Gelatinized cereal product containing oligosaccharide

Abstract: A gelatinised cereal product which contains a plant material which is a source of inulin; for example chicory. Sufficient of the plant material is included to provide at least about 0.25% by weight of inulin on a dry basis. The cereal product may be used as a pet food or breakfast cereal.

Description: This invention relates to a gelatinised cereal product which contains oligosaccharide in the form of inulin; especially in the form of natural sources of inulin such as chicory. In use, the cereal product has a beneficial effect in the gastro-intestinal tract of the consumer and hence upon the consumer as a whole. The invention also relates to a process of producing the cereal product and to methods of promoting beneficial effects in the gastro-intestinal tracts of humans and animals. The cereal product is particularly suitable for use as a pet food. Oligosaccharides such as inulin and various fructo-oligosaccharides are reported to promote the growth of bifido- and lacto-bacteria in the gastro-intestinal tract at the expense of pathogens such as Clostridium perfringens . For example, see Gibson et al ; 1994; Food Microbiology , 11(6), 491-498. Although most reported experimentation has been carried out in vitro , there have been reports that these oligosaccharides have a similar effect in the gut of rats and humans. Further, promoting the growth of bifido- and lacto-bacteria through the use of oligosaccharides is reported to have various beneficial effects on animals and humans. These beneficial effects include the prevention or treatment of diarrhoea, and increased growth; improved ability to breed, and enhanced health. These beneficial effects have resulted in use of oligosaccharides, particularly fructo-oligosaccharides, in human foods and feeds for live stock. For example, International patent application WO 94/27617 discloses the use of a caramel which contains fructo-oligosaccharides in animal feed to enhance the health of live stock. However, reports of the use of inulin also exist. For example Japanese patent application 63-309147 discloses the use of a purified inulin in the feed for younger animals to prevent diarrhoea after weaning and to increase body weight. Similarly, US patent 4,865,852 discloses the use of inulin in the form of treated chicory as a feed for live stock. Although the primary focus for oligosaccharides has been human foods and feeds for live stock, the use of fructo-oligosaccharides in a veterinary diet for pets has also been suggested (Willard et al ; 1994, Am. J. Vet. Res. , 55, 654-659). Further, products containing fructo-oligosaccharide are on the market; for example the Eukanuba product (The IAMS Company). For the products which contain inulin, the inulin is usually purified from plants which contain higher concentrations of inulin; such as chicory, Jerusalem artichoke, leek and asparagus. Otherwise, the plant material is treated in some form or another prior to use. A reason for the purification or treatment is that the plants themselves are reported to have bitter flavours which result in palatability problems; see for example US patent 4,865,852. This is particularly the case with chicory where the bitter flavours are believed to be due to the concentrations of sesquiterpene lactones such as lactucin and lactucopicrin in chicory. Also, it is generally believed that more accurate control of the amounts added may be obtained with purified product. Various procedures for purifying the inulin or treating the plant material have been reported. Usually however they include the steps of chopping up the plant, extracting it, and hydrolysing it with acids or enzymes. The hydrolysate is then collected and condensed to obtain the inulin. For example, Japanese patent application 63-309147 discloses grinding chicory tubers, partially hydrolysing them with acids, and then drying the hydrolysate with or without neutralisation. Unfortunately, fructo-oligosaccharides and purified inulin greatly add to the cost of the products. Consequently, for pet foods, their use has been confined to speciality veterinary products such as the Eukanuba product and to pet treats. Similarly, for human foods, their use has been confined to speciality products. Therefore there is a need for a cereal product which has the properties of food which contains fructo-oligosaccharides and purified inulin, which is palatable to humans and animals, and which may be inexpensively produced. Accordingly, in one aspect, this invention provides a pet food comprising a cereal product which comprises a gelatinised starch matrix which contains an amount of a natural plant material which is a source of inulin, sufficient to provide at least about 0.25% by weight inulin, on a dry matter basis. It has been surprisingly found that adding a natural plant material which is a source of inulin to the usual ingredients of gelatinised cereal products and then gelatinising the ingredients does not adversely affect the palatability of the food to pets. This is despite the presence of sesquiterpene lactones such as lactucin and lactucopicrin in the plant materials. The gelatinisation of the ingredients of the cereal products surprisingly appears to remove or destroy these compounds. Also, trials indicate that dogs may find the cooked food even more palatable than commercially available foods. Given that these plant materials were thought to be highly unpalatable to animals, this result is extremely surprising. Cats find the cooked food at least as palatable as commercially available foods. It is also surprisingly found that gelatinising of the ingredients does not result in any significant degradation of the shorter chain oligosaccharides of inulin. Therefore, it is believed that the gelatinised cereal product retains the properties of unprocessed inulin. The plant material preferably comprises an inulin-rich plant material such as chicory or Jerusalem artichoke, or both; especially chicory. The gelatinised cereal product preferably contains sufficient of the plant material such that it comprises at least 0.5% by weight of inulin on a dry matter basis. The maximum amount is inulin is preferably about 10% by weight on a dry matter basis. The gelatinised cereal product preferably includes at least about 0.01% by weight of kestose; 0.01 % by weight of nystose and 0.01% by weight of fructosyl-nystose. More preferably kestose, nystose and fructosyl-nystose make up at least about 0.1% by weight of the gelatinised cereal product; for example the gelatinised cereal product may include at least about 0.04% by weight of kestose; 0.04 % by weight of nystose and 0.04% by weight of fructosyl-nystose. Preferably, the gelatinised matrix further includes protein. The gelatinised cereal product preferably comprises an extrusion cooked product. The extrusion cooked product may be in dried pellet form, dried expanded form, or flaked form. In a further aspect, this invention provides a process of preparing a pet food gelatinised cereal product which contains at least about 0.25% by weight of inulin on a dry matter basis, the process comprising gelatinising a starch source, a protein source, and a natural plant material which is a source of inulin to form a gelatinised starch and protein matrix which contains the inulin. Preferably the starch source, protein source, and plant material are extrusion cooked and then extruded. Further, the extrudate may be dried. In another aspect, this invention provides a method of increasing the digestibility of a pet food cereal product comprising incorporating a natural plant material which is a source of inulin into the cereal product. In a yet further aspect, this invention provides a method of decreasing faecal volume of a pet, the method comprising feeding the pet a gelatinised cereal product which contains an amount of a plant material which is a source of inulin, sufficient to provide at least about 0.25% by weight inulin, on a dry matter basis. Embodiments of the invention are now described, by way of example only. The invention provides a gelatinised cereal product which contains an amount of a natural plant material, which is a source of inulin, sufficient to provide at least about 0.25% by weight inulin, on a dry matter basis. The plant material used may be any suitable source of inulin; for example chicory, Jerusalem artichoke, leek, onion, asparagus which contains high levels or inulin, and mixtures of these plants. However inulin rich plant materials such as chicory and Jerusalem artichoke are preferred; especially chicory. These plant materials usually comprise at least about 50% by weight of inulin. For ease of handling, the plant material is preferably in a dried, comminuted form. For simplicity of description, the processes described below are described with reference to the use of dried, comminuted chicory. However it is to be understood that any suitable plant material may be used in any suitable form. The remaining ingredients included in the gelatinised cereal product may be any suitable ingredients commonly used in gelatinised cereal products. Usually these ingredients include a starch source and a protein source. Suitable starch sources are, for example, grains such as corn, rice, wheat, beets, barley, oats, soy, and mixtures of these. Suitable protein sources may be selected from any suitable animal or vegetable protein source; for example meat meal, bone meal, fish meal, soy protein concentrates, milk proteins, gluten, and the like. The choice of the starch and protein sources will be largely determined by the nutritional needs of the animal or human, palatability considerations, and the type of cereal product produced. Various other ingredients, for example, sugar, salt, spices, seasonings, vitamins, minerals, flavouring agents, fats and the like may also be incorporated into the gelatinised cereal product as desired. The gelatinised cereal product may be produced in many different ways as desired. However, for a dried cereal product, an especially suitable way of producing the product is extrusion cooking. This may be done as is well known in the art. For example, in one suitable process, a feed mixture is fed into a preconditioner. The feed mixture is primarily made up of a starch source, a protein source, and the chicory. Preferably the chicory comprises at least about 1% by weight of the feed material; more preferably at least about 2% by weight. The maximum of chicory is preferably about 20% by weight; especially about 10% by weight. In the preconditioner, water or steam, or both, is mixed into the feed mixture. Sufficient water or steam is mixed into the feed mixture to moisten the feed mixture. If desired, the temperature of the feed mixture may be raised in the preconditioner to about 60°C to about 90°C by weight. A suitable preconditioner is described in US patent 4,752,139. Plainly, it is not necessary to use a preconditioner. The moistened feed leaving the preconditioner is then fed into an extruder. The extruder may be any suitable single or twin screw, cooking-extruder. Suitable extruders may be obtained from Wenger Manufacturing Inc. Clextral SA, Bühler AG, and the like. During passage through the extruder, the moistened feed passes through a cooking zone, in which it is subjected to mechanical shear and is heated; for example up to a maximum temperature of up to about 150°C, and a forming zone. The gauge pressure in the forming zone is about 300 kPa to about 10 MPa as desired. If desired, water or steam, or both, may be introduced into the cooking zone. During passage through the extruder, the starch source of the moistened feed is gelatinised to provide a gelatinised matrix structure primarily of starch, protein and chicory. The gelatinised matrix leaving the extruder is forced through a suitable die; for example a die as described in European patent application 0665051; the disclosure of which is incorporated by reference. A shaped extrudate, which has a cross-sectional shape corresponding to that of the orifice of the die, leaves the die. Depending upon the conditions in the extruder and the starch source used, the shaped extrudate expands to a greater or lesser extent. The shaped extrudate is then cut into pieces using blades. The individual pieces are then dried and, if desired, coated with protective or flavouring agents, or both. After cooling, the pieces may be packed into suitable packages. Alternatively, the individual pieces may be formed into flakes and then dried. Depending upon the ingredients used, the gelatinised cereal product may be in the form of dried kibbles suitable for use as pet foods, expanded pieces suitable for use in breakfast cereals, flakes suitable for use in breakfast cereals, and the like. It is also possible to produce a dried cereal product by mixing together water and the ingredients of cereal product; for example in a preconditioner. The wet mixture may then be shaped into a desired shape; for example using shaping rollers. The shaped mixture may then be baked in an oven; for example at about 220°C to about 280°C for about 10 minutes to about 1 hour. The dried cereal product has the appearance of a baked biscuit. If it is desired to produce a simulated meat product which may be used in canned pet foods, the processes described in US patents 4,781,939 and 5,132,137 may be used. In these processes, a protein source, especially a meat material, is emulsified. The meat material may be any suitable source of animal protein; for example the muscular or skeletal meat of mammals, poultry, and fish or meat by-products such as hearts, liver, kidneys, tongue and the like, or meat meals. Vegetable protein sources may also be included if desired. The exact composition may be selected according to cost and the desired flavour. The emulsification may be carried out in any suitable equipment. The dried chicory is added to the emulsion. Also, if desired or needed, additional protein may be added to the emulsion. The additional protein may be any protein source as mentioned above. The exact choice will depend upon availability, cost and palatability. Usually about 5% to about 35% of the further protein source is used. If desired or required, fats may also be added to the emulsion. Usually the amount of fat in the emulsion must be controlled to facilitate processing and to obtain an acceptable product. However, the meat material may well contain the desired amount of fats and hence adjustment may not be necessary. Typically at this stage the emulsion contains a maximum fat level of about 25% by weight. Conveniently, the amount of fat in the emulsion is in the range of about 5% to 15% by weight; more preferably about 7% to about 12% by weight. The mass ratio protein to fat in the emulsion is preferably about 1:1 to about 7:1. If added, the fats may be any suitable animal fats; for example tallow, or may be vegetable fats. Additional ingredients such as sugars, salts, spices, seasonings, flavouring agents, minerals, and the like may also be added to the emulsion. The amount of additional ingredients used is preferably such that they make up about 1% to about 5% by weight of the gelatinised cereal product. Water may also be added to provide from about 45% to 80% by weight moisture in the emulsion. If sufficient moisture is present in the meat material, water need not be added. Once mixed, the emulsion is preferably fed through a vacuum stuffer, or similar de-aeration apparatus, to de-aerate the emulsion. This removes air which may otherwise cause disruption of the formulated emulsion product and reduce its meat-like appearance. The emulsion is then fed to an emulsion mill which subjects the emulsion to rapid mechanical heating and shearing. Any suitable emulsion mill may be used, for example the emulsion mill disclosed in US patent 5,132,137. Other suitable emulsion mills are commercially available under the trade name of Trigonal and may be obtained from Siefer Machinenfabrik GmbH & Co KG, Bahnhofstrasse 114, Postfach 101008, Velbert 1, Germany. The temperature of the emulsion is raised to the desired coagulation temperature in the emulsion mill in a few seconds. For example, the temperature may be raised to from about 100°C to about 120°C. Alternatively, the temperature may be raised to in the range of about 45°C to about 75°C as described in US patent 5,132,137. Usually the mechanical energy generated in the emulsion mill will be sufficient to heat the emulsion to the desired temperature but this may be supplemented by the injection of superheated steam. The heated emulsion leaving the emulsion mill is then transferred to a holding tube. In the holding tube, the heated emulsion coagulates while moving slowly along the holding tube. The residence time of the heated emulsion in the holding tube is sufficient for the emulsion to have coagulated into a firm emulsion product upon reaching the exit of the holding tube. The firm emulsion product leaving the holding tube is then transferred to a cutter where it is cut into chunks of size suitable for use in a pet food. The chunks have the appearance and texture of meat. The chunks may be subjected to flaking if desired. The chunks may also be formulated into a chunk-in-gravy type of product. Other procedures for producing chunks are known and may be used; for example extruding a feed mixture, cooking the feed mixture in a steam oven, and the cutting the cooked extrudate into chunks. If it is desired to produce a canned pet food in the form of a meat loaf, a meat batter may be prepared by emulsifying a suitable meat material to produce a meat emulsion. The meat material may be any suitable meat source, for example as described above. Suitable gelling agents, for example gums such as kappa-carrageenan, locust bean gum, guar gum and xanthan gum may be added to the meat emulsion. Usually no more than about 2% by weight of gum is needed. The dried chicory is then added to the meat emulsion. Additional ingredients such as sugars, salts, spices, seasonings, flavouring agents, minerals, and the like may also be added to the meat emulsion. The amount of additional ingredients used is preferably such that they make up about 0.25% to about 5% by weight of the meat batter. Water may also be added the meat emulsion to provide from about 70% to about 85% by weight. If sufficient moisture is present in the meat material, water need not be added. The meat emulsion is then heated to a temperature above about 65°C in a mixer-cooker. Steam may be injected into the meat batter if desired. The heated meat emulsion is then again emulsified to provide a loaf batter and the loaf batter maintained at a temperature above about 60°C until filling into cans. It will be appreciated that the gelatinised cereal product may he produced by any suitable process and not only those described above. Other types of oligosaccharides may also be included in the gelatinised cereal product; for example fructo oligosaccharide and soy oligosaccharide. The soy oligosaccharides may be added in the form of soy meal or other suitable soy source. The cereal products may be in any suitable form; for example dried, semi-wet and wet. However, the matrix making up the cereal product must be gelatinised in order to remove or destroy the sesquiterpene compounds present in the inulin-containing plant material. Specific examples are now described for further illustration. Example 1 A feed mixture is made up of about 58% by weight corn, about 5.5% by weight of corn gluten, about 22% by weight of chicken and fish meal, dried chicory and salts, vitamins and minerals making up the remainder. Two levels of chicory are used; about 2.5% and about 5%. Also, two commercial types of chicory are used; Leroux standard blend and Leroux Rubis variety. Both types are commercially available on the French market from the Leroux company. The feed mixture is fed into a preconditioner and moistened. The moistened feed leaving the preconditioner is then fed into an extruder-cooker and gelatinised. The gelatinised matrix leaving the extruder is force through a die and extruded. The extrudate leaving the die head is cut into pieces suitable for feeding to cats, dried, and cooled to pellets. The pellets are fed to a panel of 80 cats. For comparison, the cats may choose between the pellets with chicory and control pellets which are identical except that they do not contain chicory. The amount that each cat eats of each type of pellet is monitored. The results are as follows: Example No Chicory Type Chicory level % Percentage consuming pellets containing chicory 1A Standard 2.5 42 1B Standard 5.0 52 1C Rubis 2.5 46 1D Rubis 5.0 52 The results indicate that the pellets with chicory have substantially the same palatability as those without. However, even more surprisingly, as the chicory content increases, the palatability appears to increase. The gut flora of the cats is analysed and it is determined that bifidobacteria counts have increased while C. perfringens counts have decreased. Further, faecal pH and odours are found to have decreased. Energy and mineral digestibility have increased leading to a decrease in faecal volume. The pellets are crushed and extracted with methanol by boiling under reflux for 1 hour. The extract is twice partitioned between water and chloroform and santonin is added. The chloroform phase is separated, dried and evaporated, The residue is dissolved in a mixture of methanol and chloroform and analysed using HPLC for free sesquiterpene lactones. The water phase is run through a column and glycosylated compounds eluted from the column using methanol. The eluant is evaporated, dissolved in water and treated with cellulase at 40°C for 2 hours. Santonin is added to the hydrolysate and the mixture extracted with ethyl acetate. The mixture is then analysed using HPLC for bound sesquiterpene lactones. No sesquiterpene lactones are detected. Similar analysis of the chicory starting ingredient reveals between 130 to 350 ppm free sesquiterpene lactones and between 380 to 680 ppm bound sesquiterpene lactones. Example 2 A trial is conducted using 30 dogs. The control food is the Friskies Menu Energy product, which is dried dog food available on the market. Two test foods are prepared; they correspond to the Friskies Menu Energy product except that they include 5% by weight of chicory. One test food contains the Leroux standard blend chicory and the other contains the Leroux Rubis chicory. The foods are fed to the panel of 30 dogs. The amount that each dog eats of each type of food is monitored. The trial is then repeated. The results are as follows: Example No Chicory Type Chicory level % Percentage consuming pellets containing chicory 2A Standard 5.0 62 2B 69 2C Rubis 5.0 80 2D 89 The results indicate that the foods with chicory have improved palatability as compared to the control. In the case of the standard chicory, the improvement is pronounced. The gut flora of the dogs is analysed and it is determined that bifidobacteria counts have increased while C. perfringens counts have decreased. Further, faecal pH and odours are found to have decreased. Energy and mineral digestibility have increased leading to a decrease in faecal volume. Example 3 The amount of kestose, nystose and fructosyl-nystose in the pellets of example 1 is measured. Oligosaccharide Example 1A Example 1B Example 1C Example 1D kestose 0.04 0.08 0.04 0.07 nystose 0.04 0.08 0.05 0.08 fructosyl-nystose 0.04 0.09 0.05 0.09 Total 0.12 0.25 0.14 0.24 The amount of total inulin, kestose, nystose and fructosyl-nystose in the two different types of chicory used in example 1 is measured. On the basis of this determination and the amount of chicory added, a theoretical amount of kestose. nystose and fructosyl-nystose is determined for each pellet. The theoretical. combined amounts of kestose, nystose and fructosyl-nystose in the pellets are then compared to the measured, combined amounts. The theoretical amounts and the measured amounts are comparable indicating that little or no degradation of the kestose, nystose and fructosyl-nystose has taken place during extrusion cooking. Example 4 A feed mixture is made up of rice flour, wheat flour, sugar, malt, vegetable fats, salt and about 5% by weight of chicory. The feed mixture is fed into a preconditioner and moistened. The moistened feed leaving the preconditioner is then fed into an extruder and gelatinised. The temperature at the exit of the extruder is about 150°C. The pressure in the extruder reaches about 130 bar. The gelatinised matrix leaving the extruder is forced through a die and extruded. The extrudate expands upon leaving the die head and is cut into pieces of about 2 to 3 mm. The pieces are then dried to a moisture content of about 1% by weight. The pieces are in the form of a puffed breakfast cereal. The pieces are tasted by a panel of consumers and are found to have a good taste; comparable to a puffed breakfast cereal produced without chicory. Example 5 A trial is conducted using 16 dogs. The control food is the Friskies Menu Vitality product, which is dried dog food available on the market. A test food is prepared which correspond to the Friskies Menu Vitality product except that it include 3% by weight of Leroux standard blend chicory. Eight dogs are fed the control food and eight dogs are fed the test food. Feces samples are collected from each dog, heated for 2 hours at 30°C, and the compounds released trapped on a Tenax tube. The trapped compounds are desorbed on a gas chromatograph. The levels of dimethylsulphide, dimethyldisulphide, and dimethyltrisulphide are determined as follows: Food Dimethylsulphide Area Dimethyldisulphide Area Dimethyltrisulphide Area Control 5731312 1084439 379164 Test 1719824 48824 43739 The results indicate that the feces of the dogs fed the test diet have much reduced amounts of those sulfur containing compounds which are believe to cause unpleasant odors. The levels of short chain fatty acids in the feces are also determined by gas chromatograph as follows: Food Acetate Area Propionate Area Butyrate Area Total Area Control 120 66 20 207 Test 159 91 18 267 The results indicate that the dogs fed the test diet have higher levels of short chain fatty acids in the gut. Short chain fatty acids are important nutrients for gut cells, the liver and muscles. An increase in the content of short chain fatty acids in the gut may result in an improvement in the health of the animal or human.

Claims: A pet food comprising a cereal product which comprises a gelatinised starch matrix which contains a natural plant material which is a source of inulin in an amount sufficient to provide at least 0.25% by weight inulin, on a dry matter basis. A pet food according to claim 1 in which the gelatinised starch matrix includes protein. A pet food according to claim 1 or claim 2 which is an extrusion cooked, dried pellet. A pet food according to any of claims 1 to 3 which is free of sesquiterpene lactones. A pet food according to any one of claims 1 to 4 in which the plant material is chicory or Jerusalem artichoke. A pet food according to any one of claims 1 to 5 which comprises at least 0.5% by weight of inulin, on a dry basis. A pet food according to any of claims 1 to 6 which comprises at least 0.1% by weight of kestose, nystose and fructosyl-nystose. A process of preparing a pet food cereal product which contains at least 0.25% by weight of inulin on a dry basis, the process comprising gelatinising a starch source, a protein source, and a natural plant material which is a source of inulin, to form a gelatinised starch and protein matrix which contains the inulin. A process according to claim 8 in which the starch source, the protein source, and the plant material are extrusion cooked and then extruded. The use of a natural plant material which is a source of inulin in the manufacture of a pet food comprising a cereal product having a gelatinised starch matrix for increasing the digestibility of the pet food. The use of a natural plant material which is a source of inulin in the manufacture of a pet food comprising a cereal product having a gelatinised starch matrix and at least 0.25% by weight of inulin on a dry matter basis, for decreasing faecal volume of a pet.

Inventors: ANANTHARAMAN HELEN GILLIAN, BALLEVRE OLIVIER, ROCHAT FLORENCE, ANANTHARAMAN, HELEN GILLIAN, BALLEVRE, OLIVIER, ROCHAT, FLORENCE
Applicants: NESTLE SA, SOCIETE DES PRODUITS NESTLE S.A.
Application year: 1997
Main classification: A23K1
IPC codes: A23L1, A23K1