Patent Application
20080254167
The present invention provides seafood compositions and simulated seafood compositions comprising structured protein products and optionally may include seafood meat. In particular, the seafood composition generally comprises structured protein products along with seafood meat and optional macronutrients, micronutrients, and other ingredients.
Food scientists have devoted time and resources developing methods for preparing acceptable seafood meat-like food products, such as fish and shellfish, from a wide variety of proteins from different sources. Extrusion of high protein mixtures has been widely utilized to form these seafood meat analogs. While some high protein extrudates have much more seafood meat-like characteristics than other high protein extrudates, many have the disadvantage of being light beige or straw colored. Oftentimes, the seafood meat analog can be mixed with seafood meat and the mixture can be colored to resemble the color of the final seafood meat product, but the texture and taste are not analogous to authentic seafood.
Thus, there is an unmet need for a seafood meat analog that simulates the fibrous structure of seafood meat and mimics the texture, taste, mouthfeel, and color of an all seafood meat product. For example, it is desirable to have a seafood meat analog that would resemble seafood meat products, such as fish steaks, patties, sticks, nuggets, fillets, minced meat, or any other seafood product.
One aspect of the present invention provides seafood meat compositions comprising seafood meat and structured plant protein products having protein fibers that are substantially aligned.
The seafood meat and analogous seafood meat compositions may also generally comprise a firming agent.
Another aspect of the invention provides simulated seafood meat compositions comprising structured protein products. The structured protein product is formed by extruding a plant protein-containing material through a die assembly, whereby the extrudate has protein fibers that are substantially aligned.
A further aspect of the invention provides a process for producing a seafood meat composition or an analogous seafood meat composition. The process comprises extruding an amount of protein products that optionally may include an amount of seafood meat and other optional ingredients such as macronutrients, micronutrients, colorants, and flavorants to produce a structured protein product having protein fibers that are substantially aligned.
Other aspects and features of the invention are described in more detail below.
The application 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 seafood meat compositions or simulated seafood meat composition (seafood meat analog compositions) and processes for producing each of the seafood meat compositions. The seafood meat compositions comprise structured protein products having protein fibers that are substantially aligned. The structured protein products are formed by extruding a protein-containing material through a die assembly, such that the extrudate has substantially aligned protein fibers. Advantageously, as illustrated in the examples, the seafood meat compositions of the invention possess improved flavor, texture, mouth feel, aroma, and nutritional properties.
In an additional embodiment, the structural protein products are formed by extruding a protein-containing material and at least one colorant through a die assembly, such that the colored extrudate has substantially aligned protein fibers.
(I) Seafood Meat Compositions and Simulated Seafood Meat Compositions
One aspect of the invention provides seafood meat compositions comprising structured protein products and seafood meat. Another aspect of the invention provides simulated seafood meat compositions comprising structured protein products. The composition and properties of the structured protein products are detailed below in section (I)A. Because the structured protein products have protein fibers that are substantially aligned in a manner similar to seafood meat, the meat compositions of the invention generally have the texture and eating quality characteristics of compositions comprised of one hundred percent seafood meat.
The seafood meat compositions and the simulated seafood meat compositions of the invention may comprise conventionally grown ingredients, or the meat compositions may comprise organically grown ingredients. Furthermore, the seafood meat compositions may comprise kosher and/or Halal certified ingredients. Additionally, the simulated seafood meat compositions may comprise entirely plant-derived ingredients, and therefore be vegan. Conversely, the simulated seafood meat composition may comprise plant, dairy, and/or egg derived ingredients, and therefore, be lacto-, ovo-, or lacto-ovo-vegetarian.
A. Structured Protein Products
The structured protein products have protein fibers that are substantially aligned, as described below. A structured protein product is made by extruding a protein-containing material through a die assembly under conditions of elevated temperature and pressure, such that the extrudate has substantially aligned protein fibers. A variety of protein-containing materials as described below, may be used to produce the structured protein products. The protein-containing materials may be derived from plant, seafood, or other animal sources. Additionally, combinations of protein-containing materials from various sources may be used in combination to produce structured protein products having substantially aligned protein fibers.
(a) Protein-Containing Materials
As mentioned above, the protein-containing material may be derived from a variety of sources and then further utilized in a thermal plastic extrusion process to produce structured protein products suitable for use in the seafood meat and simulated seafood meat compositions. Irrespective of its source or ingredient classification, the ingredients utilized in the extrusion process are typically capable of forming structured protein products having protein fibers that are substantially aligned. Suitable examples of such ingredients are detailed more fully below.
The amount of protein present in the ingredient(s) 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.
A variety of ingredients that contain protein may be utilized in a thermal plastic extrusion process to produce structured protein products suitable for use in the seafood meat simulated meat compositions. 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, 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, ovovitella, ovovitellin, albumin globulin, vitellin, and combinations thereof may be utilized. Further, meat proteins or protein ingredients consisting of collagen, blood, organ meat, mechanically separated meat, partially defatted tissue, blood serum proteins, and combinations thereof may be included as one or more of the ingredients of the structured protein products.
It is envisioned that other ingredient types in addition to proteins may be utilized. Non-limiting examples of such ingredients include sugars, starches, oligosaccharides, soy fiber, other dietary fibers, and combinations thereof.
While in some embodiments gluten may be used as a protein, it is also envisioned that the protein-containing starting materials may be gluten-free. Further, it is envisioned that the protein-containing starting materials may be wheat-free. Because gluten is typically used in filament formation during the extrusion process, if a gluten-free starting material is used, an edible cross-linking agent may be utilized to facilitate filament formation. Non-limiting examples of suitable cross-linking agents include Konjac glucomannan (KGM) flour, BetaGlucan manufactured by Kirin Food-Tech Company (Japan), transglutaminase, calcium salts, magnesium salts, and combinations thereof. One skilled in the art can readily determine the amount of cross-linking material 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 extrudates 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 structured protein product. Generally speaking, the ingredient will comprise a protein. The protein containing material derived from a plant may be a plant extract, a plant meal, a plant-derived flour, a plant protein isolate, a plant protein concentrate, and combinations thereof.
The ingredient(s) utilized in extrusion may be derived from a variety of suitable plants. The plants may be grown conventionally or organically. By way of non-limiting examples, suitable plants include amaranth, arrowroot, barley, buckwheat, cassava, canola, channa (garbanzo), corn, kamut, lentil, lupin, millet, oat, pea, peanut, potato, quinoa, rice, rye, sorghum, sunflower, tapioca, triticale, wheat, and mixtures thereof. Exemplary plants include soy, wheat, canola, corn, lupin, oat, pea, potato, and rice.
In one embodiment, the ingredients may be isolated from wheat and soybeans. In another exemplary embodiment, the ingredients may be isolated from soybeans. In a further embodiment, the ingredients may be isolated from wheat. Suitable wheat derived protein-containing ingredients include wheat gluten, wheat flour, and mixtures thereof. Examples of commercially available wheat gluten that may be utilized in the invention include Manildra Gem of the West Vital Wheat Gluten and Manildra Gem of the West Organic Vital Wheat Gluten each of which are available from Manildra Milling. Suitable soy derived protein-containing ingredients (“soy protein material”) include soy protein isolate, soy protein concentrate, soy flour, and mixtures thereof, each of which is detailed below.
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 soybeans may be standard soybeans (i.e., non genetically modified soybeans), organic soybeans, commoditized soybeans, genetically modified soybeans, and combinations thereof.
In one embodiment, the soy protein material may be a soy protein isolate (ISP). In general, a soy protein isolate has a protein content of at least about 90% soy protein on a moisture-free basis. Generally speaking, when soy protein 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. Additionally, the soy protein isolate utilized preferably has an emulsion strength and gel strength sufficient to enable the protein in the isolate to form fibers that are substantially aligned upon extrusion. 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, SUPRO® EX 45, SUPRO® 595, and combinations thereof. In an exemplary embodiment, a form of SUPRO® 620 is utilized as detailed in Example 3.
Alternatively, soy protein concentrate 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 55% of the soy protein isolate by weight. The soy protein concentrate can be substituted for up to about 50% of the soy protein isolate by weight. It is also possible in an embodiment to substitute 40% by weight of the soy protein concentrate for the soy protein isolate. In another embodiment, the amount of soy protein concentrate substituted is up to about 30% of the soy protein isolate by weight. Examples of suitable soy protein concentrates useful in the invention include PROCON™ 2000, ALPHA™ 12, ALPHA™ 5800, and combinations thereof, which are commercially available from Solae, LLC (St. Louis, Mo.).
In yet another embodiment, the soy protein material may be soy flour, which has a protein content of about 49% to about 65% on a moisture-free basis. Alternatively, soy flour may be blended with soy protein isolate or soy protein concentrate. If 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. When soy flour is used, the starting material is preferably a defatted soybean flour or flakes. Full fat soybeans contain approximately 40% protein by weight and approximately 20% oil by weight. These whole full fat soybeans may be defatted through conventional processes when a defatted soy flour or flakes form the starting protein material. For example, the bean may be cleaned, dehulled, cracked, passed through a series of flaking rolls and then subjected to solvent extraction by use of hexane or other appropriate solvents to extract the oil and produce “spent flakes” The defatted flakes may be ground to produce a soy flour. Although the process is yet to be employed with full fat soy flour, it is believed that full fat soy flour may also serve as a protein source. However, where full fat soy flour is processed, it is most likely necessary to use a separation step, such as three-stage centrifugation to remove oil.
Any fiber known in the art can be used as the fiber source in the application. Soy cotyledon fiber may optionally be utilized as a fiber source. Typically, 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 generally be present in the soy protein material in an amount ranging from about 1% to about 20% on a moisture free basis, preferably from about 1.5% to about 20% on a moisture free basis, 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.).
The seafood meat compositions, in addition to structured plant protein product, may also comprise animal meat. A variety of animal meats are suitable as a protein source. Animals from which the meat is obtained may be raised conventionally or organically. By way of example, meat and meat ingredients defined specifically for the various structured vegetable protein patents include intact or ground beef, pork, lamb, mutton, horsemeat, goat meat, meat, fat and skin of poultry (domestic fowl such as chicken, duck, goose or turkey) and more specifically flesh tissues from any fowl (any bird species), fish flesh derived from both fresh and salt water, animal flesh of shellfish and crustacean origin, animal flesh trim and animal tissues derived from processing such as frozen residue from sawing frozen fish, chicken, beef, pork etc., chicken skin, pork skin, fish skin, animal fats such as beef fat, pork fat, lamb fat, chicken fat, turkey fat, rendered animal fat such as lard and tallow, flavor enhanced animal fats, fractionated or further processed animal fat tissue, finely textured beef, finely textured pork, finely textured lamb, finely textured chicken, low temperature rendered animal tissues such as low temperature rendered beef and low temperature rendered pork, mechanically separated meat or mechanically deboned meat (MDM) (meat flesh removed from bone by various mechanical means) such as mechanically separated beef, mechanically separated pork, mechanically separated fish including surimi, mechanically separated chicken, mechanically separated turkey, any cooked animal flesh and organ meats derived from any animal species, and combinations thereof. Meat flesh should be extended to include muscle protein fractions derived from salt fractionation of the animal tissues, protein ingredients derived from isoelectric fractionation and precipitation of animal muscle or meat and hot boned meat as well as mechanically prepared collagen tissues and gelatin. Additionally, meat, fat, connective tissue and organ meats of game animals such as buffalo, deer, elk, moose, reindeer, caribou, antelope, rabbit, bear, squirrel, beaver, muskrat, opossum, raccoon, armadillo and porcupine as well as reptilian creatures such as snakes, turtles and lizards, and combinations thereof should be considered meat.
In a further embodiment, the animal meat may be from fish or seafood. Non-limiting examples of suitable fish include bass, carp, catfish, cobia, cod, grouper, flounder, haddock, hoki, perch, pollock, salmon, snapper, sole, trout, tuna, whitefish, whiting, tilapia, and combinations thereof. Non-limiting examples of seafood include scallops, shrimp, lobster, clams, crabs, mussels, oysters, and combinations thereof.
It is also envisioned that in addition to a variety of meat qualities a variety of fish species that are currently not used because of the proteolytic enzymes found in the fish species can be utilized in the seafood composition. Certain fish species contain an amount of proteolytic enzymes that cause rapid degradation of myosin. The degradation can occur at any time during the processing of the fish, including during storage, including frozen storage, and when a fish product produced from the fish is cooked. The rapid degradation of myosin produces a fish product where the fish tissue and/or muscle, cooked or uncooked, have a mushy texture and unacceptable mouthfeel for consumers. In an embodiment of the current seafood composition the fish or seafood used can be any fish species that possess the proteolytic enzyme known in the industry including but not limited to Arrowtooth flounder.
It is also envisioned that a variety of meat qualities may be utilized in the invention. The meat may comprise muscle tissue, organ tissue, connective tissue, skin, and combinations thereof. The meat may be any meat suitable for human consumption. The meat may be non-rendered, non-dried, raw meat, raw meat products, raw meat by-products, and mixtures thereof. For example, whole meat muscle that is either ground or in chunk or steak form may be utilized. In another embodiment, the meat may be mechanically deboned or separated raw meats using high-pressure machinery that separates bone from animal tissue, by first crushing bone and adhering animal tissue and then forcing the animal tissue, and not the bone, through a sieve or similar screening device. The process forms an unstructured, paste-like blend of soft animal tissue with a batter-like consistency and is commonly referred to as mechanically deboned meat or MDM. In an additional embodiment, seafood meat can be obtained through typical MDM processes or any method known in the art for separating seafood meat, such as fish or shellfish from bones or shells. Alternatively, the meat may be a meat by-product. In the context of the present invention, the term “meat by-products” is intended to refer to those non-rendered parts of the carcass of slaughtered animals, fish, and shellfish. Examples of meat by-products are organs and tissues such as lungs, spleens, kidneys, brain, liver, blood, bone, partially defatted low-temperature fatty tissues, stomachs, intestines free of their contents, and the like.
The protein source may also be an animal derived protein other than animal tissue. For example, the protein-containing material may be derived from a dairy product. Suitable dairy protein products include non-fat dried milk powder, whole milk powder, liquid milk, milk protein isolate, milk protein concentrate, casein protein isolate, casein protein concentrate, caseinates, whey protein isolate, whey protein concentrate, and combinations thereof. The milk protein-containing material may be derived from cows, goats, sheep, donkeys, camels, camelids, yaks, or water buffalos. In an exemplary embodiment, the dairy protein is whey protein.
By way of further example, a protein-containing material may also be from an egg product. Suitable egg protein products include powdered egg, dried egg solids, dried egg white protein, liquid egg white protein, egg white protein powder, isolated ovalbumin protein, and combinations thereof. Examples of suitable isolated egg proteins include ovalbumin, ovoglobulin, ovomucin, ovomucoid, ovotransferrin, ovovitella, ovovitellin, albumin globulin, vitellin, and combinations thereof. Egg protein products may be derived from the eggs of chicken, duck, goose, quail, or other birds.
(iii) Combinations of Protein-Containing Materials
Non-limiting combinations of protein-containing materials isolated from a variety of sources are detailed in Table A. In one embodiment, the protein-containing material is derived from soybeans. In a preferred embodiment, the protein-containing material comprises a mixture of materials derived from soybeans and wheat. In another preferred embodiment, the protein-containing material comprises a mixture of materials derived from soybeans and canola. In still another preferred embodiment, the protein-containing material comprises a mixture of materials derived from soybeans, wheat, and dairy, wherein the dairy protein is whey.
sorghum
(b) Additional Ingredients
It is envisioned that other ingredient additives in addition to proteins may be utilized in the structured protein products. Non-limiting examples of such ingredients include sugars, starches, oligosaccharides, and dietary fibers. As an example, starches may be derived from wheat, corn, tapioca, potato, rice, and the like. A suitable fiber source may be soy cotyledon fiber. Typically, suitable soy cotyledon fiber will generally effectively bind water when the mixture of soy protein and soy cotyledon fiber is co-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. Soy cotyledon fiber may generally be present in the soy protein-containing material 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.).
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, 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% fiber 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.
(ii) pH-Adjusting Agent
In some embodiments, it may be desirable to adjust the pH of the protein-containing material to an acidic pH (i.e., below approximately 7.0). Thus, the protein-containing material may be contacted with a pH-lowering agent, and the mixture is then extruded according to the process detailed below. In one embodiment, the pH of the protein-containing material to be extruded may range from about 6.0 to about 7.0. In another embodiment, the pH may range from about 5.0 to about 6.0. In an alternate embodiment, the pH may range from about 4.0 to about 5.0. In yet another embodiment, the pH of the material may be less than about 4.0.
Several pH-lowering agents are suitable for use in the invention. The pH-lowering agent may be organic. Alternatively, the pH-lowering agent may be inorganic. In exemplary embodiments, the pH-lowering agent is a food grade edible acid. Non-limiting acids suitable for use in the invention include acetic, lactic, hydrochloric, phosphoric, citric, tartaric, malic, and combinations thereof. In an exemplary embodiment, the pH-lowering agent is lactic acid.
As will be appreciated by a skilled artisan, the amount of pH-lowering agent contacted with the protein-containing material can and will vary depending upon several parameters, including, the agent selected and the desired pH. In one embodiment, the amount of pH-lowering agent may range from about 0.1% to about 15% on a dry matter basis. In another embodiment, the amount of pH-lowering agent may range from about 0.5% to about 10% on a dry matter basis. In an alternate embodiment, the amount of pH-lowering agent may range from about 1% to about 5% on a dry matter basis. In still another embodiment, the amount of pH-lowering agent may range from about 2% to about 3% on a dry matter basis.
In some embodiments, it may be desirable to raise the pH of the protein-containing material. Thus, the protein-containing material may be contacted with a pH-raising agent, and the mixture is then extruded according to the process detailed below.
(iii) Antioxidants
One or more antioxidants may be added to any of the combinations of protein-containing materials mentioned above without departing from the scope of the invention. Antioxidants may be included to increase the shelf-life or nutritionally enhance the structured protein products. Non-limiting examples of suitable antioxidants include BHA, BHT, TBHQ, vitamins A, C, and E and derivatives, various plant extracts, such as those containing carotenoids, tocopherols, or flavonoids having antioxidant properties, and combinations thereof. The antioxidants 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.
The protein-containing material may also optionally comprise supplemental minerals. Suitable minerals may include one or more minerals or mineral sources. Non-limiting examples of minerals include, without limitation, chloride, sodium, calcium, iron, chromium, copper, iodine, zinc, magnesium, manganese, molybdenum, phosphorus, potassium, selenium, and combinations thereof. Suitable forms of any of the foregoing minerals include soluble mineral salts, slightly soluble mineral salts, insoluble mineral salts, chelated minerals, mineral complexes, non-reactive minerals such as carbonyl minerals, reduced minerals, and combinations thereof.
Free amino acids may also be included in the protein-containing material. Suitable amino acids include the essential amino acids, i.e., arginine, cysteine, histidine, isoleucine, leucine, lysine, methionine, phenylalanine, threonine, tryptophan, valine, and combinations thereof. Suitable forms of the amino acids include salts and chelates.
The structured protein product may also include at least one colorant. The colorant(s) may be mixed with the protein-containing material and other ingredients prior to being fed into the extruder. Alternatively, the colorant(s) may be combined with the protein-containing material and other ingredients after being fed into the extruder. In the presence of the heat or the heat and pressure utilized during the extrusion process, some combinations of colorants and protein-containing materials result in unexpected colors. As an example, when carmine (soluble dye or lake) is contacted with the protein-containing material during the extrusion process, the color changes from red to violet/purple.
The colorant(s) may be 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 approved for use in food include annatto (reddish-orange), anthocyanins (red to blue, depends upon pH), beet juice, beta-carotene (orange), beta-APO 8 carotenal (orange), black currant, burnt sugar; canthaxanthin (pink-red), caramel, carmine/carminic acid (bright red), cochineal extract (red), curcumin (yellow-orange); lac (scarlet red), lutein (red-orange); lycopene (orange-red), mixed carotenoids (orange), monascus (red-purple, from fermented red rice), paprika, red cabbage juice, riboflavin (yellow), saffron, titanium dioxide (white), and turmeric (yellow-orange). Suitable examples of artificial colorants approved for food use in the United States include FD&C Red No. 3 (Erythrosine), FD&C Red No. 40 (Allure Red), FD&C Yellow No. 5 (Tartrazine), FD&C Yellow No. 6 (Sunset Yellow FCF), FD&C Blue No. 1 (Brilliant Blue), FD&C Blue No. 2 (Indigotine). Artificial colorants that may be used in other countries include Cl Food Red 3 (Carmoisine), Cl Food Red 7 (Ponceau 4R), Cl Food Red 9 (Amaranth), Cl Food Yellow 13 (Quinoline Yellow), and Cl Food Blue 5 (Patent Blue V). 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.
Suitable colorant(s) may be combined with the protein-containing materials in a variety of forms. Non-limiting examples include solid, semi-solid, powdered, liquid, and gelatin. The type and concentration of colorant(s) utilized may vary depending on the protein-containing materials used and the desired color of the colored structured protein product. Typically, the concentration of colorant(s) may range from about 0.001% to about 5.0% by weight. In one embodiment, the concentration of colorant(s) may range from about 0.01% to about 4.0% by weight. In another embodiment, the concentration of colorant(s) may range from about 0.05% to about 3.0% by weight. In still another embodiment, the concentration of colorant(s) may range from about 0.1% to about 3.0% by weight. In a further embodiment, the concentration of colorant(s) may range from about 0.5% to about 2.0% by weight. In another embodiment, the concentration of colorant(s) may range from about 0.75% to about 1.0% by weight.
(c) Making the Structured Protein Products
The structured protein products of the invention are made by extruding protein-containing material through a die assembly under conditions of elevated temperature and pressure producing structured protein products with protein fibers that are substantially aligned. In another embodiment, the protein-containing material may be combined with at least one colorant before it is put in the extruder. After extrusion, the resulting structured protein product comprises protein fibers that are substantially aligned.
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 structured protein products having protein fibers that are substantially aligned is detailed below and in Example 3.
The structured protein products of the invention are made by extruding protein-containing material through a die assembly under conditions of elevated temperature and pressure. In an additional embodiment, at least one colorant may be combined with the protein-containing material either prior to or during the extrusion process. Regardless of the point at which the protein-containing material and the colorant(s) are combined, the concentration of colorant(s) generally range from about 0.001% to about 5.0% by weight. The type and concentration of colorant(s) utilized may vary depending on the protein-containing materials used, the desired color of the colored structured protein product, and the point of the process the colorant(s) is introduced.
A suitable extrusion process for the preparation of a structured protein product comprises introducing the protein-containing material and other ingredients into a mixing tank (i.e., an ingredient blender) to combine the ingredients and form a blended protein material pre-mix. The blended protein material pre-mix may then be transferred to a hopper from which the blended ingredients may be introduced along with moisture into the extruder. In another embodiment, the blended protein material pre-mix may be combined with a conditioner to form a conditioned protein material mixture. The conditioned material may then be fed into an extruder in which the protein material mixture is heated under mechanical pressure generated by the screws of the extruder to form a molten extrusion mass. The extrudate exits the extruder through an extrusion die and comprises protein fibers that are substantially aligned.
(iii) Extrusion Process Conditions
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 Model X-175, the WENGER Model X-165, and the WENGER Model 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 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 shearlock 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. and 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. One skilled in the art could adjust the temperature either heating or cooling to achieve the desired properties. Typically, temperature changes are due to work input and can happen suddenly.
The pressure within the extruder barrel is typically between 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 preferably between about 150 psig to about 500 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 in communication with a heating zone. 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 protein-containing material, reducing sugar and other ingredients (protein-containing mixture) are preheated, contacted with moisture, and held under controlled temperature and pressure conditions to allow the moisture to penetrate and soften the individual particles. The preconditioning step increases the bulk density of the particulate fibrous material mixture and improves its flow characteristics. 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 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 using appropriate water temperature.
Typically, the protein-containing pre-mix is conditioned for a period of about 30 to about 60 seconds, depending on the speed and the size of the pre-conditioner. The 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 pre-mix, 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 low moisture pre-mix is desired, the conditioned pre-mix may contain from about 1% to about 35% (by weight) water. If high moisture pre-mix 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. This is presently believed to be due to such mixtures occupying all or a majority of the space between the screws of the extruder, thereby facilitating conveying the extrusion mass through the barrel.
The dry pre-mix or 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.
The rate at which the pre-mix is generally introduced to the extrusion apparatus will vary depending upon the particular apparatus. Generally, the pre-mix is introduced at a rate of no more than about 75 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. Whatever extruder is used, it should be run in excess of about 50% motor load. The rate at which the pre-mix is generally introduced to the extrusion apparatus will vary depending upon the particular apparatus. 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. In another embodiment, the conditioned pre-mix is introduced to the extrusion apparatus at a rate between 20 kilograms per minute to about 40 kilograms per minute. 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 pre-mix 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 forward through the extruder and through the die assembly. 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 500 to about 3000 psig, and more preferably an extruder barrel exit pressure of from about 600 to about 1000 psig is generated.
The extruder controls the temperature of the mixture as it passes through the extruder further denaturing the protein in the mixture. Passing through the extruder the denatured protein is restructured or reconfigured to produce a structured protein material with protein fibers substantially aligned. 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 also includes steam injection ports for directly injecting steam into the mixture within the extruder. The extruder may also include colorant injection ports for directly injecting colorant 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. In one embodiment, 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. For a further example, the extruder may be set in a six temperature zone arrangement, where the first zone is set to a temperature of about 90° C., the second zone is set to a temperature of about 100° C., the third zone is set to a temperature of about 105° C., the fourth zone is set to a temperature of about 100° C., the fifth zone is set to a temperature of about 120° C., and the sixth zone is set to a temperature of about 130° 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 and produces substantial alignment of the protein fibers within the plasticized mixture as it flows through the die assembly. The die assembly may include either a faceplate die or a peripheral 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.
Referring to the drawings (
As shown in
In one embodiment, the end plate 20 of the die sleeve 12 may be secured to a die cone 16 adapted to interface with the die insert 14 when the end plate 20 is secured to the rear portion 18 of the die sleeve 12 during assembly of the peripheral die assembly 10. As further shown, the rear portion 18 of die sleeve 12 defines a plurality of circular-shaped outlets 24 along the sleeve body 17 which are adapted to provide a conduit for the egress of extrusion from the peripheral die assembly 10 during the extrusion process. In the alternative, the plurality of outlets 24 may have different configurations, such as square, rectangular, scalloped or irregular. As further shown, the rear portion 18 of the die sleeve 12 may include a circular flange 37 that surrounds opening 72 and defines a pair of opposing slots 82A and 82B that are used to properly align the die sleeve 12 when engaging the die sleeve 12 to the extruding apparatus (not shown).
Referring to
Referring to
As shown specifically in
As further shown, each flow pathway 42 has a three-sided tapered configuration collectively defined between the opposing side walls 50 of adjacent flow diverters 38 and the slanted configuration of bottom portion 64 of the die insert 14. In one embodiment, this three-sided tapered configuration gradually tapers inwardly on all three sides of the flow pathway 42 from the entrance 84 to the outlet 24.
In an embodiment, the front face 27 of the die insert 14 may include eight flow diverters 38 that define a respective flow pathway 42 between adjacent flow diverters 38 for a total of eight flow pathways 42. However, other embodiments may define at least two or more flow diverters 38 circumferentially spaced around the peripheral edge of the 76 of the die insert 14 in order to provide at least two or more flow pathways 42 along the front face 27 of the die insert 14.
During the extrusion process, the peripheral die assembly 10 may be operatively engaged with an extruding apparatus (not shown) that produces an extrusion that contacts the well 52 defined by the rear face 29 of the die insert 14 and flows into the throat 34 and enters the inner space opening 36 as indicated by flow path A. The extrusion may enter the inner space 44 defined by the die insert 14 and enter the entrance 84 of each tapered flow channel 42. As noted above, the extrusion then flows through each flow channel 42 and exits from a respective outlet 24 in a manner that causes the substantial alignment of the vegetable protein fibers in the extrusion produced by the peripheral die assembly 10.
Examples of peripheral die assemblies suitable for use in this invention to produce the structured protein fibers that are substantially aligned are described in U.S. Pat. App. No. 60/882,662, and U.S. patent application Ser. No. 11/964,538, which are hereby incorporated by reference in their entirety.
The extrudate may be cut after exiting the die assembly. Suitable apparatuses for cutting the extrudate include flexible knives manufactured by Wenger Manufacturing, Inc. (Sabetha, Kans.) and Clextral, Inc. (Tampa, Fla.). Typically, the speed of the cutting apparatus is from about 1000 rpm to about 2500 rpm. In an exemplary embodiment, the speed of the cutting apparatus is about 1600 rpm. A delayed cut can also 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. Examples known in the art include convection dryers. The extrudate will be present in the dryer for a time sufficient to produce an extrudate having the desired moisture content. Thus, the temperature of the air is not important; if a lower temperature is used (such as 50° C.) 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 45 minutes and more generally, for at least about 65 minutes. Suitable dryers include those manufactured by CPM Wolverine Proctor (Lexington, N.C.), National Drying Machinery Co. (Trevose, Pa.), Wenger (Sabetha, Kans.), Clextral (Tampa, Fla.), and Buehler (Lake Bluff, Ill.).
Another option is to use microwave assisted drying. In this embodiment, a combination of convective and microwave heating is used to dry the product to the desired moisture. Microwave assisted drying is accomplished by simultaneously using forced-air convective heating and drying to the surface of the product while at the same time exposing the product to microwave heating that forces the moisture that remains in the product to the surface whereby the convective heating and drying continues to dry the product. The convective dryer parameters are the same as discussed previously. The addition is the microwave-heating element, with the power of the microwave being adjusted dependent on the product to be dried as well as the desired final product moisture. As an example the product can be conveyed through an oven that contains a tunnel that is equipped with wave-guides to feed the microwave energy to the product and chokes designed to prevent the microwaves from leaving the oven. As the product is conveyed through the tunnel the convective and microwave heating simultaneously work to lower the moisture content of the product whereby drying. Typically, the air temperature is 50° C. to about 80° C., and the microwave power is varied dependent on the product, the time the product is in the oven, and the final moisture content desired.
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 less than 10% moisture as a further example the material may have a moisture content typically from about 5% 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 and is to be used immediately, its moisture content can be higher, generally from about 16% to about 30% by weight. If a protein material with high moisture content is produced, the protein material may require immediate use or refrigeration to ensure product freshness, and minimize spoilage.
The extrudate may further be comminuted to reduce the average particle size of the extrudate. Typically, the reduced extrudate has an average particle size of from about 0.1 mm to about 40.0 mm. In one example, the reduced extrudate has an average particle size of from about 5.0 mm to about 30.0 mm. In another embodiment, the reduced extrudate has an average particle size of from about 0.5 mm to about 20.0 mm. In a further embodiment, the reduced extrudate has an average particle size of from about 0.5 mm to about 15.0 mm. In an additional embodiment, the reduced extrudate has an average particle size of from about 0.75 mm to about 10.0 mm. In yet another embodiment, the reduced extrudate has an average particle size of from about 1.0 mm to about 5.0 mm. Suitable apparatus for reducing particle size 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, Inc. (Valparaiso, Ind.), and roller mills such as RossKamp Roller Mills manufactured by RossKamp Champion (Waterloo, Ill.).
(e) Characteristics of the Structured Protein Products
The structured protein products produced above, typically comprise 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 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 protein product are substantially aligned. In another embodiment, an average of at least 60% of the protein fibers comprising the structured protein product are substantially aligned. In a further embodiment, an average of at least 70% of the protein fibers comprising the structured protein product are substantially aligned. In an additional embodiment, an average of at least 80% of the protein fibers comprising the structured protein product are substantially aligned. In yet another embodiment, an average of at least 90% of the protein fibers comprising the structured 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 protein products of the invention 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 structured 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 1. Generally speaking, the structured protein products of the invention will have average shear strength of at least 1400 grams. In an additional embodiment, the structured protein products will have average shear strength of from about 1500 to about 1800 grams. In yet another embodiment, the structured protein products will have average shear strength of from about 1800 to about 2000 grams. In a further embodiment, the structured protein products will have average shear strength of from about 2000 to about 2600 grams. In an additional embodiment, the structured protein products will have average shear strength of at least 2200 grams. In a further embodiment, the structured protein products will have average shear strength of at least 2300 grams. In yet another embodiment, the structured protein products will have average shear strength of at least 2400 grams. In still another embodiment, the structured protein products will have average shear strength of at least 2500 grams. In a further embodiment, the structured 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 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 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 protein product. Generally speaking, as the percentage of large pieces increases, the degree of protein fibers that are aligned within a structured protein product also typically increases. Conversely, as the percentage of large pieces decreases, the degree of protein fibers that are aligned within a structured protein product also typically decreases. A method for determining shred characterization is detailed in Example 2. The structured 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 protein products have an average shred characterization of from about 10% to about 15% by weight of large pieces. In another embodiment, the structured 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 protein products have an average shred characterization of from about 20% to about 25% 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 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 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. A another example, the structured 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 15% by weight large pieces. In exemplary embodiment, the structured 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 17% by weight large pieces. In another exemplary embodiment, the structured protein products will have protein fibers that are at least 55% aligned, have average shear strength of at least 2400 grams, and have an average shred characterization of at least 20% by weight large pieces.
B. Seafood Meat
The seafood meat compositions, in addition to structured plant protein products may also comprise seafood meat, such as fresh and saltwater fish and shellfish. As detailed above in (I)A(a)(ii), numerous suitable meats are available. Generally speaking, the seafood meat may be obtained from a variety of fish and shellfish species suitable for human consumption. Suitable examples of fish species include amberjack, anchovies, bluefish, bonito, buffalofish, burbot, butterfish, carp, catfish, crevalle jack, cobia, cod, croaker, cusk, eel, grouper, flounder (arrowtooth, southern, starry, summer, winter, witch, yellowtail), haddock, Goliath grouper, kingfish, lake chub, lake herring, lake sturgeon, lake whitefish, lingcod, mackerel, mahi mahi, monkfish, mullet, northern pike, orange roughy, Pacific sand dab, perch, pollock, pompano, rockfish, sable, salmon, sauger, sculp, sea bass (black, giant, white), sea dab, shark, sheepshead, smelt, snapper (red, mangrove, vermillion, yellowtail), snook, sole (Dover, English, Petrale, Rex, rock), spot, spotted cabrilla, striped bass, swordfish, tautog, tilefish, turbot, trout (brook, lake, rainbow, sea, white sea), tuna, walleye, white crappie, whiting, and wolfish. Examples of shellfish species include mulluses, crustaceans, and echinoderms, such as crab, crayfish, lobster, langouste, langoustine, moreton bay bugs, shrimp, yabbies, abalone (US), paua (NZ), clam, cockle, mussel, octopus, oyster, pipi, snail, conch, whelk, winkle, squid (calamari), tuatua, scallop, sea cucumber, and sea urchins.
The term “meat” is understood to apply not only to the flesh of the seafood, but also comprises meat by-products. By way of example, meat includes striated muscle, which is skeletal muscle, or smooth muscle that is found, for example, in the tongue, diaphragm, heart, or esophagus, with or without accompanying overlying fat and portions of the skin, sinew, nerve and blood vessels that normally accompany the meat flesh. Examples of meat by-products are organs and tissues such as lungs, spleens, kidneys, brain, liver, blood, bone, partially defatted low-temperature fatty tissues, skin, stomachs, intestines free of their contents, connective tissue, swim bladder, gills, and the like. Seafood by-products include non-rendered, clean parts of carcasses, such as heads, feet, and viscera, free from fecal content and foreign matter. The term “meat by-products” is intended to refer to those non-rendered parts of the carcass including but not restricted to seafood and the like and including such constituents as are embraced by the term “meat by-products” in the Definitions of Feed Ingredients published by the Association of American Feed Control Officials, Incorporated. The terms “meat,” and “meat by-products,” are understood to apply to all of those marine, and seafood products defined by association.
It is envisioned that a variety of meat forms may be utilized in the invention depending upon the product's intended use. In one embodiment, whole muscle meat pieces that are essentially intact may be used. In another embodiment, the meat may be in chunk or steak form. In an alternate embodiment, the meat may be coarsely ground. In another embodiment, the meat may be finely ground or comminuted. In yet another embodiment, mechanically deboned meat (MDM) may be utilized. In the context of the present invention, MDM is any mechanically deboned meat including a meat paste that is recovered, using commercially available equipment. In yet another embodiment, seafood meat can be obtained through typical MDM processes, or any method known in the art for separating seafood meat, such as fish or shellfish from bones or shells. MDM is generally an untexturized comminuted product that is devoid of the natural fibrous texture found in intact muscles. It is well known in the art to produce mechanically deboned or separated raw meats using high-pressure machinery that separates bone from seafood tissue, by first crushing bone and adhering seafood tissue and then forcing the seafood tissue, and not the bone, through a sieve or similar screening device.
It is also envisioned that combinations of meat products may be used. For example, whole meat muscle and MDM may be used. Alternatively, coarsely ground meat muscle and coarsely ground meat by-products may be used. One skilled in the art will also appreciate that the amount of fat in the different seafood meats varies widely. In some embodiments, therefore, an additional fat source may also be included. Suitable fat sources are presented below in section (II)C(c).
It is also envisioned that other meat products may also be used. Including any of the meat sources described in I(A)(a)(ii) above.
C. Other Ingredients
The seafood meat compositions and the simulated seafood meat compositions of the invention may comprise a variety of other ingredients to enhance the flavor, the nutritional profile, and the appearance of the final product.
(a) Curing Agent
In some embodiments, a seafood meat composition may further comprise a curing agent. In general, a curing agent consists only of a form of nitrites or nitrates. It is generally recognized the curing agent is reduced to nitric oxide, which combines with myoglobin to form nitric oxide myoglobin. Nitric oxide myoglobin, when heated to fix the pigment, becomes nitroso hemochrome.
Suitable curing agents include sodium nitrite, sodium nitrate, potassium nitrate, potassium nitrate, and the like. The concentration of the curing agent may range from about 0.001% to about 0.02% by weight. In a preferred embodiment, the curing agent comprises about 0.015% by weight of sodium or potassium nitrite.
(b) Flavoring Agent
The seafood meat compositions or the simulated seafood meat compositions may also comprise a variety of flavorings, spices, or other ingredients to enhance the flavor of the final food product. As will be appreciated by a skilled artisan, the selection of ingredients added to the meat compositions can and will depend upon the food product to be manufactured. For example, the meat compositions may further comprise a flavoring agent such as an animal or seafood meat flavor, an animal or seafood meat oil, spice extracts, spice oils, natural smoke solutions, natural smoke extracts, yeast extract, mushroom extract, and shiitake extract. Additional flavoring agents may include onion extract, onion powder, garlic extract, or garlic powder. Herbs or spices may be added as flavoring agents. Suitable herbs and spices include allspice, basil, bay leaves, black pepper, caraway seeds, cayenne, celery leaves, celery seeds, chervil, chili pepper, chives, cilantro, cinnamon, cloves, coriander, cumin, dill, fennel, ginger, marjoram, mustard, nutmeg, paprika, parsley, oregano, rosemary, saffron, sage, savory, shallots, smoked pimento, tarragon, thyme, and white pepper. The meat composition may further comprise a flavor enhancer. Examples of flavor enhancers that may be used include salt (sodium chloride, potassium 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 concentration of the flavoring agents and/or flavoring enhancers may range from about 0.01% to about 10% by weight, and more preferably from about 0.1% to about 3% by weight.
Phosphates may be added (up to 0.5% phosphate) to increase the water holding capacity of the final product. Suitable phosphates include the sodium tripolyphosphate, sodium hexametaphosphate, sodium acid pyrophosphate, sodium pyrophosphate, monosodium phosphate, and disodium phosphate.
(c) Fat Source
In some embodiments, the seafood meat composition or the simulated seafood meat composition may also further comprise a fat source to impart flavor and improve texture. In general, the total fat concentration of a meat composition will range from about 1% to about 40% by weight. Thus, the amount of a fat source added to the composition can and will vary depending upon the ingredients utilized. The fat source may be an animal or seafood derived fat, or the fat source may be a plant-derived oil. Non-limiting examples of suitable fats include tallow, lard, chicken fat, butter, fish oil, and mixtures thereof. Non-limiting examples of suitable plant derived oils include canola oil, coconut oil, corn oil, cottonseed oil, flax seed oil, grape seed oil, olive oil, peanut oil, palm oil, soybean oil, sunflower seed oil, and mixtures thereof. The plant derived oil may nonhydrogenated, partially hydrogenated, or fully hydrogenated. Typically, a simulated seafood meat composition will comprise a plant derived fat substance when it is formulated as a vegetarian composition.
(d) Antioxidant
An antioxidant may also be included in the seafood meat compositions or the simulated seafood meat compositions. The antioxidant may prevent the oxidation of the polyunsaturated fatty acids in the meat products, and the antioxidant may also prevent oxidative color changes in the structured protein product and the seafood meat products. 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, m-aminobenzoic acid, o-aminobenzoic acid, p-aminobenzoic acid (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 (e.g., catechin, epicatechin, epicatechin gallate, epigallocatechin (EGC), epigallocatechin gallate (EGCG), polyphenol epigallocatechin-3-gallate), 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, rice bran extract, lactic acid and its salts, lecithin, 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, 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., Ionox 100), 2,4-(tris-3′,5′-bi-tert-butyl-4′-hydroxybenzyl)-mesitylene (i.e., Ionox 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, and combinations thereof.
The concentration of the antioxidant in the meat compositions may range from about 0.0001% to about 20% by weight. In another embodiment, the concentration of an antioxidant in a seafood meat composition may range from about 0.001% to about 5% by weight. In yet another embodiment, the concentration of an antioxidant in a seafood meat composition may range from about 0.01% to about 1% by weight.
(e) Binding Agent
The seafood meat compositions or the simulated seafood meat compositions may also further comprise a binding or gelling agent to improve the texture and/or the appearance of the product. Suitable binding agents include proteins, such as soy protein, pea protein, dairy protein; starches, such as corn starch, wheat starch, potato starch, and the like; alginic acid and its salts; agar; carrageenan and its salts; processed Eucheuma seaweed, gums, such as carob bean, guar, tragacanth, and xanthan; pectins; sodium carboxymethylcellulose, methylcellulose (high viscosity forms), konjac flour, egg white, dried egg white, egg albumin, blood proteins, and bovine serum albumin.
(f) pH-Lowering Agent
In some embodiments, the seafood meat composition or the simulated seafood meat composition may further comprise a pH-lowering agent to increase the chewiness of the final product. In exemplary embodiments, the pH-lowering agent is a food grade edible acid. Non-limiting examples of acids suitable for use in the invention include acetic, lactic, hydrochloric, phosphoric, citric, tartaric, malic, and combinations thereof.
(g) Vitamins and Minerals
Vitamins and minerals may also be included in the seafood meat compositions or the simulated seafood meat compositions. The vitamins may be fat-soluble or water soluble vitamins. Suitable vitamins include vitamin C, vitamin A, vitamin E, vitamin B12, vitamin K, riboflavin, niacin, vitamin D, vitamin B6, folic acid, pyridoxine, thiamine, pantothenic acid, and biotin. The form of the vitamin may include salts of the vitamin, derivatives of the vitamin, compounds having the same or similar activity of a vitamin, and metabolites of a vitamin.
Suitable minerals may include one or more minerals or mineral sources. Non-limiting examples of minerals include, without limitation, chloride, sodium, calcium, iron, chromium, copper, iodine, zinc, magnesium, manganese, molybdenum, phosphorus, potassium, and selenium. Suitable forms of any of the foregoing minerals include soluble mineral salts, slightly soluble mineral salts, insoluble mineral salts, chelated minerals, mineral complexes, non-reactive minerals such as carbonyl minerals, and reduced minerals, and combinations thereof.
(h) Polyunsaturated Fatty Acid
The seafood meat compositions or the simulated seafood meat compositions may also further include a polyunsaturated fatty acid (PUFA), which is a fatty acid having at least two carbon-carbon double bonds generally in the cis-configuration. The PUFA may be a long chain fatty acid having at least 18 carbons atoms. In an exemplary embodiment, the 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 of the carbon chain (i.e., opposite the carboxyl acid group). Examples of omega-3 fatty acids include alpha-linolenic acid (18:3, ALA), stearidonic acid (18:4), eicosatetraenoic acid (20:4), eicosapentaenoic acid (20:5; EPA), docosatetraenoic acid (22:4), n-3 docosapentaenoic acid (22:5, n-3DPA), and docosahexaenoic acid (22:6; DHA). The PUFA may also 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 n-6 docosapentaenoic acid (22:5). The fatty acid may also 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).
(II) Preparing Seafood Meat Compositions and Simulated Seafood Meat Compositions
The process for producing the meat compositions generally comprises hydrating the structured protein product, adding a colorant if necessary, reducing its particle size if necessary, optionally mixing it with animal meat or seafood meat, adding flavoring and other ingredients to the mixture, and further processing the mixture into a food product.
The structured protein product may be mixed with water to rehydrate it. The amount of water added to the structured protein product can and will vary. The ratio of water to structured protein product may range from about 1.5:1 to about 4:1. In one embodiment, the ratio of water to structured protein product may be about 2.5:1. In another embodiment, the ratio of water to structured protein product may be about 3:1.
The concentration of hydrated structured protein product in the meat compositions can and will vary depending upon the product being made. In embodiments comprising a high percentage of seafood meat, the percentage of structured protein product will be low. Whereas, in embodiments without added seafood meat, the percentage of structured protein product will be high. Thus, the concentration of the hydrated structured protein product in the various meat compositions may be about 1%, 2%, 5%, 10%, 15%, 20%, 25%, 30%, 35%, 40%, 45%, 50%, 55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, 95%, or 99% by weight.
The particle size of the structured protein product may be further reduced by grinding, shredding, slicing, cutting, or chopping the hydrated product. The particle size can and will vary depending upon the meat composition being made. Typically, the reduced hydrated product has an average particle size of from about 0.1 mm to about 40.0 mm. In one embodiment, the reduced hydrated product has an average particle size of from about 5.0 mm to about 30.0 mm. In another embodiment, the reduced hydrated product has an average particle size of from about 0.5 mm to about 20.0 mm. In a further embodiment, the reduced hydrated product has an average particle size of from about 0.5 mm to about 15.0 mm. In an additional embodiment, the reduced hydrated product has an average particle size of from about 0.75 mm to about 10.0 mm. In yet another embodiment, the reduced hydrated product has an average particle size of from about 1.0 mm to about 5.0 mm. Suitable apparatus for reducing particle size include meat grinders, bowl choppers, and hammer mills, such as Mikro Hammer Mills manufactured by Hosokawa Micron Ltd., Fitz Mill manufactured by She Hui Machinery Co., Ltd., and Comitrols®, manufactured by Urschel Laboratories, Inc.
B. Optional Blending with Seafood Meat
The hydrated structured protein product may optionally be blended with animal or seafood meat, which was detailed above in section (I)B. In general, the hydrated structured protein product will be blended with seafood meat that has a similar particle size. In some embodiments, the concentration of seafood meat may be about 50%, 55%, 60%, 65%, 70%, 75%, 80%, or 90% by weight, and the concentration of the structured protein product may be about 20%, 15%, 10%, 5%, 4%, 3%, 2%, or 1% by weight. In other embodiments, the concentration of seafood meat may be about 2%, 5%, 10%, 15%, 20%, 25%, 30%, 35%, 40%, 45%, or 50% by weight, and the concentration of the structured protein product may be about 50%, 45%, 40%, 35%, 30%, 25%, 20%, 15%, 10%, or 5% by weight. In one embodiment, the concentration of seafood meat may range from about 60% to about 80% by weight, and the concentration of the structured protein product may range from about 1% to about 20% by weight. In another embodiment, the concentration of seafood meat may range from about 40% to about 60% by weight, and the concentration of the structured protein product may range from about 1% to about 40% by weight. In still another embodiment, the concentration of seafood meat may range from about 20% to about 40% by weight, and the concentration of the structured protein product may range from about 1% to about 60% by weight.
The seafood meat utilized in the seafood meat composition may be raw. Raw meat is preferably provided in at least a substantially frozen form so as to avoid microbial spoilage prior to processing. In one embodiment, the temperature of the seafood meat is below about −40° C. In another embodiment, the temperature of the meat is below about −20° C. In yet another embodiment, the temperature of the meat is from about −10° C. to about 6° C. In a further embodiment, the temperature of the meat is from about −2° C. to about 2° C. While refrigerated or chilled meat may be used, it is generally impractical to store large quantities of unfrozen meat for extended periods of time at a plant site. The frozen products provide a longer lay time than do the refrigerated or chilled products. The frozen meat may be stored at a temperature of about −18° C. to about 0° C. Frozen meat is generally supplied in 20 kilogram blocks. Upon use, the blocks are permitted to thaw up to about 10° C., that is, to defrost, but in a tempered environment. Thus, the outer layer of the blocks, for example up to a depth of about ¼ inch, may be defrosted or thawed but still at a temperature of about 0° C., while the remaining inner portion of the blocks, while still frozen, are continuing to thaw and thus keeping the outer portion at below about 10° C.
In lieu of frozen seafood meat, the seafood meat may be freshly prepared for the preparation of the seafood meat compositions, as long as the freshly prepared seafood meat is stored at a temperature that does not exceed about 10° C.
The moisture content of the raw frozen or unfrozen meat is generally at least about 50% by weight, and most often from about 60% by weight to about 75% by weight, based upon the weight of the raw meat. In embodiments of the invention, the fat content of the raw frozen or unfrozen meat may be at least 1% by weight, generally from about 5% by weight to about 20% by weight. In other embodiments of the invention, meat products having a fat content of less than about 10% by weight and defatted meat products may be used.
In some embodiments, the seafood meat may be pre-cooked to partially dehydrate the flesh and prevent the release of those fluids during further processing applications (e.g., such as retort cooking), to remove natural oils that may have strong flavors, to coagulate the seafood protein and loosen the meat from the skeleton, or to develop desirable and textural flavor properties. The pre-cooking process may be carried out in steam, water, oil, hot air, smoke, and combinations thereof. The seafood meat is generally heated until the internal temperature is between 60° C. and 85° C.
In an additional embodiment, a simulated seafood product is produced that is analogous to seafood meat but does not contain seafood meat. In general the hydrated structured protein product is blended with seafood flavoring to produce the simulated seafood product.
C. Blending with Other Ingredients
The hydrated structured protein product or the mixture of hydrated structured protein product and seafood meat may be blended with water and a variety of flavorings, spices, antioxidants, or other ingredients, as detailed above in section (I)C. As will be appreciated by a skilled artisan, the selection of ingredients added to the seafood meat composition can and will depend upon the food product to be manufactured.
The order in which the ingredients are mixed and blended can and will vary depending upon the product being made. In one embodiment, the seafood meat may be blended with flavorings, colorings, and other ingredients, with the hydrated structured protein product added last. In another embodiment, the seafood meat and the hydrated structured protein may be blended together and then additional ingredients may be added simultaneously or sequentially. In still another embodiment, the seafood meat may be wet cured in a brine solution before being combined with the hydrated structured protein product. In other embodiments, the hydrated structured protein product may be blended with flavorings and other ingredients simultaneously or sequentially (with no added seafood meat).
Irrespective of the order in which the ingredients are combined, the mixture may be blended by stirring, agitating, or mixing the ingredients for a period of time sufficient to form a homogenous mixture. Conventional means for stirring, agitating, blending, or mixing the mixture may be used to effect the blending of the mixture. Ice chips may replace part of the water of the formulation, such that the mixture remains at about 10° C. or less during the blending step(s). Alternatively, carbon dioxide snow may be incorporated during the blending to keep the mixture at about 10° C. or less.
D. Processing into Meat Products
The meat mixture or simulated meat mixture typically will then be processed into a variety of food products having a variety of shapes. The food products produced can be any seafood product known in the industry. Examples include, but are not limited to, cutlets, patties, sticks, nuggets, and fillets. Alternatively, the product may be a smoked meat product, such as smoked salmon, kippered herring, and the like. In yet an additional embodiment, the product may be a wet cured or dry cured meat product, such as dried fish products used for toppings. The product may be a white colored product, such as typically found in patties, sticks, nuggets, and fillets of white-fleshed fish. In an additional embodiment, the seafood meat product may be coated with a batter and/or it may be coated with a breading.
In an additional embodiment, the seafood meat mixture or the simulated seafood meat mixture may be formed into a seafood block product. The seafood block may be wet before optionally being inserted into a casing. The casing may be a permeable casing, such as a cellulose casing, a fibrous casing, a collagen casing, or a natural membrane. In another embodiment, the seafood meat mixture may be formed into loaves, rolls, cutlets, patties, links, or other shapes before being processed further. The formed seafood mixture may be coated with a batter and/or it may be coated with a breading. Alternatively, the formed seafood mixture may then be sliced, cubed, chunked, or shredded. In yet another embodiment, the seafood mixture or may be introduced into a sealable package, pouch, or can for further processing.
After the mixture is formed into the desired shape or introduced into the desired package, the food product may be further processed. The processing may include cooking, partial cooking, freezing, retorting, or any method known in the art for producing a shelf stable product. In one embodiment, the formed food product may be cooked on-site. Any method known in the art for cooking the final meat product may be used. Non-limiting examples of cooking methods include hot water cooking, steam cooking, par-boiling, par-frying, frying, retort cooking, hot smoke cooking under controlled humidity, and oven methods, including microwave, traditional, and convection. Typically, a meat product is cooked to an internal temperature of at least 70° C. Prior to cooking, some meat products may be wet cured or dried cured by storing them at a temperature of about 10° C. for a period of time. Furthermore, some meat products may be subjected to a period of smoking before or during cooking.
In one embodiment, the meat product may be cooked in a hot water cooker, preferably at about 80° C., to an internal temperature of about 70° C. to about 80° C. In another embodiment, the meat product may be steam cooked, to an internal temperature of about 70° C. to about 80° C. In an alternative embodiment, the meat product may be par-fried in 190° C. oil and then cooked to an internal temperature of about 74° C. in a humidity controlled oven. In another embodiment, the meat product, either cooked or uncooked, may be packed and sealed in cans in a conventional manner and employing conventional sealing procedures in preparation for sterilization by retorting. In still another embodiment, the final meat product may be partially cooked for finishing at a later time, or frozen either in an uncooked state, partially cooked state, or cooked state. While a simulated seafood meat product comprising structured protein product may not have to be cooked to the same internal temperature as products containing animal meat, they generally are heated to a temperature sufficient to congeal the optional binding agent(s), remove excess moisture, or stabilize the product. The foregoing products may be sealed in plastic, placed in a tray with overwrap, vacuum packed, frozen, or retorted.
The term “seafood meat” as used herein refers to the muscles, organs, and by-products thereof derived from a freshwater or saltwater fish or shellfish.
The term “comminuted meat” as used herein refers to a meat paste that is recovered from a land or aquatic animal carcass. The meat, on the bone is forced through a deboning device such that the meat is separated from the bone and reduced in size. Meat that is off the bone would not be further treated with a deboning device. The meat is separated from the meat/bone mixture by forcing through a cylinder with small diameter holes. The meat acts as a liquid and is forced through the holes while the remaining bone material remains behind. The fat content of the comminuted meat may be adjusted upward by the addition of seafood fat.
The term “extrudate” as used herein refers to the product of extrusion. In this context, the structured 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 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 2 is performed.
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 “animal meat” as used herein refers to the flesh, whole meat muscle, organs, parts and by-products thereof derived from an animal including land and aquatic animals further including, beef, pork, poultry, wild game, fish, shellfish, and combinations thereof.
The term “large piece” as used herein is the manner in which a structured protein product's shred percentage is characterized. The determination of shred characterization is detailed in Example 2.
The term “meat emulsion” or “emulsified meat” as used herein refers to a flowable meat product, such as a meat slurry, where the meat is more malleable than unprocessed meats.
The term “simulated” as used herein refers to an animal meat composition that contains no animal meat.
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 protein products of the invention. Additionally, because the 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 protein products.
The term “soy cotyledon fiber” as used herein refers to the polysaccharide portion of soy cotyledons containing at least about 70% dietary fiber. 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, 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 flour” as used herein, refers to full fat soy flour, enzyme-active soy flour, defatted soy flour, and mixtures thereof. Defatted soy flour 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 material are comminuted into 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 four is retained on a 300 mesh (U.S. Standard) screen. Full fat soy flour refers to ground whole soybeans containing all of the original oil, usually 18% to 20%. The flour may be enzyme-active or it may be heat-processed or toasted to minimize enzyme activity. Enzyme-active soy flour refers to a full fat soy flour that has been minimally heat-treat in order not to neutralize its natural enzyme.
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, 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 soluble carbohydrates of the cotyledon.
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 “starch” as used herein refers to starches derived from any native source. Typically sources for starch are cereals, tubers, roots, and fruits.
The term “strand” as used herein refers to a structured 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 2 is performed.
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 to about 120 μm.
The invention having been generally described above, may be better understood by reference to the examples described below. The following examples represent specific but non-limiting embodiments of the present invention.
The following examples illustrate properties of the structure protein product and various meat compositions of the invention.
Shear strength of a sample is measured in grams and may be determined by the following procedure. Weigh a sample of the structured 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 shear through the sample.
A procedure for determining shred characterization may be performed as follows. Weigh about 150 grams of a structured 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 about 0.2 cm wide. Group 3 is the portion that is discarded since it does not fit within the parameters of Group 1 or Group 2, the sample amount left for discard in Group 3 is minimal. 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 colored structured protein products of the invention, similar to as those utilized in Examples 1 and 2. As an example, a red colored structured protein product is made by combining the ingredients listed in Table 1 in a paddle blender.
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 water to form a conditioned soy protein pre-mixture. The conditioned soy protein pre-mixture is then fed to a twin-screw extrusion apparatus at a rate of not more than 75 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 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.
Fish patties comprising ground fish meat and white-colored SPP may be prepared according to the formulation presented in Table 2. See
The fish patty is prepared using the formulation percentages in Table 2. In a Kitchen Aid mixer model KM14GO (or equivalent) with a bowl and single blade paddle, 100 grams of SPP is added to 300 grams of tap water and mixed on slow speed for 2 minutes. Once the SPP has started hydration, the mixture is then mixed at high speed until the fibers are separated. Upon separation of the fibers 572.7 grams of fish trim are added to the bowl and mixed for one minute on low speed followed by adding the remaining ingredients (10 grams salt, 10 grams dried onion, 5 grams dried dill, 0.8 grams Herbalox, and 1.5 grams white pepper) for one minute on low speed. The resulting mix is then formed into patties and cooked. Optionally the patties may be battered and breaded with about 27.4% (final dry weight basis) and cooked.
The following extrusion process may be used to prepare the fish product, similar to as those utilized in Examples 1 and 2. As an example, an amount of minced fish meat is included in the process producing a fish product that includes an amount of structured protein products. The fish product is prepared using the formulation percentages in Table 3. In a Kitchen Aid mixer KM14GO (or equivalent) with a bowl and single blade paddle, the amount of 300 grams of ice water (80:20) and 0.3 grams TiO2 are combined in the bowl. Additionally, 100 grams of SuproMax 5050 is added and mixed on slow speed for 2 minutes. Once the SuproMax has started hydration, the mixture is then mixed at high speed until the fibers are separated. After the fibers are separated 450 grams of minced fish (4 degrees C.) are added and mixed for 1 minute on low speed. Then 65 grams of SuproMax 6010 are added and mixed for 1 minute on low speed. Finally, the remaining ingredients (11.2 grams salt, 70 grams vegetable oil, 0.3 grams sodium erythorbate, and 3 grams of lactic acid) are added to the mixture and mixed for 1 minute on low speed. The resulting mix is then formed and cooked. Optionally, if patties are formed they may be battered and breaded with about 27.4% (final dry weight basis) and cooked.
The following extrusion process may be used to prepare the fish product, similar to as those utilized in Examples 1 and 2. As an example, an amount of minced fish meat is included in the process producing a fish product that includes an amount of structured protein products. The fish product is prepared using the formulation percentages in Table 3. In a Kitchen Aid mixer KM14GO (or equivalent) with a bowl and single blade paddle, the amount of 300 grams of water are combined with 100 grams of SPP and mixed on slow speed for 2 minutes. Once the SPP has started hydration, the mixture is then mixed at high speed until the fibers are separated. After the fibers are separated 500 grams of fish trim and 62.7 grams of chicken breast meat, that has been ground to 3 mm, are added and mixed for 1 minute on low speed. Then 10 grams of salt and 10 grams of ISP are added and mixed for 1 minute on low speed. Finally, the remaining ingredients (10 grams dried onion, 0.8 grams Herbalox, and 1.5 grams of white pepper) are added to the mixture and mixed for 1 minute on low speed. The resulting mix is then formed into patties and cooked. Optionally, the patties may be battered and breaded with about 27.4% (final dry weight basis) and cooked.
While the invention has been explained in relation to exemplary embodiments, it is to be understood that various modifications thereof will become apparent to those skilled in the art upon reading the description. Therefore, it is to be understood that the invention disclosed herein is intended to cover such modifications as fall within the scope of the appended claims.
This application claims priority from U.S. Provisional Application Ser. No. 60/910,903 filed on Apr. 10, 2007, which is hereby incorporated by reference in its entirety.
| Number | Date | Country | |
|---|---|---|---|
| 60910903 | Apr 2007 | US |
