IL37075A - Protein fortified snack,process and product - Google Patents
Protein fortified snack,process and productInfo
- Publication number
- IL37075A IL37075A IL37075A IL3707571A IL37075A IL 37075 A IL37075 A IL 37075A IL 37075 A IL37075 A IL 37075A IL 3707571 A IL3707571 A IL 3707571A IL 37075 A IL37075 A IL 37075A
- Authority
- IL
- Israel
- Prior art keywords
- starch
- product
- protein
- mixture
- source
- Prior art date
Links
- 235000011888 snacks Nutrition 0.000 title claims description 49
- 108090000623 proteins and genes Proteins 0.000 title claims description 46
- 102000004169 proteins and genes Human genes 0.000 title claims description 46
- 238000000034 method Methods 0.000 title claims description 31
- 229920002472 Starch Polymers 0.000 claims description 63
- 235000019698 starch Nutrition 0.000 claims description 62
- 239000008107 starch Substances 0.000 claims description 59
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 40
- 239000000203 mixture Substances 0.000 claims description 27
- 239000000463 material Substances 0.000 claims description 26
- 235000013305 food Nutrition 0.000 claims description 21
- VBICKXHEKHSIBG-UHFFFAOYSA-N 1-monostearoylglycerol Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(O)CO VBICKXHEKHSIBG-UHFFFAOYSA-N 0.000 claims description 18
- 229920000881 Modified starch Polymers 0.000 claims description 13
- 238000002156 mixing Methods 0.000 claims description 12
- 235000019426 modified starch Nutrition 0.000 claims description 11
- 108010073771 Soybean Proteins Proteins 0.000 claims description 10
- 239000011159 matrix material Substances 0.000 claims description 10
- 229940001941 soy protein Drugs 0.000 claims description 10
- 239000004368 Modified starch Substances 0.000 claims description 9
- 229940075507 glyceryl monostearate Drugs 0.000 claims description 9
- 239000001788 mono and diglycerides of fatty acids Substances 0.000 claims description 9
- 239000008139 complexing agent Substances 0.000 claims description 7
- 238000003860 storage Methods 0.000 claims description 7
- 235000016709 nutrition Nutrition 0.000 claims description 6
- 235000019629 palatability Nutrition 0.000 claims description 6
- 230000000536 complexating effect Effects 0.000 claims description 3
- 235000004213 low-fat Nutrition 0.000 claims description 3
- 229920001592 potato starch Polymers 0.000 claims 2
- 235000010469 Glycine max Nutrition 0.000 claims 1
- 244000068988 Glycine max Species 0.000 claims 1
- 238000007493 shaping process Methods 0.000 claims 1
- 239000000047 product Substances 0.000 description 92
- 235000018102 proteins Nutrition 0.000 description 34
- 239000003925 fat Substances 0.000 description 21
- 244000061456 Solanum tuberosum Species 0.000 description 12
- 235000002595 Solanum tuberosum Nutrition 0.000 description 12
- 239000004615 ingredient Substances 0.000 description 10
- 150000003839 salts Chemical class 0.000 description 7
- 239000003153 chemical reaction reagent Substances 0.000 description 6
- 235000013312 flour Nutrition 0.000 description 6
- 241000209140 Triticum Species 0.000 description 5
- 235000021307 Triticum Nutrition 0.000 description 5
- 239000002253 acid Substances 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 5
- 239000000796 flavoring agent Substances 0.000 description 5
- 235000019634 flavors Nutrition 0.000 description 5
- 238000001125 extrusion Methods 0.000 description 4
- 240000008042 Zea mays Species 0.000 description 3
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 3
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 3
- 235000014633 carbohydrates Nutrition 0.000 description 3
- 150000001720 carbohydrates Chemical class 0.000 description 3
- 238000010411 cooking Methods 0.000 description 3
- 235000005822 corn Nutrition 0.000 description 3
- 239000000499 gel Substances 0.000 description 3
- 239000013067 intermediate product Substances 0.000 description 3
- LDVVTQMJQSCDMK-UHFFFAOYSA-N 1,3-dihydroxypropan-2-yl formate Chemical class OCC(CO)OC=O LDVVTQMJQSCDMK-UHFFFAOYSA-N 0.000 description 2
- 240000003183 Manihot esculenta Species 0.000 description 2
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- 235000013339 cereals Nutrition 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 125000003976 glyceryl group Chemical group [H]C([*])([H])C(O[H])([H])C(O[H])([H])[H] 0.000 description 2
- 230000036571 hydration Effects 0.000 description 2
- 238000006703 hydration reaction Methods 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 102000009027 Albumins Human genes 0.000 description 1
- 108010088751 Albumins Proteins 0.000 description 1
- 229920000856 Amylose Polymers 0.000 description 1
- 229920002261 Corn starch Polymers 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 102000004407 Lactalbumin Human genes 0.000 description 1
- 108090000942 Lactalbumin Proteins 0.000 description 1
- 235000019759 Maize starch Nutrition 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000005018 casein Substances 0.000 description 1
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 1
- 235000021240 caseins Nutrition 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 230000010006 flight Effects 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000873 masking effect Effects 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000008935 nutritious Nutrition 0.000 description 1
- 238000000643 oven drying Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 235000019699 ravioli Nutrition 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 235000012184 tortilla Nutrition 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L19/00—Products from fruits or vegetables; Preparation or treatment thereof
- A23L19/10—Products from fruits or vegetables; Preparation or treatment thereof of tuberous or like starch containing root crops
- A23L19/12—Products from fruits or vegetables; Preparation or treatment thereof of tuberous or like starch containing root crops of potatoes
- A23L19/18—Roasted or fried products, e.g. snacks or chips
- A23L19/19—Roasted or fried products, e.g. snacks or chips from powdered or mashed potato products
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L7/00—Cereal-derived products; Malt products; Preparation or treatment thereof
- A23L7/10—Cereal-derived products
- A23L7/117—Flakes or other shapes of ready-to-eat type; Semi-finished or partly-finished products therefor
- A23L7/13—Snacks or the like obtained by oil frying of a formed cereal dough
Landscapes
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Confectionery (AREA)
- Grain Derivatives (AREA)
- Preparation Of Fruits And Vegetables (AREA)
- Bakery Products And Manufacturing Methods Therefor (AREA)
Description
PROTEIN FORTIFIED .SHACK, PROCESS AND PRODUCT FORTIFIED SNACK PROCESS AND PRODUCT Abstract of the Disclosure A process for producing nutritious protein fortified low calorie snack food products is disclosed. The process involves fortifying carbohydrate materials such as substantially gelatinize starch with a protein material which has not been substantially he gelled: The fortified carbohydrate material can then be formed into a variety of snack food products, such as snack chips, which exhibit an increased shelf life, improved organoleptic properties, reduced calorie content, and improved nutritional value.
Background of the Invention The prior art has taught a wide variety of processes for producing snack food products and products made by a number of these processes are currently available to the consumer. Typicall many of these products are deep fat fried to give the product a puffed or expanded configu ion. However, the fat fried products for example as described and claimed in our patent No.3¾575, of the art/have the disadvantage of adsorbing too much fat on frying, resulting in a product which has a high energy content and which is not acceptable to consumers who want a low calorie snack product. To avoid the problem of high fat content, it has been suggested that snack products be formed from a dough containing a low fat content and cooked by high temperature oven drying or by exposure to microwave or infrared radiation. These methods do avoid the problem of a high fat content in the product, but fail to produce the high palatability which is developed in the frying process.
The prior art has also failed to provide a satisfactory shelf life in a fried product. Typically, the products of the prior art adsorb moisture during storage and develop a stale, soggy texture and a rancid flavor due to the oxidation of the fat present in the product. It would fill a need in the snack food market, therefore, to provide a process of producing a nutritionally fortified, relatively low calorie snack food product which has high palatability and a long, stable shelf life on storage and which does not have the high fat content of normally prepared fat fried products.
Summary of the Invention The invention relates to a novel process for preparing low calorie, low density snack type food products having increased nutritional value, particularly an enhanced protein content, and to the product produced by the process.
The process involves a method of producing a snack product intermediate which does not pick up an excessive amount of fat when converted to a snack food product by frying and to the finish snack product. The finished product has an exceptional shelf life and does not develop rancidity as rapidly as known products due to the low fat content. The product remains fresh and crisp for long periods of time due to the properties of an in situ heat gelled protein and to the stabilization of the starch content by a starch modifying agent. The starch modifying agent acts to block the hydrophilic sites on the starch molecule to prevent the pick-up of an excessive amount of water during the mixing of the snack produc dough prior to forming. The starch modifying agent permeates the starch matrix and lubricates the mix enabling a smooth dough to be formed at a low moisture content. The mixed dough, containing 30 to 48% water, 41 to 49% starch or flour, 16 to 25% protein, and 0.25 to 4% of a starch modifying agent, is then formed into a shaped product, preferably by extruding. The shaped product is then converted to a snack food product, preferably by frying. Dur the frying operation, the product is heated by the hot oil and the fryin operation, the product is heated by the hot oil and the water content of the product boils off and is partially replaced by oil from the frying bath. Since the hydrophilic sites of the starch molecule have been blocked by the starch complexing agent during mixing and possibly by the protein, there is less water boil off and less fat adsorbtion by the snack food intermediate during the frying step. The heat of the frying step also serves to 3et or heat gel the protein source. It is believed that the heat gelled protein present in the product matrix and the retained starch complexing agent resist readsorption of moisture and produc a finished snack food product which remains crisp and palatable during a long storage period. The moisture content of the cooked product will typically be in the range of 2 to 6% by weight; the protein content will be from 16 to 25% by weight; the starch content may be from 48 to 56% by weight; and the fat content between 12 and 35% by weight.
The starch source used in the process may be any of the common grain source materials such as wheat, rice, corn, flours. or starch, as well as starches or flours from common tubers such as potato or tapioca source material. The starch material should be substantially pre-gelatinized prior to being cooked to inhibit excessive browning of the product during the cooking step. Modified starch materials such as acid modified starches or esterified starches, partially dextrinized, or partially gelatinized starches may also be added to the product to modify extrusion, frying, mixing and handling characteristics.
The protein source material may be any of the high purit protein sources such as casein, albumin, or oilseed protein isolates. Soy protein isolates containing at least about 90 to 95% protein on a dry basis are preferred.
Description of the Preferred Embodiments The concept of this invention pertains broadly to a process for producing a nutritionally fortified snack food intermediate product from both starch and protein sources which has superior organoleptic properties and an increased shelf life and which has a reduced fat and calorie content on frying, and the fried product. The method involves preparing a dough of a starch source, the protein source and a starch modifying or complexing reagent which blocks the hydrophilic sites on the starch molecules so that they do not take up or bind water and less total water is needed to form the dough.
A modified starch source may be used, such as an acid modified waxy maize starch, a cereal starch or flour such as wheat, rice or corn may be used, or a tuber starch or flour such as tapioca or potato may be used. It is preferred that the starch material be substantially pre-gelatinized before being used in the process. If a modified starch is used, it may be added in pro portions up to about 15% by weight. Typical modified starch materials are the acid modified, esterified and enzyme modified starch An acid modified starch suitable for use in the product of this invention may be obtained from National Starch Co. under the trade name "Fry A Snack." Modified starches may be used to improve texture and cooking characteristics of the product.
The protein source may be any high purity protein, for example milk, egg, or oilseed proteins. The protein material should not have been substantially heat set or gelled prior to being used in the process of the invention, however. We have found that a functional isolated soy protein having a protein content of at least about 90 to 95% by weight on a dry basis is preferred.
The starch modifying and complexing agent may be a saturated monoglyceride material which will react to mask the hydrophilic sites on the starch molecule to prevent the hydration of the starch molecule by water. A preferred saturated monoglyceride material for masking the hydrophilic sites on the starch molecule is glyceryl monostearate. 0 I I CH2-0-C-C17H35 diOH The process of the invention involves preparing a mix of the starch source, the protein source, the starch complexing agent, and water. The water is added in smaller proportions than would normally be required without the starch modifying agent. The mix is then formed into the shape of a snack food product such as a snack chip. The forming is preferably performed on an extruder, e.g. , a De Francisci Press. The dough should be extrude under conditions that do not heat gel the protein present in the dough mix in order to preserve the heat gelling characteristics ' of the protein until the fat frying step.
In forming the dough mix the starch source is added at a level of between about 41 and 4970 by weight of the mix and the protein source is added at a level of between about 16 and 25% by weight of the mix. Between about 0.25 and 4% by weight of the starch modifying reagent is added to the mix and between 30 and 487c by weight water. The mix is worked to form a free-flowing mixture, usually between 5 and 25 minutes. A conventional dough mixer may be used, such as a commercial ribbon blender.
We believe that the starch complexing agent acts to align the starch and protein molecules of the mix and to lubricate the molecules so that in ermolecular slippage is possible at a much lower moisture content than in a dough made without the added reagent. The starch complexing agent is a polar structure which is hydrophilic at one end of the molecule and lipophilic on the other end. The hydrophilic end of the starch complexing molecule attaches itself at the sites of the starch molecule' which would normally be occupied by water, particularly the sites in the amylose fraction of the starch molecule. The lipophilic portion of the starch modifying reagent resists hydration by water and acts to lubricate the spaces between the molecules. The resulting dough is thus able to develop the proper viscosity or elasticity for working at a lower moisture content. The starch modifying reagent also is believed to operate on the protein source in a similar fashion, though the water resisting effect may be somewhat less than that occurring with starch. Due to the blockage of the water accepting sites on the starch and possibly the protein molecules there is less total water present in the dough and in the intermediate product formed from the dough. As a result, there is less water to boil off during the frying operation to be replaced by fat from the frying bath.
The forming of the dough into the intermediate product by extrusion is performed by passing the dough through the barrel of the extruder where the dough is mixed and worked by the action of the extruder screw. The screw flights tend to advance the dough faster than it can be expelled from the extruder causing back-mixing and a great deal of internal friction in the dough. The friction develops heat in the mix and care must be taken to prevent the build-up of heat in the product to the point where the protein source is prematurely heat set or gelatinized. ί Preferably, the extrusion is performed in an extruder which is equipped with cooling jackets along the length of the barrel. A cooling medium such as cool water is circulated in the cooling jackets to reduce the heat build-up in the material- in the extrude Heat can also be added along the extruder barrel to maintain the temperature at a desired level, if necessary. Preferably,' the extruder is operated to maintain the product at a temperature of between about 155° and 185° F. as the product leaves the extruder. The optimum temperature of the product leaving the extruder is about 170° F. The product leaving the extruder passes through a restricted outlet or die which forms the dough mix into a flattene sheet or ribbon. To form a desirable, crisp snack product when fried, the sheet or ribbon will be between about .018 and .050 inches thick as it leaves the die. After the sheet or ribbon leaves the die, it passes over rolls onto a belt. The rolls and belt are preferably operated at a speed which will stretch the dough sheet or ribbon. By imparting a stretch to give the dough an elongation of from preferably about 25 to 100% or more, the c cooking characteristics of the dough are improved. The stretched ribbon exhibits much better texture on frying; the fried product has fewer large, fragile bubbles, is denser and has greater streng than an unstretched product. The unstretched product tends to form large, hollow, balloon-like structures when fried which are not suitable for snack chip products. The large bubbles break during handling, packaging, and transporting and produce a crumble unsatisfactory product. The large balloon structures also do not have the strength required of a snack chip product and fracture when used as a dip cracker. However, the hollow structures could be satisfactorily used for containers for filled type products suc as egg rolls or ravioli.
The desirable elasticity in the dough mix is believed v to be developed by the use of the starch modifying material during the mixing of ingredients prior to extrusion. The starch chains and possibly the protein chains are believed to be longitudinally aligned due to the action of the starch modifying material with the' intermolecular spaces lubricated so that intermolecular slippage is possible. The alignment and slippage are believed to give the mix the resilience and elasticity needed for a good stretch prior to frying.
The ribbon or sheet is then cut to form strips by a conventional means such as a rotating cutter or a similar device. A finished cooked snack food product would preferably be in the form of a thin rectangular strip of approximately 1 1/4" x 2 1/2" x 1/8" dimensions. The snack food intermediate strip leaving the extruder will contain about 41 to 4970 starch, about 16 to 25% protein, about 30 to 48% water, and about 0.25 to 4% of the starch modifying reagent. The cut strips may then be transferred to a fat frying bath. During the transfer operation the strips may lose between 2 and 4% moisture. The moisture content of the strips placed in the frying bath will typically be between 30 and 46% water by weight.
The strips are fried in a fat fry bath for between 15 and 60 seconds at a temperature of between 350 and 425° F. to develop the crisp texture of a snack food product and to develop the palatable taste expected in a snack product. The material should have a pleasant golden color when removed from the fry bath, should have friable texture in the mouth, and be free of any raw spots. Excessive browning should be avoided in the product to prevent a dark color in the product which is not appealing to the consumer and to prevent deterioration of the nutritional quality of the product due to the browning reaction of the protein The pleasing taste which develops in the product is due in part to the controlled development of flavor by the browning reaction and in part by the adsorption of fat. The presence of fat in the product is essential for proper palatability; however, excess adsorption is not desirable since the energy content or caloric value of the resulting product is increased and the tendency of the product to develop fat oxidative rancidity is increased. Due to the low moisture content of the material entering the frying bath, the excessive pick-up of fat during the frying operation is prevented. During frying, the heat from the frying oil causes th water in the fried product to boil, resulting in a dehydrating action on the fried material. The water which leaves the product is replaced by fat from the frying bath resulting in a fried product which is lower in water and higher in fat than the origin starting material. By controlling the amount of water present in the starting material, a finished fried product can be produced which has a controlled fat content. By having less water to boil off during the frying operation, there is less water to be replac by fat in the product matrix.
The frying operation also heat gels the protein materia to a crisp sub-matrix which resists readsorption of water by the finished product. The gelled protein sub-matrix and the starch matrix which has been modified to resist water adsorbtion combine to produce a product which remains crisp for a long period of tim even at relatively high moisture content. By remaining crisp and resisting oxidative rancidity, a product can be produced which ha exceptional palatability, a long shelf life and storage stability, and which has a lower energy or caloric value than prior fat frie "snack products.
To assure that one having ordinary skill in the art wil understand this invention, the following examples are provided: Exam le 1 : A protein fortified potato snack chip was prepared from: Ingredients Parts by Weight Pre-gelatinized potato flakes 920 Isolated soy protein (Pvalston Purina Company Supro 610) 300 Salt 60 Glyceryl monpstearate 20 Water 720 By mixing the water, salt, and glyceryl raonostearate in an Oster blender and by mixing dry ingredients in a Hobart mixer, when blended, the wet ingredients were added to the dry ingredient and mixing was continued until the mass was free-flowing. The mix ture was then extruded on a De Francisci Press using a .050 by 1 inch ribbon die. Water at 165° F. was circulated in the extruder jacket; the extruded ribbon was stretched from 40 to 607o as it left the die. The ribbon was cut into 2 to 3 inch lengths and fried at 375° F. for about 45 seconds. The fried product had a light golden color and a highly pleasing taste with a very crisp mouthfeel and fiber texture.
Example 2: A potato snack type product was prepared as described in Example 1, but using: Ingredients Parts by Weight Pre-gelatinized potato flakes 720 Acid modified starch (Fry A Snack) 200 Isolated soy protein 300 Salt 60 Glyceryl monostearate 20 Water 720 The material was mixed, extruded as described in Example 1. The fried product had a crisp mouthfeel and pleasing taste similar to the product of Example 1.
Example 3: A wheat snack chip product was prepared as described in Example 1 by mixing: Ingredients Parts by Weight Pre-gelatinized wheat flakes 720 Fry A Snack 200 Isolated soy protein 300 Salt 60 Glyceryl monostearate 20 Water 720 The material was mixed, extruded and fried as described in Example 1. The prepared snack product was dark brown with a mild wheat flavor, had a friable texture with a very crisp mouthfeel and pleasing taste.
Example 4: A potato snack chip product was prepared as described in Example 1 from: Ingredients Parts by Weight Pre-gelatinized potato flakes 720 Isolated soy protein 300 Fry A Snack 200 Salt 60 Glyceryl monostearate 80 Water 720 The product was mixed, extruded and fried as in Example 1. The mixed dough was noticeably lump free and extruded very smoothly and produced an extremely stretchy, resilient ribbon. The product when fried was similar to that in Example 1, but was Example 5 : The experiment of Example 4 was repeated without any glyceryl monostearate being added to the product. The mixture was noticeably lumpy and the extruded ribbon did not stretch as well as the product in Example 4 or in Example 1. The fried product ballooned into a large hollow structure.
Example 6 ; Parallel runs to produce a potato snack chip product were conducted as described in Example 1, but using sodium caseina and lactalbumin as the protein sources. The fried snack chip products were similar to that as described in Example 1, but tended to darken quickly on frying and did not have as pleasing a taste as the product of Example 1.
Exam le 7 : A corn snack chip product was prepared by the method of Example 1 using: Ingredients Parts by Weight Pre-gelatinized alkali treated com flour 720 Fry A Snack 200 Isolated soy protein 300 Salt ) 60 Glyceryl monostearate 20 Water 720 The product was mixed, extruded and fried as described in Example 1. A light brown chip product was produced having a tortilla flavor with good crisp mouthfeel and flangible texture. Example 8 : Parallel runs were made to produce a potato snack chip product by mixing: Ingredients Parts .by Weight Pre-gelatinized potato flakes 41.0 Isolated soy protein 17.5 Fry A Snack 11.3 Salt 4.2 Glyceryl monostearate 1.3 Water 24.8 The products were mixed in a commercial ribbon blender until free-flowing and then extruded on a Johnson extruder throug a 0.040" by 12" die. The temperature of the product leaving the die was 170° F. The ribbon exiting the die was divided into 12 1 inch strips. Parallel runs were conducted, stretching the product 25%, 45%, 60%, 75%, and 85%. The product was cut into 2 inch sections and fried at 365° F. for 30 seconds. The product stretched 25% exhibited some blistering, but was an acceptable product. The product stretched 45% had very little blistering and the remaining products exhibited almost no blistering. The fried products had a light golden color, a pleasing potato flavor and very crisp mouthfeel and frangible texture. The product analyzed 20% by weight protein, 44.0% carbohydrates, 24.0% fats, and 3.2% water.
It is believed that one having ordinary skill in the art could alter the details of the process taught by the above descri tion to obtain the desired product. These variations are conside within the inventive concept which is limited only by the scope of the appended claims and the reasonable equivalents thereto.
Claims (12)
1. A process for producing a low calorie snack food product having Improved nutritional value* Improved palatabllity and stability on storage comprising mixing water, a source of pregelatinized starch, a starch modifying source, and a protein fortifying source which has not been subjected to the gelling action of heat, working the mixture and forming the mixture into a shaped food product without heat gelling the protelnaceous material, and frying the shaped product in an oil bath to produce a crisp texture in the shaped product and a low fat content in the fried product.
2. ¾e process of Claim 1 wherein the mixture contains between 16 and 25$ protelnaceous . material ·
3. · The process of Claim 1 wherein the mixture contains between 30 and 48$ water*
4. The process of Claim 1 wherein the mixture contains between 4l and h9$> starch source material.
5. · The process of Claim 1 wherein between 0.25 and 4.0$ of glyceryl monostearate is added to the mixture as the starch modifying source.
6. », The process of Claim 1 wherein the protelnaceous material is isolated soy protein.
7. · T e process of Claim 1 wherein the starch source material is potato flour. ,
8. The process of Claim 1 wherein a modified starch material is added to the mixture·
9. « The process of. Claim 1 wherein the fried product contains between 12 and 35$ fat. ■J SP-334 ■ir
10. A process for producing a crisp, fried snack food product having improved nutritional properties, increased palatability, and an increased shelf life under ambient storage conditions comprising mixing water, a source of pre-gelatinized potato starch, and a protein fortifying soybean isolate source which has not been substantially heat gelled to form a mixture containing between about 30 and 48% water, between about 41 and 49% pre-gelatinized starch, and between about 16 and 25% of protein, addi between about 0.25 and 4.0% of glyceryl monostearate and between about 0 and 15%> of a modified starch to the mixture, working the mixture to form a uniform mass and shaping the mass into a snack food shape without subjecting the protein in the mass to heat sufficient to substantially gel the protein, and frying the shape product in the presence of fat to produce a crisp snack food product containing between about 48 and 56%, starch, between about 16 and 25% protein, between about 2 and 6% moisture, and between about 12 and 35% fat.
11. A crisp fried snack food product having improved nutritional and storage properties and improved palatability comprising a crisp fried matrix of between about 48 and 56% starch, between about 2 and 6% moisture, between about 16 and 25% protein, and between about 12 and 35%, fat and protein matrix, the starch and protein matrix containing between about 0.25 and 4.0% of a starch modifying and complexing agent, the starch complexing agen and protein being distributed throughout the starch matrix to blo the hydrophilic sites on the starch molecules.
12. The product of Claim 11 wherein the protein is an isolated, soy protein.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US6455370A | 1970-08-17 | 1970-08-17 |
Publications (2)
Publication Number | Publication Date |
---|---|
IL37075A0 IL37075A0 (en) | 1971-08-25 |
IL37075A true IL37075A (en) | 1974-11-29 |
Family
ID=22056766
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
IL37075A IL37075A (en) | 1970-08-17 | 1971-06-16 | Protein fortified snack,process and product |
Country Status (9)
Country | Link |
---|---|
JP (1) | JPS516736B2 (en) |
BE (1) | BE771104A (en) |
CA (1) | CA962512A (en) |
FR (1) | FR2104030A5 (en) |
GB (1) | GB1358097A (en) |
IL (1) | IL37075A (en) |
LU (1) | LU63713A1 (en) |
NL (1) | NL152442B (en) |
SE (1) | SE382906B (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2280325A1 (en) * | 1974-08-02 | 1976-02-27 | Bel La Vache Qui Rit Fromage | Expanded food products - by heating and extruding mixture of proteins glucides having accurately controlled composition |
GB2074436B (en) * | 1980-04-26 | 1983-10-05 | Howard A N | Cereal snackfoods and compositions and methods for making the same |
WO2001089325A1 (en) * | 2000-05-24 | 2001-11-29 | Allouche Reginald | High protein and low calorie raw batter for making products resembling potato-based products, and method for preparing same |
EP1788895B1 (en) * | 2004-07-19 | 2012-08-15 | The Procter and Gamble Company | Low carbohydrate snack food |
JP6337191B1 (en) * | 2017-10-20 | 2018-06-06 | 森永製菓株式会社 | Low-sugar baked snack food |
-
1971
- 1971-06-08 CA CA115,127A patent/CA962512A/en not_active Expired
- 1971-06-16 IL IL37075A patent/IL37075A/en unknown
- 1971-08-05 FR FR7128819A patent/FR2104030A5/fr not_active Expired
- 1971-08-09 NL NL717110950A patent/NL152442B/en not_active IP Right Cessation
- 1971-08-09 BE BE771104A patent/BE771104A/en unknown
- 1971-08-12 JP JP46060666A patent/JPS516736B2/ja not_active Expired
- 1971-08-13 LU LU63713A patent/LU63713A1/xx unknown
- 1971-08-16 SE SE7110408A patent/SE382906B/en unknown
- 1971-08-17 GB GB3858871A patent/GB1358097A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE2140859A1 (en) | 1972-03-16 |
FR2104030A5 (en) | 1972-04-14 |
IL37075A0 (en) | 1971-08-25 |
NL152442B (en) | 1977-03-15 |
BE771104A (en) | 1971-12-16 |
NL7110950A (en) | 1972-02-21 |
JPS475266A (en) | 1972-03-16 |
CA962512A (en) | 1975-02-11 |
LU63713A1 (en) | 1972-04-05 |
SE382906B (en) | 1976-02-23 |
GB1358097A (en) | 1974-06-26 |
JPS516736B2 (en) | 1976-03-02 |
DE2140859B2 (en) | 1974-04-18 |
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