Patent Application
20080069927
The application file contains at least one photograph executed in color. Copies of this patent application publication with color photographs will be provided by the Office upon request and payment of the necessary fee.
The present invention provides simulated seafood compositions. Typically, the simulated seafood composition will comprise structured plant protein products and fatty acids. Alternatively, the simulated seafood composition will further comprise seafood meat. In one embodiment, the simulated seafood composition will comprise structured plant protein products having protein fibers that are substantially aligned. In another embodiment, the simulated seafood composition will comprise coloring systems such that the simulated seafood composition has the color and texture of seafood meat. In addition, the simulated seafood composition also generally has the flavor, texture, and smell of seafood meat. Further, the simulated seafood composition can have levels of omega-3 fatty acids typically found in seafood rich in omega-3 fatty acids.
The seafood compositions and simulated seafood compositions of the invention each comprise structured plant protein products comprising protein fibers that are substantially aligned, as described in more detail in I(c) below. In an exemplary embodiment, the structured plant protein products are extrudates of plant materials that have been subjected to the extrusion process detailed in I(b) below. Because the structured plant protein products utilized the invention have protein fibers that are substantially aligned in a manner similar to seafood meat, the seafood compositions and simulated seafood compositions generally have the texture and feel of compositions containing all seafood meat.
A variety of ingredients that contain protein may be utilized in an extrusion process to produce structured plant protein products suitable for use in the invention. While ingredients comprising proteins derived from plants are typically used, it is also envisioned that proteins derived from other sources, such as animal sources, may be utilized without departing from the scope of the invention. For example, a dairy protein selected from the group consisting of casein, caseinates, whey protein, milk protein concentrate, milk protein isolate, and mixtures thereof may be utilized. In an exemplary embodiment, the dairy protein is whey protein. By way of further example, an egg protein selected from the group consisting of ovalbumin, ovoglobulin, ovomucin, ovomucoid, ovotransferrin, ovovitelia, ovovitellin, albumin globulin, and vitellin may be utilized.
It is envisioned that other ingredient types in addition to proteins may be utilized. Not limiting examples of such ingredients include sugars, starches, oligosaccharides, soy fiber and other dietary fibers, and gluten.
It is also envisioned that the protein-containing starting materials may be gluten-free. Because gluten is typically used in filament formation during the extrusion process, if a gluten-free starting material is used, an edible crosslink agent may be utilized to facilitate filament formation. Non-limiting examples of suitable crosslink agents include Konjac glucomannan (KGM) flour, edible crosslink agents, Pureglucan manufactured by Takeda (USA), calcium salts, and magnesium salts. One skilled in the art can readily determine the amount of cross linker needed, if any, in gluten-free embodiments.
Irrespective of its source or ingredient classification, the ingredients utilized in the extrusion process are typically capable of forming structured plant protein products having protein fibers that are substantially aligned. Suitable examples of such ingredients are detailed more fully below.
In an exemplary embodiment, at least one ingredient derived from a plant will be utilized to form the protein-containing materials. Generally speaking, the ingredient will comprise a protein. The amount of protein present in the ingredient(s) utilized can and will vary depending upon the application. For example, the amount of protein present in the ingredient(s) utilized may range from about 40% to about 100% by weight. In another embodiment, the amount of protein present in the ingredient(s) utilized may range from about 50% to about 100% by weight. In an additional embodiment, the amount of protein present in the ingredient(s) utilized may range from about 60% to about 100% by weight. In a further embodiment, the amount of protein present in the ingredient(s) utilized may range from about 70% to about 100% by weight. In still another embodiment, the amount of protein present in the ingredient(s) utilized may range from about 80% to about 100% by weight. In a further embodiment, the amount of protein present in the ingredient(s) utilized may range from about 90% to about 100% by weight.
The ingredient(s) utilized in extrusion may be derived from a variety of suitable plants. By way of non-limiting example, suitable plants include legumes, corn, peas, canola, sunflowers, sorghum, rice, amaranth, potato, tapioca, arrowroot, canna, lupin, rape seed, wheat, oats, rye, barley, and mixtures thereof.
In one embodiment, the ingredients are isolated from wheat and soybeans. In another exemplary embodiment, the ingredients are isolated from soybeans. Suitable wheat derived protein-containing ingredients include wheat gluten, wheat flour, and mixtures thereof. An example of commercially available wheat gluten that may be utilized in the invention is Gem of the West Vital Wheat Gluten, either regular or organic, available from Manildra Milling (Shawnee Mission, Kans.). Suitable soybean derived protein-containing ingredients (“soy protein material”) include soy protein isolate, soy protein concentrate, soy flour, and mixtures thereof, each of which are detailed below. In each of the foregoing embodiments, the soybean material may be combined with one or more ingredients selected from the group consisting of a starch, flour, gluten, a dietary fiber, and mixtures thereof.
Suitable examples of protein-containing material isolated from a variety of sources are detailed in Table A, which shows various combinations.
In each of the embodiments delineated in Table A, the combination of protein-containing materials may be combined with one or more ingredients selected from the group consisting of a starch, flour, gluten, a dietary fiber, and mixtures thereof. In one embodiment, the protein-containing material comprises protein, starch, gluten, and fiber. In an exemplary embodiment, the protein-containing material comprises from about 45% to about 65% soy protein on a dry matter basis; from about 20% to about 30% wheat gluten on a dry matter basis; from about 10% to about 15% wheat starch on a dry matter basis; and from about 1% to about 5% starch on a dry matter basis. In each of the foregoing embodiments, the protein-containing material may comprise dicalcium phosphate, L-cysteine or combinations of both dicalcium phosphate and L-cysteine.
In an exemplary embodiment, as detailed above, soy protein isolate, soy protein concentrate, soy flour, and mixtures thereof may be utilized in the extrusion process. The soy protein materials may be derived from whole soybeans in accordance with methods generally known in the art. The whole soybean may be standard soybeans (i.e., non genetically modified soybeans), commoditized soybeans, hybridized soybeans, genetically modified soybeans, and combinations thereof.
Generally speaking, when soy isolate is used, an isolate is preferably selected that is not a highly hydrolyzed soy protein isolate. In certain embodiments, highly hydrolyzed soy protein isolates, however, may be used in combination with other soy protein isolates provided that the highly hydrolyzed soy protein isolate content of the combined soy protein isolates is generally less than about 40% of the combined soy protein isolates, by weight. Examples of soy protein isolates that are useful in the present invention are commercially available, for example, from Solae, LLC (St. Louis, Mo.), and include SUPRO® 500E, SUPRO® EX 33, SUPRO® 620, and SUPRO® 545. In an exemplary embodiment, a form of SUPRO® 620 is utilized as detailed in Example 5.
Alternatively, soy protein concentrate or soy flour may be blended with the soy protein isolate to substitute for a portion of the soy protein isolate as a source of soy protein material. Typically, if a soy protein concentrate is substituted for a portion of the soy protein isolate, the soy protein concentrate is substituted for up to about 40% of the soy protein isolate by weight, at most, and more preferably is substituted for up to about 30% of the soy protein isolate by weight. Examples of suitable soy protein concentrates useful in the invention include Procon, Alpha 12 and Alpha 5800, which are commercially available from Solae, LLC (St. Louis, Mo.). If a soy flour is substituted for a portion of the soy protein isolate, the soy flour is substituted for up to about 35% of the soy protein isolate by weight. The soy flour should be a high protein dispersibility index (PDI) soy flour.
Any fiber known in the art that will work in the application can be used as the fiber source. Soy cotyledon fiber may be utilized as a fiber source. Suitable soy cotyledon fiber will generally effectively bind water when the mixture of soy protein and soy cotyledon fiber is extruded. In this context, “effectively bind water” generally means that the soy cotyledon fiber has a water holding capacity of at least 5.0 to about 8.0 grams of water per gram of soy cotyledon fiber, and preferably the soy cotyledon fiber has a water holding capacity of at least about 6.0 to about 8.0 grams of water per gram of soy cotyledon fiber. When present in the soy protein material, soy cotyledon fiber may be present in an amount ranging from about 1% to about 20%, preferably from about 1.5% to about 20% and most preferably, at from about 2% to about 5% by weight on a moisture free basis. Suitable soy cotyledon fiber is commercially available. For example, FIBRIM® 1260 and FIBRIM® 2000 are soy cotyledon fiber materials that are commercially available from Solae, LLC (St. Louis, Mo.).
A variety of additional ingredients may be added to any of the combinations of protein-containing materials above without departing from the scope of the invention. For example, antioxidants, antimicrobial agents, and combinations thereof may be included. Antioxidant additives include BHA, BHT, TBHQ, vitamins A, C and E and derivatives, and various plant extracts such as those containing carotenoids, tocopherols or flavonoids having antioxidant properties, may be included to increase the shelf-life or nutritionally enhance the seafood compositions or simulated seafood compositions. The antioxidants and the antimicrobial agents may have a combined presence at levels of from about 0.01% to about 10%, preferably, from about 0.05% to about 5%, and more preferably from about 0.1% to about 2%, by weight of the protein-containing materials that will be extruded.
As will be appreciated by the skilled artisan, the moisture content of the protein-containing materials can and will vary depending upon the extrusion process. Generally speaking, the moisture content may range from about 1% to about 80% by weight. In low moisture extrusion applications, the moisture content of the protein-containing materials may range from about 1% to about 35% by weight. Alternatively, in high moisture extrusion applications, the moisture content of the protein-containing materials may range from about 35% to about 80% by weight. In an exemplary embodiment, the extrusion application utilized to form the extrudates is low moisture. An exemplary example of a low moisture extrusion process to produce extrudates having proteins with fibers that are substantially aligned is detailed in I(b) and Example 5.
A suitable extrusion process for the preparation of a structured plant protein product comprises introducing the plant protein material and other ingredients into a mixing tank (i.e., an ingredient blender) to combine the ingredients and form a dry blended plant protein material pre-mix. The dry blended plant protein material pre-mix is then transferred to a hopper from which the dry blended ingredients are introduced along with moisture into a pre-conditioner to form a conditioned plant protein material mixture. The conditioned material is then fed to an extruder in which the plant protein material mixture is heated under mechanical pressure generated by the screws of the extruder to form a molten extrusion mass. The molten extrusion mass exits the extruder through an extrusion die.
Among the suitable extrusion apparatuses useful in the practice of the present invention is a double barrel, twin-screw extruder as described, for example, in U.S. Pat. No. 4,600,311. Further examples of suitable commercially available extrusion apparatuses include a CLEXTRAL Model BC-72 extruder manufactured by Clextral, Inc. (Tampa, Fla.); a WENGER Model TX-57 extruder, a WENGER Model TX-168 extruder, and a WENGER Model TX-52 extruder all manufactured by Wenger Manufacturing, Inc. (Sabetha, Kans.). Other conventional extruders suitable for use in this invention are described, for example, in U.S. Pat. Nos. 4,763,569, 4,118,164, and 3,117,006, which are hereby incorporated by reference in their entirety. A single-screw extruder could also be used in the present invention. Examples of suitable commercially available single-screw extrusion apparatuses include the Wenger X-175, the Wenger X-165, and the Wenger X-85 all of which are available from Wenger Manufacturing, Inc.
The screws of a twin-screw extruder can rotate within the barrel in the same or opposite directions. Rotation of the screws in the same direction is referred to as single flow or co-rotating whereas rotation of the screws in opposite directions is referred to as double flow or counter-rotating. The speed of the screw or screws of the extruder may vary depending on the particular apparatus; however, it is typically from about 250 to about 450 revolutions per minute (rpm). Generally, as the screw speed increases, the density of the extrudate will decrease. The extrusion apparatus contains screws assembled from shafts and worm segments, as well as mixing lobe and ring-type shearing elements as recommended by the extrusion apparatus manufacturer for extruding plant protein material.
The extrusion apparatus generally comprises a plurality of heating zones through which the protein mixture is conveyed under mechanical pressure prior to exiting the extrusion apparatus through an extrusion die. The temperature in each successive heating zone generally exceeds the temperature of the previous heating zone by between about 10° C. to about 70° C. In one embodiment, the conditioned pre-mix is transferred through four heating zones within the extrusion apparatus, with the protein mixture heated to a temperature of from about 100° C. to about 150° C. such that the molten extrusion mass enters the extrusion die at a temperature of from about 100° C. to about 150° C. There is no active heating or cooling necessary. Typically, temperature changes are due to work input and can happen suddenly.
The pressure within the extruder barrel is typically about 50 psig to about 500 psig, preferably between about 75 psig to about 200 psig. Generally the pressure within the last two heating zones is from about 100 psig to about 3000 psig. The barrel pressure is dependent on numerous factors including, for example, the extruder screw speed, feed rate of the mixture to the barrel, feed rate of water to the barrel, and the viscosity of the molten mass within the barrel.
Water is injected into the extruder barrel to hydrate the plant protein material mixture and promote texturization of the proteins. As an aid in forming the molten extrusion mass, the water may act as a plasticizing agent. Water may be introduced to the extruder barrel via one or more injection jets. Typically, the mixture in the barrel contains from about 15% to about 35% by weight water. The rate of introduction of water to any of the heating zones is generally controlled to promote production of an extrudate having desired characteristics. It has been observed that as the rate of introduction of water to the barrel decreases, the density of the extrudate decreases. Typically, less than about 1 kg of water per kg of protein is introduced to the barrel. Preferably, from about 0.1 kg to about 1 kg of water per kg of protein are introduced to the barrel.
In a pre-conditioner, the plant protein material and other ingredients can be preheated, contacted with moisture, and held under controlled temperature and pressure conditions to allow the moisture to penetrate and soften the individual particles. The preconditioner contains one or more paddles to promote uniform mixing of the protein and transfer of the protein mixture through the preconditioner. The configuration and rotational speed of the paddles vary widely, depending on the capacity of the preconditioner, the extruder throughput and/or the desired residence time of the mixture in the preconditioner or extruder barrel. Generally, the speed of the paddles is from about 100 to about 1300 revolutions per minute (rpm). Agitation must be high enough to obtain even hydration and good mixing.
Typically, the protein-containing material mixture is pre-conditioned prior to introduction into the extrusion apparatus by contacting the pre-mix with moisture (i.e., steam and/or water). Preferably the protein-containing mixture is heated to a temperature of from about 25° C. to about 80° C., more preferably from about 30° C. to about 40° C. in the preconditioner.
Typically, the plant protein material pre-mix is conditioned for a period of about 30 to about 60 seconds, depending on the speed and the size of the conditioner. The plant protein material pre-mix is contacted with steam and/or water and heated in the pre-conditioner at generally constant steam flow to achieve the desired temperatures. The water and/or steam conditions (i.e., hydrates) the plant protein material mixture, increases its density, and facilitates the flowability of the dried mix without interference prior to introduction to the extruder barrel where the proteins are texturized. If a low moisture plant protein material is desired, the conditioned pre-mix may contain from about 1% to about 35% (by weight) water. If a high moisture plant protein material is desired, the conditioned pre-mix may contain from about 35% to about 80% (by weight) water.
The conditioned pre-mix typically has a bulk density of from about 0.25 g/cm3 to about 0.6 g/cm3. Generally, as the bulk density of the pre-conditioned protein mixture increases within this range, the protein mixture is easier to process.
The conditioned pre-mix is then fed into an extruder to heat, shear, and ultimately plasticize the mixture. The extruder may be selected from any commercially available extruder and may be a single-screw extruder or preferably a twin-screw extruder that mechanically shears the mixture with the screw elements.
Whichever extruder is used, it should be run in excess of about 50% motor load. Typically the conditioned pre-mix is introduced to the extrusion apparatus at a rate of between about 16 kilograms per minute to about 60 kilograms per minute. More preferably, the conditioned pre-mix is introduced to the extrusion apparatus at a rate of between about 26 kilograms per minute to about 32 kilograms per minute. Generally, it has been observed that the density of the extrudate decreases as the feed rate of pre-mix to the extruder increases.
The protein mixture is subjected to shear and pressure by the extruder to plasticize the mixture. The screw elements of the extruder shear the mixture as well as create pressure in the extruder by forcing the mixture forwards though the extruder and through the die. The screw motor speed determines the amount of shear and pressure applied to the mixture by the screw(s). Preferably, the screw motor speed is set to a speed of from about 200 rpm to about 500 rpm, and more preferably from about 300 rpm to about 450 rpm, which moves the mixture through the extruder at a rate of at least about 20 kilograms per minute, and more preferably at least about 40 kilograms per minute. Preferably the extruder generates an extruder barrel exit pressure of from about 50 psig to about 3000 psig.
The extruder heats the protein mixture as it passes through the extruder denaturing the protein in the mixture. The extruder includes a means for heating the mixture to temperatures of from about 100° C. to about 180° C. Preferably the means for heating the mixture in the extruder comprises extruder barrel jackets into which heating or cooling media such as steam or water may be introduced to control the temperature of the mixture passing through the extruder. The extruder may also include steam injection ports for directly injecting steam into the mixture within the extruder. The extruder preferably includes multiple heating zones that can be controlled to independent temperatures, where the temperatures of the heating zones are preferably set to increase the temperature of the mixture as it proceeds through the extruder. For example, the extruder may be set in a four temperature zone arrangement, where the first zone (adjacent the extruder inlet port) is set to a temperature of from about 80° C. to about 100° C., the second zone is set to a temperature of from about 100° C. to 135° C., the third zone is set to a temperature of from 135° C. to about 150° C., and the fourth zone (adjacent the extruder exit port) is set to a temperature of from 150° C. to 180° C. The extruder may be set in other temperature zone arrangements, as desired. For example, the extruder may be set in a five temperature zone arrangement, where the first zone is set to a temperature of about 25° C., the second zone is set to a temperature of about 50° C., the third zone is set to a temperature of about 95° C., the fourth zone is set to a temperature of about 130° C., and the fifth zone is set to a temperature of about 150° C.
The mixture forms a melted plasticized mass in the extruder. A die assembly is attached to the extruder in an arrangement that permits the plasticized mixture to flow from the extruder exit port into the die assembly, wherein the die assembly consists of a die and a back plate. Additionally, the die assembly produces substantial alignment of the protein fibers within the plasticized mixture as it flows through the die assembly. The back plate in combination with the die create at least one central chamber that receives the melted plasticized mass from the extruder through at least one central opening. From the at least one central chamber, the melted plasticized mass is directed by flow directors into at least one elongated tapered channel. Each elongated tapered channel leads directly to an individual die aperture. The extrudate exits the die through at least one aperture in the periphery or side of the die assembly at which point the protein fibers contained within are substantially aligned. It is also contemplated that the extrudate may exit the die assembly through at least one aperture in the die face, which may be a die plate affixed to the die.
The width and height dimensions of the die aperture(s) are selected and set prior to extrusion of the mixture to provide the fibrous material extrudate with the desired dimensions. The width of the die aperture(s) may be set so that the extrudate resembles from a cubic chunk of meat to a steak filet, where widening the width of the die aperture(s) decreases the cubic chunk-like nature of the extrudate and increases the filet-like nature of the extrudate. Preferably the width of the die aperture(s) is/are set to a width of from about 5 millimeters to about 40 millimeters.
The height dimension of the die aperture(s) may be set to provide the desired thickness of the extrudate. The height of the aperture(s) may be set to provide a very thin extrudate or a thick extrudate. Preferably, the height of the die aperture(s) may be set to from about 1 millimeter to about 30 millimeters, and more preferably from about 8 millimeters to about 16 millimeters.
It is also contemplated that the die aperture(s) may be round. The diameter of the die aperture(s) may be set to provide the desired thickness of the extrudate. The diameter of the aperture(s) may be set to provide a very thin extrudate or a thick extrudate. Preferably, the diameter of the die aperture(s) may be set to from about 1 millimeter to about 30 millimeters, and more preferably from about 8 millimeters to about 16 millimeters.
The extrudate can be cut after exiting the die assembly. Suitable apparatuses for cutting the extrudate after it exits the die assembly include flexible knives manufactured by Wenger Manufacturing, Inc. (Sabetha, Kans.) and Clextral, Inc. (Tampa, Fla.). Alternatively, a delayed cut can be done to the extrudate. One such example of a delayed cut device is a guillotine device.
The dryer, if one is used, generally comprises a plurality of drying zones in which the air temperature may vary. The extrudate will be present in the dryer for a time sufficient to provide an extrudate having a desired moisture content. Thus, the temperature of the air is not important, if a lower temperature is used, longer drying times will be required than if a higher temperature is used. Generally, the temperature of the air within one or more of the zones will be from about 100° C. to about 185° C. At such temperatures, the extrudate is generally dried for at least about 5 minutes and more generally, for at least about 10 minutes. Suitable dryers include those manufactured by Wolverine Proctor & Schwartz (Merrimac, Mass.), National Drying Machinery Co. (Philadelphia, Pa.), Wenger (Sabetha, Kans.), Clextral (Tampa, Fla.), and Buehler (Lake Bluff, Ill.).
The desired moisture content may vary widely depending on the intended application of the extrudate. Generally speaking, the extruded material has a moisture content of from about 6% to about 13% by weight, if dried. Although not required in order to separate the fibers, hydrating in water until the water is absorbed is one way to separate the fibers. If the protein material is not dried or not fully dried, its moisture content is higher, generally from about 16% to about 30% by weight, on a moisture free basis.
The dried extrudate may further be comminuted to reduce the average particle size of the extrudate. Suitable grinding or processing apparatus include hammer mills such as Mikro Hammer Mills manufactured by Hosokawa Micron Ltd. (England), Fitzmill® manufactured by The Fitzpatrick Company (Elmhurst, Ill.), Comitrol® processors made by Urschel Laboratories (Valparaiso, Ind.), and roller mills such as Rosskamp Roller Mills manufactured by RossKamp Champion (Waterloo, Iowa). The size of the particles can and will vary depending upon the seafood or seafood preparation to be simulated. As an example, structured plant protein products may be cut into chunks, which have dimensions of not less than 1.2 cm in each direction and in which the original substantially aligned protein fibers are retained. Alternatively, structured plant protein products may also be cut into flakes, which have dimensions less than 1.2 cm in each direction but in which the aligned protein fibers are essentially retained. Furthermore, structured plant protein products may be grated or shredded, in which discrete particles of uniform size are produced.
The extrudates produced in I(b) typically comprise the structured plant protein products comprising protein fibers that are substantially aligned. In the context of this invention “substantially aligned” generally refers to the arrangement of protein fibers such that a significantly high percentage of the protein fibers forming the structured plant protein product are contiguous to each other at less than approximately a 45° angle when viewed in a horizontal plane. Typically, an average of at least 55% of the protein fibers comprising the structured plant protein product are substantially aligned. In another embodiment, an average of at least 60% of the protein fibers comprising the structured plant protein product are substantially aligned. In a further embodiment, an average of at least 70% of the protein fibers comprising the structured plant protein product are substantially aligned. In an additional embodiment, an average of at least 80% of the protein fibers comprising the structured plant protein product are substantially aligned. In yet another embodiment, an average of at least 90% of the protein fibers comprising the structured plant protein product are substantially aligned Methods for determining the degree of protein fiber alignment are known in the art and include visual determinations based upon micrographic images. By way of example,
In addition to having protein fibers that are substantially aligned, the structured plant protein products also typically have shear strength substantially similar to whole meat muscle. In this context of the invention, the term “shear strength” provides one means to quantify the formation of a sufficient fibrous network to impart whole-muscle like texture and appearance to the plant protein product. Shear strength is the maximum force in grams needed to puncture through a given sample. A method for measuring shear strength is described in Example 3. Generally speaking, the structured plant protein products of the invention will have average shear strength of at least 1400 grams. In an additional embodiment, the structured plant protein products will have average shear strength of from about 1500 to about 1800 grams. In yet another embodiment, the structured plant protein products will have average shear strength of from about 1800 to about 2000 grams. In a further embodiment, the structured plant protein products will have average shear strength of from about 2000 to about 2600 grams. In an additional embodiment, the structured plant protein products will have average shear strength of at least 2200 grams. In a further embodiment, the structured plant protein products will have average shear strength of at least 2300 grams. In yet another embodiment, the structured plant protein products will have average shear strength of at least 2400 grams. In still another embodiment, the structured plant protein products will have average shear strength of at least 2500 grams. In a further embodiment, the structured plant protein products will have average shear strength of at least 2600 grams.
A means to quantify the size of the protein fibers formed in the structured plant protein products may be done by a shred characterization test. Shred characterization is a test that generally determines the percentage of large pieces formed in the structured plant protein product. In an indirect manner, percentage of shred characterization provides an additional means to quantify the degree of protein fiber alignment in a structured plant protein product. Generally speaking, as the percentage of large pieces increases, the degree of protein fibers that are aligned within a structured plant protein product also typically increases. Conversely, as the percentage of large pieces decreases, the degree of protein fibers that are aligned within a structured plant protein product also typically decreases. A method for determining shred characterization is detailed in Example 4. The structured plant protein products of the invention typically have an average shred characterization of at least 10% by weight of large pieces. In a further embodiment, the structured plant protein products have an average shred characterization of from about 10% to about 15% by weight of large pieces. In another embodiment, the structured plant protein products have an average shred characterization of from about 15% to about 20% by weight of large pieces. In yet another embodiment, the structured plant protein products have an average shred characterization of from about 20% to about 50% by weight of large pieces. In another embodiment, the average shred characterization is at least 20% by weight, at least 21% by weight, at least 22% by weight, at least 23% by weight, at least 24% by weight, at least 25% by weight, or at least 26% by weight large pieces.
Suitable structured plant protein products of the invention generally have protein fibers that are substantially aligned, have average shear strength of at least 1400 grams, and have an average shred characterization of at least 10% by weight large pieces. More typically, the structured plant protein products will have protein fibers that are at least 55% aligned, have average shear strength of at least 1800 grams, and have an average shred characterization of at least 15% by weight large pieces. In exemplary embodiment, the structured plant protein products will have protein fibers that are at least 55% aligned, have average shear strength of at least 2000 grams, and have an average shred characterization of at least 17% by weight large pieces. In another exemplary embodiment, the structured plant protein products will have protein fibers that are at least 55% aligned, have average shear strength of at least 2200 grams, and have an average shred characterization of at least 20% by weight large pieces.
The simulated seafood composition, in addition to structured plant protein products, also comprises fatty acids. The fatty acid will generally range in length from about 10 to 26 carbon atoms, and preferably in the range of 18 to 22 carbons. The fatty acid may be a saturated fatty acid or an unsaturated fatty acid. The unsaturated fatty acid may be monounsaturated or polyunsaturated. The polyunsaturated fatty acid (PUFA) may be an omega-3 fatty acid in which the first double bond occurs in the third carbon-carbon bond from the methyl end (opposite the acid group) of the carbon chain. Examples of omega-3 fatty acids include alpha-linolenic acid (18:3, ALA), stearidonic acid (18:4, SDA), eicosatetraenoic acid (20:4), eicosapentaenoic acid (20:5; EPA), and docosahexaenoic acid (22:6; DHA). The PUFA may be an omega-6 fatty acid, in which the first double bond occurs in the sixth carbon-carbon bond from the methyl end. Examples of omega-6 fatty acids include linoleic acid (18:2), gamma-linolenic acid (18:3), eicosadienoic acid (20:2), dihomo-gamma-linolenic acid (20:3), arachidonic acid (20:4), docosadienoic acid (22:2), adrenic acid (22:4), and docosapentaenoic acid (22:5). The fatty acid may be an omega-9 fatty acid, such as oleic acid (18:1), eicosenoic acid (20:1), mead acid (20:3), erucic acid (22:1), and nervonic acid (24:1). The fatty acid may be one of the aforementioned fatty acids or a combination of the aforementioned fatty acids.
The fatty acid will be an essentially pure fatty acid that is devoid of contaminants and odorants. The fatty acid may be derived from an appropriate plant or seafood source. PUFAs and, in particular, omega-3 and omega-6 fatty acids are primarily found in plants and seafood. The ratio of omega-3 to omega-6 fatty acids in seafood ranges from about 8:1 to 20:1. Seafood rich in omega-3 fatty acids include anchovies, catfish, clams, cod, herring, lake trout, mackerel, salmon, sardines, shrimp, and tuna.
The concentration of the fatty acid in the simulated seafood compositions may range from about 0.0001% to about 1%, and preferably from about 0.001% to about 0.05%.
The simulated seafood composition, in addition to structured plant protein products and fatty acids, may also comprise seafood meat. Generally speaking, the seafood meat may be obtained from a variety of seafood species suitable for human consumption. Suitable examples of seafood include fish, both fresh water and salt water fish, such as amberjack, anchovies, bluefish, bonito, bowfin, bream, buffalofish, burbot, butterfish, carp, catfish, crevalle jack, cobia, cod, croaker, cusk, eel, gar, grouper, flounder (arrowtooth, southern, starry, summer, winter, witch, yellowtail), haddock, jewfish, kingfish, lake chub, lake herring, lake sturgeon, lake whitefish, lingcod, mackerel (Atlantic, king, Spanish), mahi mahi, monkfish, mullet, muskie, pike, orange roughy, Pacific sand dab, paddlefish, perch, pollock, pompano, rockfish, sable, salmon (Atlantic, chum, Chinook, coho or silver, pink, sockeye or red), sauger, sculp, sea bass (black, giant, white), sea dab, shark, sheepshead, smelt, snakehead, snapper (red, mangrove, vermillion, yellowtail), snook, sole (Dover, English, Petrale, Rex, rock), spot, spotted cabrilla, bass, sturgeon, swordfish, tautog, tilefish, turbot, trout (brook, lake, rainbow, sea, white sea), tuna (albacore, Atlantic bluefin, big eye, blackfin, skipjack, southern bluefin, tongol, yellowtail), walleye, crappie, whiting, and wolfish. Seafood also includes shellfish and crustaceans such as crabs (Alaskan, blue, Dungeness, Jonah, red, softshell, snow) clams (butter, Goeduck, hard, littleneck, razor, steamer), shrimp (blue, brown, California, Key West, northern, pink, rock, tiger, white), lobster (American, rock, slipper, spiny), mollusks (abalone, cockle, conch, welk), mussels (blue, California, green lip), octopus, oysters (Apalachicola, Atlantic, gulf, Olympia, Pacific, soft American), scallops (bay, calico, sea), and squid.
The seafood meat may be fresh or cooked before it is added to the simulated seafood composition. The seafood meat may include animal flesh trim and animal tissues derived from processing such as the frozen residue from sawing frozen fish. Seafood meat may also include fish skin and mechanically separated fish. The seafood meat may be cooked by steam, water, oil, hot air, smoke, or a combination thereof. The seafood meat is generally heated until the internal temperature is between 60° C. and 85° C. The simulated seafood composition comprising structured plant protein products and seafood meat may or may not be cooked further prior to or during packaging.
Typically, the amount of structured plant protein product in relation to the amount of seafood meat in the simulated seafood composition can and will vary depending upon the composition's intended use. By way of example, when a significantly vegetarian composition that has a relatively small degree of seafood flavor is desired, the concentration of seafood meat in the simulated seafood composition may be about 45%, 40%, 35%, 30%, 25%, 20%, 15%, 10%, 5%, 2%, or 0% by weight. Alternatively, when a simulated seafood composition having a relatively high degree of seafood flavor or seafood meat is desired, the concentration of seafood meat in the simulated seafood composition may be about 50%, 55%, 60%, 65%, 70%, or 75% by weight. Consequently, the concentration of structured plant protein product in the simulated seafood composition may be about 25%, 30%, 35%, 40%, 45%, 50%, 55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, 95%, or 99% by weight.
Another aspect of the invention provides a simulated seafood composition, which further comprises an appropriate colorant. The simulated seafood compositions may further comprise antioxidants, flavoring agents, or additional nutrients.
The structured plant protein products generally will be colored to resemble the color of the seafood flesh it will simulate in the simulated seafood composition. In one embodiment, the structured plant protein product will be colored to resemble retorted tuna meat or salmon meat. In another embodiment, the structured plant protein product will be colored to resemble chopped shrimp. The composition of the structured plant protein product was described above in I(a). The structured plant protein product used in the simulated seafood composition, as an exemplary example, may comprise soy protein and wheat protein.
The structured plant protein products may be colored with a natural colorant, a combination of natural colorants, an artificial colorant, a combination of artificial colorants, or a combination of natural and artificial colorants. Suitable examples of natural colorants include annatto (reddish-orange), anthocyanins (red, purple, bleu), beet juice, beta-carotene (yellow to orange), beta-APO 8 carotenal (orange to red), black currant, burnt sugar; canthaxanthin (orange), caramel, carmine/carminic acid (magenta, pink, red), carrot, cochineal extract (magenta, pink, red), curcumin (yellow-orange); grape, hibiscus (blue-red), lac red, lutein (yellow); monascus red, paprika, red cabbage juice, redfruit, riboflavin (yellow-orange), saffron, titanium dioxide (white), and turmeric (yellow-orange). Examples of FDA-approved artificial colorants include FD&C (Food Drug & Cosmetics) Red No. 3 (Erythrosine), Red No. 40 (Allura Red AC), Yellow No. 5 (Tartrazine), Yellow No. 6 (Sunset Yellow), Blue No. 1 (Brilliant Blue FCF), and Blue No. 2 (Indigotine). Food colorants may be dyes, which are powders, granules, or liquids that are soluble in water. Alternatively, natural and artificial food colorants may be lake colors, which are combinations of dyes and insoluble materials. Lake colors are not oil soluble, but are oil dispersible; they tint by dispersion.
The type of colorant or colorants and the concentration of the colorant or colorants will be adjusted to match the color of the seafood meat to be simulated. The final concentration of a natural food colorant in a simulated seafood composition may range from about 0.01% percent to about 4% by weight, preferably in the range from about 0.03% to about 2% by weight, and more preferably in the range from about 0.1% to about 1% by weight. The final concentration of an artificial food colorant in a simulated seafood composition may range from about 0.000001% to about 0.2% by weight, preferably in the range from about 0.00001% to about 0.02% by weight, and more preferably in the range from about 0.0001% to about 0.002% by weight.
During the coloring process, the structured plant protein products are generally mixed with water to rehydrate the structured plant protein product. The amount of water added to the plant protein product can and will vary. The ratio of water to structured plant protein product may range from about 1:1 to about 10:1. In a preferred embodiment, the ration of water to structured plant protein product may range from about 2:1 to about 3:1.
The coloring system may further comprise an acidity regulator to maintain the pH in the optimal range for the colorant. The acidity regulator may be an acidulent. Examples of acidulents that may be added to food include citric acid, acetic acid (vinegar), tartaric acid, malic acid, fumaric acid, lactic acid, phosphoric acid, sorbic acid, and benzoic acid. The final concentration of the acidulent in a simulated seafood composition may range from about 0.001% to about 5% by weight. The final concentration of the acidulent may range from about 0.01% to about 2% by weight. The final concentration of the acidulent may range from about 0.1% to about 1% by weight. The acidity regulator may also be a pH-raising agent, such as disodium diphosphate.
The simulated seafood composition may further comprise an antioxidant. The antioxidant may prevent the oxidation of the polyunsaturated fatty acids (e.g., omega-3 fatty acids) in the simulated seafood composition, and the antioxidant may also prevent oxidative color changes in the colored structured plant protein product and the seafood meat. The antioxidant may be natural or synthetic. Suitable antioxidants include, but are not limited to, ascorbic acid and its salts, ascorbyl palmitate, ascorbyl stearate, anoxomer, N-acetylcysteine, benzyl isothiocyanate, o-, m- or p-amino benzoic acid (o is anthranilic acid, p is PABA), butylated hydroxyanisole (BHA), butylated hydroxytoluene (BHT), caffeic acid, canthaxantin, alpha-carotene, beta-carotene, beta-caraotene, beta-apo-carotenoic acid, carnosol, carvacrol, catechins, cetyl gallate, chlorogenic acid, citric acid and its salts, clove extract, coffee bean extract, p-coumaric acid, 3,4-dihydroxybenzoic acid, N,N′-diphenyl-p-phenylenediamine (DPPD), dilauryl thiodipropionate, distearyl thiodipropionate, 2,6-di-tert-butylphenol, dodecyl gallate, edetic acid, ellagic acid, erythorbic acid, sodium erythorbate, esculetin, esculin, 6-ethoxy-1,2-dihydro-2,2,4-trimethylquinoline, ethyl gallate, ethyl maltol, ethylenediaminetetraacetic acid (EDTA), eucalyptus extract, eugenol, ferulic acid, flavonoids, flavones (e.g., apigenin, chrysin, luteolin), flavonols (e.g., datiscetin, myricetin, daemfero), flavanones, fraxetin, fumaric acid, gallic acid, gentian extract, gluconic acid, glycine, gum guaiacum, hesperetin, alpha-hydroxybenzyl phosphinic acid, hydroxycinammic acid, hydroxyglutaric acid, hydroquinone, N-hydroxysuccinic acid, hydroxytryrosol, hydroxyurea, ice bran extract, lactic acid and its salts, lecithins, lecithin citrate; R-alpha-lipoic acid, lutein, lycopene, malic acid, maltol, 5-methoxy tryptamine, methyl gallate, monoglyceride citrate; monoisopropyl citrate; morin, beta-naphthoflavone, nordihydroguaiaretic acid (NDGA), octyl gallate, oxalic acid, palmityl citrate, phenothiazine, phosphatidylcholine, phosphoric acid, phosphates, phospholipids such as phosphatidyl inositol, phosphatidyl ethanolamine, phosphatidyl serine, and phosphatidic acid, phytic acid, phytylubichromel, pimento extract, propyl gallate. polyphosphates, quercetin, trans-resveratrol, rosemary extract, rosmarinic acid, sage extract, sesamol, silymarin, sinapic acid, succinic acid, stearyl citrate, syringic acid, tartaric acid, thymol, tocopherols (i.e., alpha-, beta-, gamma- and delta-tocopherol), tocotrienols (i.e., alpha-, beta-, gamma- and delta-tocotrienols), tyrosol, vanilic acid. 2,6-di-tert-butyl-4-hydroxymethylphenol (i.e., lonox 100), 2,4-(tris-3′,5′-bi-tert-butyl-4′-hydroxybenzyl)-mesitylene (i.e., lonox 330), 2,4,5-trihydroxybutyrophenone, ubiquinone, tertiary butyl hydroquinone (TBHQ), thiodipropionic acid, trihydroxy butyrophenone, tryptamine, tyramine, uric acid, vitamin K and derivates, vitamin Q10, wheat germ oil, zeaxanthin, or combinations thereof. The concentration of an antioxidant in a simulated seafood composition may range from about 0.0001% to about 20% by weight. The concentration of an antioxidant in a simulated seafood composition may range from about 0.001% to about 5% by weight. The concentration of an antioxidant in a simulated seafood composition may range from about 0.01% to about 1%.
The simulated seafood composition may further comprise a chelating agent to stabilize the color. Suitable examples of chelating agents approved for use in food include ethylenediaminetetraacetic acid (EDTA), citric acid, gluconic acid, and phosphoric acid.
The simulated seafood composition may further comprise a flavoring agent to impart the flavor and smell of seafood meat. The flavoring agent may be seafood oil or SDA. Generally, seafood oil contains high amounts of EPA and DHA, with smaller amounts of omega-6 fatty acids, 18C omega-3 fatty acids, 16C-22C unsaturated fatty acids, and 12C-18C saturated fatty acids. The seafood oil may be from herring, mackerel, menhaden, salmon, sardine, shellfish, shrimp, tuna, fish body, cod liver, fish liver, or shark liver. DHA may also be derived from algae. SDA can be derived from soybeans. The seafood oil may be health grade, pharmaceutical grade, concentrated, refined, or distilled. The flavoring agent may also be a seafood extract, seafood broth, or seafood liquor. The seafood extract, broth, or liquor may be from herring, mackerel, menhaden, salmon, sardine, shellfish, shrimp, or tuna. Alternatively, the seafood extract, broth, or liquor may be from a milder tasting seafood, such as cod, haddock, whitefish, flounder, or crab.
The simulated seafood composition may further comprise a flavor agent that imparts additional flavors. Examples of such agents include spices, spice oils, spice extracts, onion flavorings, garlic flavorings, herbs, herb oils, herb extracts, natural smoke solutions, and natural smoke extracts. The simulated seafood composition may further comprise a flavor enhancer. Examples of flavor enhancers that may be used include salt (sodium chloride), glutamic acid salts (e.g., monosodium glutamate), glycine salts, guanylic acid salts, inosinic acid salts, 5′-ribonucleotide salts, hydrolyzed proteins, and hydrolyzed vegetable proteins.
The simulated seafood composition may further comprise a nutrient such as a vitamin, a mineral, an antioxidant, or an herb. Suitable vitamins include Vitamins A, C, and E, which are also antioxidants, and Vitamins B and D. Examples of minerals that may be added include the salts of aluminum, ammonium, calcium, magnesium, and potassium. Herbs that may be added include basil, celery leaves, chervil, chives, cilantro, parsley, oregano, tarragon, and thyme.
The simulated seafood composition may further comprise a thickening or a gelling agent, such as alginic acid and its salts, agar, carrageenan and its salts, processed Eucheuma seaweed, gums (carob bean, guar, tragacanth, and xanthan), pectins, sodium carboxymethylcellulose, and modified starches.
The packaging of the simulated seafood compositions can and will vary depending upon the type of composition and its intended use. The simulated seafood compositions may be packaged fresh, frozen, canned, retorted, dried, or freeze dried. The compositions may be packed under vacuum, modified atmosphere (e.g., under high CO2), or at atmospheric pressure. Standards for food packaging are well known in the art. Fresh, frozen, or dried simulated seafood compositions may be packed in plastic wraps, shrink film, plastic bags/pouches/containers, or composite (i.e., plastic and foil) bags/pouches/containers. Canned or retorted simulated seafood compositions may be packed in cans, glass containers, plastic bags/pouches, or composite bags/pouches. Freeze dried simulated seafood compositions may be vacuum packed in plastic bags/pouches or composite bags/pouches. Additionally, the simulated seafood compositions may be mixed with vegetables, pasta, rice, beans, animal meats, cheese, dairy products, or eggs to make seafood entrees, meatless entrees, meat-seafood entrees, appetizers, stews, soups, salads, omelets, etc. prior to packaging.
The simulated seafood composition may be combined with additional ingredients to make a variety of seasoned seafood products. As an example, a tuna salad product may be produced according to the following formula:
A curry flavored tuna product may be produced using the following formula:
The term “extrudate” as used herein refers to the product of extrusion. In this context, the structured plant protein products comprising protein fibers that are substantially aligned may be extrudates in some embodiments.
The term “fiber” as used herein refers to a structured plant protein product having a size of approximately 4 centimeters in length and 0.2 centimeters in width after the shred characterization test detailed in Example 4 is performed. Fibers generally form Group 1 in the shred characterization test. In this context, the term “fiber” does not include the nutrient class of fibers, such as soybean cotyledon fibers, and also does not refer to the structural formation of substantially aligned protein fibers comprising the plant protein products.
The term “fish meat” as used herein refers to the flesh, whole meat muscle, or parts thereof derived from a fish.
The term “gluten” as used herein refers to a protein fraction in cereal grain flour, such as wheat, that possesses a high content of protein as well as unique structural and adhesive properties.
The term “gluten free starch” as used herein refers to modified tapioca starch. Gluten free or substantially gluten free starches are made from wheat, corn, and tapioca based starches. They are gluten free because they do not contain the gluten from wheat, oats, rye or barley.
The term “large piece” as used herein is the manner in which a plant protein product's shred percentage is characterized. The determination of shred characterization is detailed in Example 4.
The term “protein fiber” as used herein refers the individual continuous filaments or discrete elongated pieces of varying lengths that together define the structure of the structured plant protein products of the invention. Additionally, because the structured plant protein products of the invention have protein fibers that are substantially aligned, the arrangement of the protein fibers impart the texture of whole meat muscle to the structured plant protein products.
The term “seafood meat” as used herein refers to the flesh, whole meat muscle, or parts thereof derived from seafood.
The term “simulated” as used herein refers to a seafood composition that contains a structured plant protein product, fatty acid, and less than 100% seafood meat.
The term “soy cotyledon fiber” as used herein refers to the fibrous portion of soy cotyledons containing at least about 70% fiber (e.g., polysaccharide). Soy cotyledon fiber typically contains some minor amounts of soy protein, but may also be 100% fiber. Soy cotyledon fiber, as used herein, does not refer to, or include, soy hull fiber. Generally, soy cotyledon fiber is formed from soybeans by removing the hull and germ of the soybean from the cotyledon, flaking or grinding the cotyledon and removing oil from the flaked or ground cotyledon, and separating the soy cotyledon fiber from the soy material and carbohydrates of the cotyledon.
The term “soy protein concentrate” as used herein is a soy material having a protein content of from about 65% to less than about 90% soy protein on a moisture-free basis. Soy protein concentrate also contains soy cotyledon fiber, typically from about 3.5% up to about 20% soy cotyledon fiber by weight on a moisture-free basis. A soy protein concentrate is formed from soybeans by removing the hull and germ of the soybean from the cotyledon, flaking or grinding the cotyledon and removing oil from the flaked or ground cotyledon, and separating the soy protein and soy cotyledon fiber from the carbohydrates of the cotyledon.
The term “soy flour” as used herein, refers to a comminuted form of defatted soybean material, preferably containing less than about 1% oil, formed of particles having a size such that the particles can pass through a No. 100 mesh (U.S. Standard) screen. The soy cake, chips, flakes, meal, or mixture of the materials are comminuted into a soy flour using conventional soy grinding processes. Soy flour has a soy protein content of about 49% to about 65% on a moisture free basis. Preferably the flour is very finely ground, most preferably so that less than about 1% of the flour is retained on a 300 mesh (U.S. Standard) screen.
The term “soy protein isolate” as used herein is a soy material having a protein content of at least about 90% soy protein on a moisture free basis. A soy protein isolate is formed from soybeans by removing the hull and germ of the soybean from the cotyledon, flaking or grinding the cotyledon and removing oil from the flaked or ground cotyledon, separating the soy protein and carbohydrates of the cotyledon from the cotyledon fiber, and subsequently separating the soy protein from the carbohydrates.
The term “strand” as used herein refers to a plant protein product having a size of approximately 2.5 to about 4 centimeters in length and greater than approximately 0.2 centimeter in width after the shred characterization test detailed in Example 4 is performed. Strands generally form Group 2 in the shred characterization test.
The term “starch” as used herein refers to starches derived from any native source. Typically sources for starch are cereals, tubers, roots, legumes, and fruits.
The term “wheat flour” as used herein refers to flour obtained from the milling of wheat. Generally speaking, the particle size of wheat flour is from about 14 μm to about 120 μm.
Examples 1-5 illustrate various embodiments of the invention.
A preparation of color from fermented red rice, i.e., rice cultured with the red mold Monascus purpureus, can be used to color a structured protein product of the invention to resemble tuna meat. The monascus colorant (AVO-Werke August Beisse, Belm, Germany) will be dispersed in water and mixed with structured soy/wheat protein product (e.g., SUPRO®MAX 5050, Solae, St. Louis, Mo.). After 1 hour, the colored structured soy/wheat protein product will be flaked using a Comitrol® Processor (Urschel Laboratories, Inc., Valparaiso, Ind.).
Yellowfin tuna loin will be steam cooked to an internal temperature of 60° C., chilled and flaked. The cooked tuna and the colored structured protein product will be blended in a 3:1 ratio and packed into cans, as shown in Table 2. The cans will be retorted at 117° C. for 75 minutes in a retort cooker. The taste, color, appearance, smell, and texture of each preparation will be evaluated.
FD&C Red Color No. 40 and FD&C Yellow Color No. 5 can be used to color a structured protein product of the invention to resemble tuna meat. Structured soy/wheat protein product (e.g., SUPRO®MAX 5050, Solae, St. Louis, Mo.) will be mixed with the dyes as detailed in Table 3. After 1 hour, the colored structured soy/wheat protein product will be flaked using a Comitrol® Processor (Urschel Laboratories, Inc., Valparaiso, Ind.).
Tuna will be cooked and flaked essentially as described in Example 1. The ingredients will be packed into cans using the amounts listed in Table 4. The cans will be retorted at 117° C. for 75 minutes in a retort cooker. The taste, color, appearance, smell, and texture of each preparation will be evaluated.
Shear strength of a sample is measured in grams and may be determined by the following procedure. Weigh a sample of the colored structured plant protein product and place it in a heat sealable pouch and hydrate the sample with approximately three times the sample weight of room temperature tap water. Evacuate the pouch to a pressure of about 0.01 Bar and seal the pouch. Permit the sample to hydrate for about 12 to about 24 hours. Remove the hydrated sample and place it on the texture analyzer base plate oriented so that a knife from the texture analyzer will cut through the diameter of the sample. Further, the sample should be oriented under the texture analyzer knife such that the knife cuts perpendicular to the long axis of the textured piece. A suitable knife used to cut the extrudate is a model TA-45, incisor blade manufactured by Texture Technologies (USA). A suitable texture analyzer to perform this test is a model TA, TXT2 manufactured by Stable Micro Systems Ltd. (England) equipped with a 25, 50, or 100 kilogram load. Within the context of this test, shear strength is the maximum force in grams needed to puncture through the sample.
A procedure for determining shred characterization may be performed as follows. Weigh about 150 grams of a structured plant protein product using whole pieces only. Place the sample into a heat-sealable plastic bag and add about 450 grams of water at 25° C. Vacuum seal the bag at about 150 mm Hg and allow the contents to hydrate for about 60 minutes. Place the hydrated sample in the bowl of a Kitchen Aid mixer model KM14G0 equipped with a single blade paddle and mix the contents at 130 rpm for two minutes. Scrape the paddle and the sides of the bowl, returning the scrapings to the bottom of the bowl. Repeat the mixing and scraping two times. Remove ˜200 g of the mixture from the bowl. Separate the ˜200 g of mixture into one of two groups. Group 1 is the portion of the sample having fibers at least 4 centimeters in length and at least 0.2 centimeters wide. Group 2 is the portion of the sample having strands between 2.5 cm and 4.0 cm long, and which are ≧0.2 cm wide. Weigh each group, and record the weight. Add the weight of each group together, and divide by the starting weight (e.g. ˜200 g). This determines the percentage of large pieces in the sample. If the resulting value is below 15%, or above 20%, the test is complete. If the value is between 15% and 20%, then weigh out another ˜200 g from the bowl, separate the mixture into groups one and two, and perform the calculations again.
The following extrusion process may be used to prepare the structured plant protein products of the invention, such as the soy structured plant protein products utilized in Examples 1 and 2. Added to a dry blend mixing tank are the following: 1000 kilograms (kg) Supro 620 (soy isolate), 440 kg wheat gluten, 171 kg wheat starch, 34 kg soy cotyledon fiber, 9 kg dicalcium phosphate, and 1 kg L-cysteine. The contents are mixed to form a dry blended soy protein mixture. The dry blend is then transferred to a hopper from which the dry blend is introduced into a preconditioner along with 480 kg of water to form a conditioned soy protein pre-mixture. The conditioned soy protein pre-mixture is then fed to a twin-screw extrusion apparatus (Wenger Model TX-168 extruder by Wenger Manufacturing Inc. (Sabetha, Kans.)) at a rate of not more than 25 kg/minute. The extrusion apparatus comprises five temperature control zones, with the protein mixture being controlled to a temperature of from about 25° C. in the first zone, about 50° C. in the second zone, about 95° C. in the third zone, about 130° C. in the fourth zone, and about 150° C. in the fifth zone. The extrusion mass is subjected to a pressure of at least about 400 psig in the first zone up to about 1500 psig in the fifth zone. Water, 60 kg, is injected into the extruder barrel, via one or more injection jets in communication with a heating zone. The molten extruder mass exits the extruder barrel through a die assembly consisting of a die and a backplate. As the mass flows through the die assembly the protein fibers contained within are substantially aligned with one another forming a fibrous extrudate. As the fibrous extrudate exits the die assembly, it is cut with flexible knives and the cut mass is then dried to a moisture content of about 10% by weight.
| Number | Date | Country | |
|---|---|---|---|
| 60826360 | Sep 2006 | US |
