[0231] Injection moulding was performed with one of the injection units of the sandwich module. Temperature profile along the cylinder of the injection moulding machine was: feeding zone: 50° C.; zone 2: 50° C.; zone 3: 60° C.; zone 4: 80° C.; zone 5: 100° C.; zone 6: 120° C.; zone 7: 130° C.; zone 8: 130° C. The sandwich hot-runner module was tempered at 130° C. The fixed mould half (including cold runner) had a temperature of 35° C., the movable mould half was tempered at 25° C.

[0232] After closing the mould, Composition B was injected into the mould (in total 465 cm.sup.3) at 200 cm.sup.3/s. No “anti-prägen” was used. After a cooling phase of 30 sec the mould was opened and the products were ejected from the mould. A total of 200 products was produced.

Description of Produced Products

[0233] Products are displayed in FIG. 10. Weight of the products produced was 23-24 gram/product for sample series B1, and 12-13 gram/product for sample series B2. Products from sample series B1 (FIGS. 10A and 10Ctop; anti-prägen function during both the injection and cooling phase) consist of a skin-core product, in which the skin consist of a non-cellular material (shore D value is 31-32) and the core consist of a homogeneous foamed material (shore D value is 21-22). (Outer) shape and dimensions are smooth and regular (no blisters). Mould details are accurately copied into the moulded product. The average density of sample series B1 is between 0.90 and 0.95 gram/cm.sup.3. A product thickness of at least 13 mm for an injection moulded pet chew product can be obtained in this process wherein two different plasticized starch matrices are injected in sandwich-mode into the injection mould and wherein an anti-prägen function during both injection and cooling phases in a single melt and cooling cycle is used.

[0234] Products from sample series B2 (FIGS. 10B and 10Cbottom; no anti-prägen function) consist of solid, non-cellular products having almost no hardness difference between skin and core (shore D value is 34-36). The average density of products is between 1.1-1.3 gram/cm.sup.3.

Example 12. Kennel Tests

Methodology

[0235] In order to determine the cleansing effect of a large dimension skin-core product according to the present invention on teeth of dogs, a product of sample series B1 was compared to a product of sample series B2, produced as described in Example 11, in a kennel test using a total of 30 dogs. Tests were carried out at an independent expert kennel specialized in palatability tests and studies on cats and dogs feeding behavior.

[0236] A palatability test was carried out for 28 days using 15 dogs for the B1 test product and 15 dogs for the B2 reference product. Dogs in the test group received 1 specimen of B1 test product per day. Dogs in the reference group received 1 specimen of B2 reference product per day. Dogs were individual housed at feeding time, and spend the remainder of the day in groups at a dog playground. Each dog was presented with 1 specimen of the test or reference product and rate of consumption was visually determined at three time points daily over a period of 18 hrs (0.5, 3 and 18 hrs) during the 28 days study. Observations were made by a single investigator. Scoring was 0 (not touched), 0.1 (10% consumed), 0.5 (50% consumed), 1.0 (100% consumed). The daily scores for individual time points in each group were combined to give the amount of product consumed at that time point as a percentage over the test or reference group. The combined daily scores over the 28 day period provided an objective indication of the rate of consumption and hence the preference of the product.

[0237] Further, in the same dogs, the amount of plaque and tartar was visually scored on a scale of 0-4 (low-high plaque/tartar) at days 0, 14 and 28 by a single investigator using a dental-plaque-disclosing agent. The presence of gum disease (inflammation) was also visually scored on a scale of 0-4 (low-high disease) at days 0, 14 and 28 by a single investigator.

Results

[0238] The average consumption of B1 test product and B2 reference product is provided in FIG. 11. At 0.5 hrs., less of the test product had been consumed compared to the reference product. At 18 hrs., both the reference and test products B2 were completely consumed in about 70% of the cases. Based on this, there was no important difference in preference of the dogs for either of the products.

[0239] Average plaque/tartar scores were 2.50 on both days 0 and 14 for the B1 test group, and 2.53 on both days 0 and 14 for the B2 reference group. Average gum disease scores were 1.53 and 1.73 on day 0 and 14, respectively, for the B1 test group, and 1.57 and 1.71 on day 0 and 14, respectively, for the B2 reference group.

[0240] In the table below, the results are presented for the plaque/tartar and gum disease tests at day 28. Numbers are average values for 15 dogs per group and based on the 0-4 score levels described above.

TABLE-US-00009 TABLE 9 Results of Example 12 Day 28 plaque reduction comparison Plaque and gum tartar disease B2 Reference 2.60 1.87 B1 Test 2.21 1.64 % reduction 15%* 12% *Significant reduction of tartar with one-tail t-test

[0241] A statistically significant reduction in plaque and tartar was observed at day 28 when comparing the B1 test group receiving the product according to the present invention, with the B2 reference group receiving the reference product. Gum disease was also reduced in the B1 test group compared to the reference group.

[0242] The above results obtained with kennel tests indicate that the product of the present invention is able to control dental health problems in domesticated pets by reducing dental plaque.