USH35H - Freeze dried cooked meats - Google Patents
Freeze dried cooked meats Download PDFInfo
- Publication number
- USH35H USH35H US06/665,899 US66589984A USH35H US H35 H USH35 H US H35H US 66589984 A US66589984 A US 66589984A US H35 H USH35 H US H35H
- Authority
- US
- United States
- Prior art keywords
- meat
- water
- gum
- cooking
- meats
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- 235000013372 meat Nutrition 0.000 title claims abstract description 89
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 37
- 238000010411 cooking Methods 0.000 claims abstract description 25
- 238000000034 method Methods 0.000 claims abstract description 17
- 239000004615 ingredient Substances 0.000 claims abstract description 13
- 235000013622 meat product Nutrition 0.000 claims abstract description 12
- 150000003839 salts Chemical class 0.000 claims abstract description 12
- 239000011159 matrix material Substances 0.000 claims abstract description 11
- 229910019142 PO4 Inorganic materials 0.000 claims abstract description 9
- 230000018044 dehydration Effects 0.000 claims abstract description 9
- 238000006297 dehydration reaction Methods 0.000 claims abstract description 9
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims abstract description 5
- 239000010452 phosphate Substances 0.000 claims abstract description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 12
- 239000000203 mixture Substances 0.000 claims description 11
- 238000002156 mixing Methods 0.000 claims description 8
- 235000021317 phosphate Nutrition 0.000 claims description 8
- 235000019832 sodium triphosphate Nutrition 0.000 claims description 8
- 150000003013 phosphoric acid derivatives Chemical class 0.000 claims description 6
- 239000011780 sodium chloride Substances 0.000 claims description 6
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 4
- 239000001913 cellulose Substances 0.000 claims description 4
- 235000010980 cellulose Nutrition 0.000 claims description 4
- 229920002678 cellulose Polymers 0.000 claims description 4
- 230000008569 process Effects 0.000 claims description 4
- 108090000623 proteins and genes Proteins 0.000 claims description 4
- 102000004169 proteins and genes Human genes 0.000 claims description 4
- 244000215068 Acacia senegal Species 0.000 claims description 3
- 229920000084 Gum arabic Polymers 0.000 claims description 3
- 229920002774 Maltodextrin Polymers 0.000 claims description 3
- 229920000168 Microcrystalline cellulose Polymers 0.000 claims description 3
- 235000010489 acacia gum Nutrition 0.000 claims description 3
- 239000000205 acacia gum Substances 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims description 3
- 238000000227 grinding Methods 0.000 claims description 3
- 229920000591 gum Polymers 0.000 claims description 3
- 235000019813 microcrystalline cellulose Nutrition 0.000 claims description 3
- 239000008108 microcrystalline cellulose Substances 0.000 claims description 3
- 229940016286 microcrystalline cellulose Drugs 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 229920001285 xanthan gum Polymers 0.000 claims description 3
- 241000416162 Astragalus gummifer Species 0.000 claims description 2
- 229920002907 Guar gum Polymers 0.000 claims description 2
- 229920000161 Locust bean gum Polymers 0.000 claims description 2
- 229920001615 Tragacanth Polymers 0.000 claims description 2
- -1 arabino gallactan Polymers 0.000 claims description 2
- 239000001768 carboxy methyl cellulose Substances 0.000 claims description 2
- 210000002808 connective tissue Anatomy 0.000 claims description 2
- 235000010417 guar gum Nutrition 0.000 claims description 2
- 239000000665 guar gum Substances 0.000 claims description 2
- 229960002154 guar gum Drugs 0.000 claims description 2
- 229940005740 hexametaphosphate Drugs 0.000 claims description 2
- 239000000416 hydrocolloid Substances 0.000 claims description 2
- 235000010420 locust bean gum Nutrition 0.000 claims description 2
- 239000000711 locust bean gum Substances 0.000 claims description 2
- 239000001267 polyvinylpyrrolidone Substances 0.000 claims description 2
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 claims description 2
- 229920000036 polyvinylpyrrolidone Polymers 0.000 claims description 2
- 239000001103 potassium chloride Substances 0.000 claims description 2
- 235000011164 potassium chloride Nutrition 0.000 claims description 2
- 238000009966 trimming Methods 0.000 claims description 2
- UNXRWKVEANCORM-UHFFFAOYSA-I triphosphate(5-) Chemical class [O-]P([O-])(=O)OP([O-])(=O)OP([O-])([O-])=O UNXRWKVEANCORM-UHFFFAOYSA-I 0.000 claims description 2
- DPXJVFZANSGRMM-UHFFFAOYSA-N acetic acid;2,3,4,5,6-pentahydroxyhexanal;sodium Chemical compound [Na].CC(O)=O.OCC(O)C(O)C(O)C(O)C=O DPXJVFZANSGRMM-UHFFFAOYSA-N 0.000 claims 1
- 230000001804 emulsifying effect Effects 0.000 claims 1
- 230000008014 freezing Effects 0.000 claims 1
- 238000007710 freezing Methods 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 claims 1
- 238000004806 packaging method and process Methods 0.000 claims 1
- 235000019812 sodium carboxymethyl cellulose Nutrition 0.000 claims 1
- 229920001027 sodium carboxymethylcellulose Polymers 0.000 claims 1
- FQENQNTWSFEDLI-UHFFFAOYSA-J sodium diphosphate Chemical class [Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OP([O-])([O-])=O FQENQNTWSFEDLI-UHFFFAOYSA-J 0.000 claims 1
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical class [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 claims 1
- 229940048086 sodium pyrophosphate Drugs 0.000 claims 1
- 239000007787 solid Substances 0.000 claims 1
- 235000019818 tetrasodium diphosphate Nutrition 0.000 claims 1
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 claims 1
- 239000003925 fat Substances 0.000 description 5
- 235000013305 food Nutrition 0.000 description 5
- 102000003505 Myosin Human genes 0.000 description 4
- 108060008487 Myosin Proteins 0.000 description 4
- 235000015177 dried meat Nutrition 0.000 description 4
- 238000011067 equilibration Methods 0.000 description 4
- 241000287828 Gallus gallus Species 0.000 description 3
- 108010070551 Meat Proteins Proteins 0.000 description 3
- 235000015278 beef Nutrition 0.000 description 3
- 210000004027 cell Anatomy 0.000 description 3
- 235000013330 chicken meat Nutrition 0.000 description 3
- 238000004132 cross linking Methods 0.000 description 3
- 230000006870 function Effects 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 235000015277 pork Nutrition 0.000 description 3
- 235000019687 Lamb Nutrition 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 210000000170 cell membrane Anatomy 0.000 description 2
- 230000002708 enhancing effect Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 210000000416 exudates and transudate Anatomy 0.000 description 2
- 238000004108 freeze drying Methods 0.000 description 2
- 238000003505 heat denaturation Methods 0.000 description 2
- 230000036571 hydration Effects 0.000 description 2
- 238000006703 hydration reaction Methods 0.000 description 2
- 230000003204 osmotic effect Effects 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 235000020995 raw meat Nutrition 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000002459 sustained effect Effects 0.000 description 2
- 210000001519 tissue Anatomy 0.000 description 2
- 235000010493 xanthan gum Nutrition 0.000 description 2
- 239000000230 xanthan gum Substances 0.000 description 2
- 229940082509 xanthan gum Drugs 0.000 description 2
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- 102000008186 Collagen Human genes 0.000 description 1
- 108010035532 Collagen Proteins 0.000 description 1
- 239000005913 Maltodextrin Substances 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 229920000881 Modified starch Polymers 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 235000020996 boneless meat Nutrition 0.000 description 1
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 230000003915 cell function Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 229920001436 collagen Polymers 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- XPPKVPWEQAFLFU-UHFFFAOYSA-J diphosphate(4-) Chemical class [O-]P([O-])(=O)OP([O-])([O-])=O XPPKVPWEQAFLFU-UHFFFAOYSA-J 0.000 description 1
- 235000011180 diphosphates Nutrition 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 235000021582 food-grade substance Nutrition 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 230000003834 intracellular effect Effects 0.000 description 1
- 210000003734 kidney Anatomy 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 229940035034 maltodextrin Drugs 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 235000019426 modified starch Nutrition 0.000 description 1
- 210000003205 muscle Anatomy 0.000 description 1
- 235000019629 palatability Nutrition 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000035790 physiological processes and functions Effects 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 235000013594 poultry meat Nutrition 0.000 description 1
- 235000013613 poultry product Nutrition 0.000 description 1
- 235000013324 preserved food Nutrition 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 235000020989 red meat Nutrition 0.000 description 1
- 239000004627 regenerated cellulose Substances 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 235000013580 sausages Nutrition 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 235000013547 stew Nutrition 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23B—PRESERVATION OF FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES; CHEMICAL RIPENING OF FRUIT OR VEGETABLES
- A23B4/00—Preservation of meat, sausages, fish or fish products
- A23B4/03—Drying; Subsequent reconstitution
- A23B4/037—Freeze-drying, i.e. cryodesiccation or lyophilisation; Apparatus therefor
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L13/00—Meat products; Meat meal; Preparation or treatment thereof
- A23L13/50—Poultry products, e.g. poultry sausages
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L13/00—Meat products; Meat meal; Preparation or treatment thereof
- A23L13/60—Comminuted or emulsified meat products, e.g. sausages; Reformed meat from comminuted meat product
Definitions
- This invention relates to a method of producing freeze-dried cooked meats which rehydrate rapidly and avoid problems caused by meats which do not rehydrate fully, and, typically have numerous unpalatable hard spots. This improvement is accomplished by expanding the matrix of the meat so as to provide pathways for water to rehydrate the meat.
- freeze drying is the least detrimental to meat texture and rehydratability. Freeze drying, the sublimation of ice to water vapor under vacuum, results in drying without significant change in product volume. The meat matrices obtained are therefore significantly more porous that those of meats dried by other means. While the rate and extent of rehydration of freeze dried meats is superior to that of meat items otherwise dried, rehydration remains relatively slow and incomplete, resulting in "hard spots" in cooked rehydrated meats.
- Dehydrated cooked meats may be the meat component of stews; or steaks, chops or pattie-like products.
- cooked meats destined to be freeze dried are heated to an internal temperature of 140° F. or more by dry or moist heat resulting in pre-dehydration moisture and fat cook-out in the range of 25%-50% of the meat's raw weight.
- Cooking also results in disruption of cell membrane function and in coagulation of intercellular and intracellular proteins.
- the heat denaturation of meat proteins creates a largely static condition with respect to water and substances in solution within and external to cells which comprise meat tissue.
- the mass of individual cells imbibe or excrete water in response to changes in osmotic pressures as a result of changes in solute level, thereby maintaining optimum solute/solvent concentration for cell function.
- Fresh, raw meats retain much of this function which cooking largely destroys. Changes in meat density and its physiological state as a result of heat denaturation contribute directly to problems relative to the rehydration of meats which have been cooked and subsequently freezed dried.
- Rehydration of freeze dried cooked meat generally involves its immersion in 150° F. or warmer water. Since cooked meat protein is largely denatured and cell membranes no longer function effectively with respect to osmotic gradient changes, hydration occurs primarily by absorption. Water moves gradually from surface to center of the meat particles, the rate of absorption being dependent on a number of factors including the dried meat's affinity for water, its density, its volume, the amount of fat, the degree of myofibrillar protein cross linking, the concentration of salts and their availability, the temperature to which the meat was cooked initially and the temperature of the rehydration water. These factors are directly affected by cooking. Meat protein which has been denatured due to cooking loses much of its affinity for water.
- This invention provides a method of producing dehydrated cooked meat products which more easily and completely rehydrate than previously made dehydrated meats. This is accomplished by expansion of the cooked meat matrix by the addition of water, salt, food grade phosphates and adjunctive hydrophilic ingredients prior to cooking.
- This invention is intended for use on formed meats which may consist of a combination of flaked, chunked, ground or emulsified meats.
- the use of a gas and moisture impermeable casing for cooking the meat allows the meat to be fully cooked without concurrent losses in either weight or volume, thus preventing density increase prior to dehydration.
- the practicing of this invention results in a dehydrated meat product which has an expanded meat matrix.
- the expanded matrix allows the meat to be more easily and completely rehydratable.
- Boneless meat is used which may be from any suitable meat cut from any animal species which is customerily used as a source of food for human consumption. Typically, it is expected that the meat will be beef, veal, lamb, pork, chicken or turkey. The meat is trimmed of all heavy connective tissue and excess fat. Trimming is essential if rehydration is to be complete. Then it is cut into pieces suitable for grinding, flaking or chunking. Up to 50 percent, but usually not more than 15 percent of the meat, is ground twice through a 0.125 inch grinder plate or emulsified in a bowl chopper.
- the balance of the meat may be flaked or chunked into particles having a volume of 0.001 cubic inches or larger, but which are more typically 2.5-6 cubic inches in volume. Flaked meat may be used but chunked meat is preferred in the practice of this invention.
- the particular brand of flaking machine used is the Urschiell Comitrol comminution machine, although other standard machines are acceptable.
- the actual size of the flaking head in the machine can vary from 1/4" to 1", although the larger size is preferred.
- the flakes generated are approximately 1/32" to 1.0" thick.
- a conventional grinding machine equipped with a kidney plate having minimum openings of 2.5 inches may be used for producing meat chunks of suitable size.
- the finely ground or emulsified meat and the chunked or flaked meat are mixed with water which may be added in the range of 1.0% to 10.0% of formula weight, but is more typically added in the range of 2.0% to 6.0% of the formula weight. If more than 10% water is added, some of the water will be purged from the meat during the cooking.
- Salt may be added in amounts in the range of 0.1% to 5.0%, but more typically 0.5% to 2.0% of the formula weight and a food grade phosphate, such as sodium tripolyphosphate may be added in amounts of 0.1% to 0.5%, but more typically about 0.5% of the formula weight.
- the salts which may be used include sodium chloride and potassium chloride.
- Food grade phosphates which are effective include the sodium salts of pyrophosphate, orthophosphate, hexametaphosphate or tripolyphosphate or mixtures thereof.
- Adjunctive, hydrophilic ingredients are added to act as matrix expansion aids, wicking agents and inhibitors of myosin cross linking thereby enhancing the rate and extent of rehydration of freeze dried cooked meats.
- Cellulose derived food grade substances such as carboxymethyl cellulose and microcrystalline cellulose and mixtures thereof have been shown to be effective hydration aids and emulsion stabilizers in the range of 0.5% to 10.0% of the free water content of the meat but their most effective use level is in the range of 0.5% to 5.0%.
- Gum such as gum arabic, polyvinylpyrrolidone, arabino gallactan, xanthan gum, kayara gum, guar gum, gum tragacanth, locust bean gum and mixtures of these in amounts in the range of 0.5% to 5.0% of formula weight. Malto dextrins and other hydrocolloids may be used in levels in the same range.
- the meat and the added ingredients are mechanically mixed or tumbled until sufficient myofibrillar proteins are extracted to render the mixture moderately tacky.
- the product is then mixed, ideally at 40° F. for sufficient time to allow the added soluble substances to equilibrate throughout the mixture. Full equilibration depends on temperature, method of mixing and duration of mixing. A post-mixing quiescent equilibration periodd typically lasting 8 to 16 hours may be used in lieu of prolonged mixing, massaging or tumbling.
- the mixture is generally remixed following equilibration to assure sufficient plasticity to enable pumping through a commercial stuffing machine.
- the mixture is then stuffed into moisture and gas impermeable flexible containers such as, but not limited to, casings used to protect hams, restructured roasts, and sausages.
- the casing used must be essentially water impervious and have an oxygen transmission rate of not more than 10 cc of O 2 /meter 2 /0.001 inch thickness/24 hours at 20° C. and 0% relative humidity.
- a casing which meets these requirements is manufactured by Walsroder Co. of Chicago, Il. This casing has a fibrous cellulose exterior laminated onto a saran film interior.
- the technique for filling or stuffing the casings or other container is critical to the success of the cooking process, which must rapidly follow the stuffing procedure.
- the casing fits tightly to the surface of the meat so as to keep moisture in equilibrium within said meat product during cooking.
- the filled container must be uniformly free of voids within the mixture and at the interface of the meat and the casings. The absence of voids prevents the water present in the meat from being purged during cooking.
- the closure of the casings may be, but are not limited to, metal clips or thermal welds and must be watertight.
- a different cooking procedure must be followed in cooking poultry products such as chicken and turkey to avoid purge.
- a two-stage process is followed of initiating and maintaining cooking at 150° F. and 100% relative humidity for two hours and then at 175° F. and 100% relative humidity until the product's center temperature reaches 162° F.
- the poultry logs are then rapidly cooled to 40° F. or below.
- the cooked logs are then frozen and subsequently sliced, diced or cubed into appropriate portion sizes.
- the portioned meats are then subjected to vacuum freeze dehydration to about a 1.5 to 2.0% moisture level.
- the freeze dried meats are then packages in an airtight container in the absence of oxygen.
- the freeze dried meat matrices obtained by this process are significantly less dense and contain significantly less rendered fat than those obtained from conventionally cooked meats and have a strong affinity for water.
- the rate and extent of rehydration of cooked meats prepared for dehydration by the method of this invention is therefore significantly superior to that of meat cooked by other methods.
- Test results showed that meat cooked in the fibrous/saran casing described above sustained 0% moisture loss during cooking while meat prepared similarly except that a moisture permeable casing made from regenerated cellulose used sustained a 30% moisture loss.
- Each of these meat logs was frozen, sliced and freeze dehydrated. Upon rehydration with 180° F. water the meat which had no moisture loss during cooking rehydrated totally in 8 minutes while the meat which lost 30% of the moisture during cooking was only 50% rehydrated in 18 minutes.
- the addition of the matrix expanding ingredients resulted in a meat product 20%-30% less dense than a similarly prepared meat product which did not contain the matrix expanding ingredients.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Meat, Egg Or Seafood Products (AREA)
Abstract
This invention provides a method of producing dehydrated meat products wh more easily and completely rehydrate than prior art dehydrated meats. This is accomplished by expansion of the cooked meat matrix by the addition of water, salt, phosphate and adjunctive hydrophilic ingredients prior to cooking. This invention is intended for use with formed meats consisting of a combination of chunked, flaked and ground or emulsified meats. The use of a gas and moisture impermeable casing for cooking the meat allows the meat to be fully cooked without concurrent losses in either weight or volume, thus preventing density increase prior to dehydration.
Description
The invention described herein may be manufactured, used, and licensed by or for the Government for governmental purposes without the payment to me of any royalty thereon.
This invention relates to a method of producing freeze-dried cooked meats which rehydrate rapidly and avoid problems caused by meats which do not rehydrate fully, and, typically have numerous unpalatable hard spots. This improvement is accomplished by expanding the matrix of the meat so as to provide pathways for water to rehydrate the meat.
It is well known that foods may be preserved for long periods by dehydration and that dehydrated meat items frequently do not rehydrate quickly or to the extent required for optimum palatability and tenderness. Among dehydration methods, freeze drying is the least detrimental to meat texture and rehydratability. Freeze drying, the sublimation of ice to water vapor under vacuum, results in drying without significant change in product volume. The meat matrices obtained are therefore significantly more porous that those of meats dried by other means. While the rate and extent of rehydration of freeze dried meats is superior to that of meat items otherwise dried, rehydration remains relatively slow and incomplete, resulting in "hard spots" in cooked rehydrated meats.
In order to produce dehydrated meats requiring only rehydration prior to their being consumed, they must be cooked prior to their being dried. Dehydrated cooked meats may be the meat component of stews; or steaks, chops or pattie-like products. Typically, cooked meats destined to be freeze dried are heated to an internal temperature of 140° F. or more by dry or moist heat resulting in pre-dehydration moisture and fat cook-out in the range of 25%-50% of the meat's raw weight.
Cooking also results in disruption of cell membrane function and in coagulation of intercellular and intracellular proteins. The heat denaturation of meat proteins creates a largely static condition with respect to water and substances in solution within and external to cells which comprise meat tissue. In living tissue, the mass of individual cells imbibe or excrete water in response to changes in osmotic pressures as a result of changes in solute level, thereby maintaining optimum solute/solvent concentration for cell function. Fresh, raw meats retain much of this function which cooking largely destroys. Changes in meat density and its physiological state as a result of heat denaturation contribute directly to problems relative to the rehydration of meats which have been cooked and subsequently freezed dried.
Rehydration of freeze dried cooked meat generally involves its immersion in 150° F. or warmer water. Since cooked meat protein is largely denatured and cell membranes no longer function effectively with respect to osmotic gradient changes, hydration occurs primarily by absorption. Water moves gradually from surface to center of the meat particles, the rate of absorption being dependent on a number of factors including the dried meat's affinity for water, its density, its volume, the amount of fat, the degree of myofibrillar protein cross linking, the concentration of salts and their availability, the temperature to which the meat was cooked initially and the temperature of the rehydration water. These factors are directly affected by cooking. Meat protein which has been denatured due to cooking loses much of its affinity for water. Conventional cooking methods increase meat density by evaporative and syneresis effects and cause rendered fats to coagulate in interstitial spaces within the meat structure, thus further inhibiting penetration by water in meat which has been dried. Increased meat density may heighten the potential for myosin cross linking, which also inhibits rehydration. Obtaining hot water and maintaining its temperature for sufficient time to rehydrate the meat is not always practicable for the military. As a result, the cooked meat components of freeze dried foods of the prior art are slow to rehydrate, do not fully rehydrate and often contain numerous unpalatable "hard spots".
SUMMARY OF THE INVENTION
This invention provides a method of producing dehydrated cooked meat products which more easily and completely rehydrate than previously made dehydrated meats. This is accomplished by expansion of the cooked meat matrix by the addition of water, salt, food grade phosphates and adjunctive hydrophilic ingredients prior to cooking. This invention is intended for use on formed meats which may consist of a combination of flaked, chunked, ground or emulsified meats. The use of a gas and moisture impermeable casing for cooking the meat allows the meat to be fully cooked without concurrent losses in either weight or volume, thus preventing density increase prior to dehydration.
The practicing of this invention results in a dehydrated meat product which has an expanded meat matrix. The expanded matrix allows the meat to be more easily and completely rehydratable. Boneless meat is used which may be from any suitable meat cut from any animal species which is customerily used as a source of food for human consumption. Typically, it is expected that the meat will be beef, veal, lamb, pork, chicken or turkey. The meat is trimmed of all heavy connective tissue and excess fat. Trimming is essential if rehydration is to be complete. Then it is cut into pieces suitable for grinding, flaking or chunking. Up to 50 percent, but usually not more than 15 percent of the meat, is ground twice through a 0.125 inch grinder plate or emulsified in a bowl chopper. The balance of the meat may be flaked or chunked into particles having a volume of 0.001 cubic inches or larger, but which are more typically 2.5-6 cubic inches in volume. Flaked meat may be used but chunked meat is preferred in the practice of this invention. The particular brand of flaking machine used is the Urschiell Comitrol comminution machine, although other standard machines are acceptable. The actual size of the flaking head in the machine can vary from 1/4" to 1", although the larger size is preferred. The flakes generated are approximately 1/32" to 1.0" thick. A conventional grinding machine equipped with a kidney plate having minimum openings of 2.5 inches may be used for producing meat chunks of suitable size.
The finely ground or emulsified meat and the chunked or flaked meat are mixed with water which may be added in the range of 1.0% to 10.0% of formula weight, but is more typically added in the range of 2.0% to 6.0% of the formula weight. If more than 10% water is added, some of the water will be purged from the meat during the cooking. Salt may be added in amounts in the range of 0.1% to 5.0%, but more typically 0.5% to 2.0% of the formula weight and a food grade phosphate, such as sodium tripolyphosphate may be added in amounts of 0.1% to 0.5%, but more typically about 0.5% of the formula weight. The salts which may be used include sodium chloride and potassium chloride. Food grade phosphates which are effective include the sodium salts of pyrophosphate, orthophosphate, hexametaphosphate or tripolyphosphate or mixtures thereof.
Adjunctive, hydrophilic ingredients are added to act as matrix expansion aids, wicking agents and inhibitors of myosin cross linking thereby enhancing the rate and extent of rehydration of freeze dried cooked meats. Cellulose derived food grade substances such as carboxymethyl cellulose and microcrystalline cellulose and mixtures thereof have been shown to be effective hydration aids and emulsion stabilizers in the range of 0.5% to 10.0% of the free water content of the meat but their most effective use level is in the range of 0.5% to 5.0%. Gum, such as gum arabic, polyvinylpyrrolidone, arabino gallactan, xanthan gum, kayara gum, guar gum, gum tragacanth, locust bean gum and mixtures of these in amounts in the range of 0.5% to 5.0% of formula weight. Malto dextrins and other hydrocolloids may be used in levels in the same range.
Mechanical mixing or massaging of the larger particles of meat in the presence of salt, sodium tripolyphosphate and the finely ground or flaked meat initially results in the extraction of a tacky myosin exudate. This permits forming of the meat flakes or chunks into cohesive logs of any desired geometry. The salts and phosphates in addition to aiding in the extraction of the myosin exudate, increase the water holding capacity of the raw meat. The addition of these solutes and water causes swelling of raw intact muscle and collagen cells, enhancing expansion of the meat matrix. The hydrophillic colloids, cellulose or starch derivatives, because of their affinity for water, assist in the retention of added water within the meat matrix during cooking. A relatively open cooked meat structure having a strong affinity for water after freeze dehydration is the result of adding the above ingredients and subsequently cooking the meat by no-purge techniques.
The meat and the added ingredients are mechanically mixed or tumbled until sufficient myofibrillar proteins are extracted to render the mixture moderately tacky. The product is then mixed, ideally at 40° F. for sufficient time to allow the added soluble substances to equilibrate throughout the mixture. Full equilibration depends on temperature, method of mixing and duration of mixing. A post-mixing quiescent equilibration periodd typically lasting 8 to 16 hours may be used in lieu of prolonged mixing, massaging or tumbling.
If a still equilibration period is employed, the mixture is generally remixed following equilibration to assure sufficient plasticity to enable pumping through a commercial stuffing machine. The mixture is then stuffed into moisture and gas impermeable flexible containers such as, but not limited to, casings used to protect hams, restructured roasts, and sausages. The casing used must be essentially water impervious and have an oxygen transmission rate of not more than 10 cc of O2 /meter2 /0.001 inch thickness/24 hours at 20° C. and 0% relative humidity. A casing which meets these requirements is manufactured by Walsroder Co. of Chicago, Il. This casing has a fibrous cellulose exterior laminated onto a saran film interior. The technique for filling or stuffing the casings or other container is critical to the success of the cooking process, which must rapidly follow the stuffing procedure. The casing fits tightly to the surface of the meat so as to keep moisture in equilibrium within said meat product during cooking. The filled container must be uniformly free of voids within the mixture and at the interface of the meat and the casings. The absence of voids prevents the water present in the meat from being purged during cooking. The closure of the casings may be, but are not limited to, metal clips or thermal welds and must be watertight.
Following stuffing, red meat, such as beef, pork, veal and lamb must be cooked at temperatures not to exceed 162° F. and at 100% relative humidity. The center temperature of the meat logs may not exceed 150° F., and must be rapidly cooled to 40° F. or below immediately upon reaching this maximum center temperature. During the cooking of the meat logs, the temperature of the cooking medium must be maintained at least 10° F. than the center temperature of the meat log.
A different cooking procedure must be followed in cooking poultry products such as chicken and turkey to avoid purge. A two-stage process is followed of initiating and maintaining cooking at 150° F. and 100% relative humidity for two hours and then at 175° F. and 100% relative humidity until the product's center temperature reaches 162° F. The poultry logs are then rapidly cooled to 40° F. or below.
The cooked logs are then frozen and subsequently sliced, diced or cubed into appropriate portion sizes. The portioned meats are then subjected to vacuum freeze dehydration to about a 1.5 to 2.0% moisture level. The freeze dried meats are then packages in an airtight container in the absence of oxygen. The freeze dried meat matrices obtained by this process are significantly less dense and contain significantly less rendered fat than those obtained from conventionally cooked meats and have a strong affinity for water. The rate and extent of rehydration of cooked meats prepared for dehydration by the method of this invention is therefore significantly superior to that of meat cooked by other methods.
Test results showed that meat cooked in the fibrous/saran casing described above sustained 0% moisture loss during cooking while meat prepared similarly except that a moisture permeable casing made from regenerated cellulose used sustained a 30% moisture loss. Each of these meat logs was frozen, sliced and freeze dehydrated. Upon rehydration with 180° F. water the meat which had no moisture loss during cooking rehydrated totally in 8 minutes while the meat which lost 30% of the moisture during cooking was only 50% rehydrated in 18 minutes. The addition of the matrix expanding ingredients resulted in a meat product 20%-30% less dense than a similarly prepared meat product which did not contain the matrix expanding ingredients.
The following examples are only a few of the possible combinations of ingredients which when processed in accordance with this invention are found to readily and completely rehydrate. The examples were prepared as discussed above.
______________________________________
Ingredient Percent
______________________________________
Beef 93.75
Water 3.00
Sodium chloride 0.75
Sodium tripolyphosphate
0.50
Gum arabic 2.00
100.00%
______________________________________
______________________________________
Pork 91.75
Water 6.00
Sodium chloride 0.75
Sodium tripolyphosphate
0.50
Microcrystalline cellulose
1.00
100.00%
______________________________________
______________________________________
Chicken 91.00
Water 4.00
Sodium chloride 0.75
Sodium tripolyphosphate
0.50
Malto Dextrin 3.75
100.00%
______________________________________
______________________________________
Turkey 95.55
Water 3.00
Sodium chloride 0.75
Sodium tripolyphosphate
0.50
Xanthan gum 0.20
100.00
______________________________________
The meat products of examples 1 to 4 rehydrated completely when placed in 180° water within 8 minutes while similarly prepared meat products which did not have the added water took 30 minutes to rehydrate and even then were frequently incompletely rehydrated.
Claims (3)
1. A method for producing freeze dried cooked meats which are more easily and completely rehydratable, comprising the steps of:
a. trimming a quantity of raw solid meat of heavy connective tissue and excess fat;
b. grinding or emulsifying a first portion of said trimmed meat and flaking or chunking a second portion of said trimmed meat into flakes or chunks which are 2.5-6.0 cubic inches in volume;
c. mixing said ground or emulsified first portion and said flaked or chunked second portion with about 2.0% to about 6.0% of the formula weight water, about 0.5% to about 2.0% of the formula weight salt, about 0.1% to about 0.5% of the formula weight phosphates and about 0.5% to about 5.0% of the formula weight an adjunctive hydrophilic ingredient until sufficient myofibrillar proteins are extracted to render the mixture moderately tacky and continuing said mixing until the water, salt, phosphates and adjunctive hydrophilic ingredients equilibrate throughout said mixture;
d. preparing a meat log by tightly stuffing said mixture into a moisture and gas impermeable container, wherein said container is a casing comprising a fibrous cellulose exterior laminated onto a saran film interior, said casing fitting tightly to the surface of said meat so as to keep moisture in equilibrium within said meat product during cooking;
e. cooking said meat log at a predetermined temperature for sufficient time to achieve a predetermined product center temperature;
f. freezing said meat log;
g. slicing or dicing said meat log into portions suitable for freeze dehydration;
h. freeze vacuum dehydrating said portions to a predetermined moisture level; and
i. packaging said dehydrated meat in an airtight container in the absence of oxygen.
2. The method as described in claim 1 wherein said salt is selected from the group consisting of sodium chloride and potassium chloride; said phosphate is selected from the group consisting of the salts of sodium pyrophosphate, orthophosphate, hexametaphosphate and tripolyphosphate and the adjunctive hydrophilic ingredients are selected from the group consisting of sodium carboxymethyl cellulose, microcrystalline cellulose, gum arabic, polyvinylpyrrolidone, arabino gallactan, xantham gum, kayara gum, guar gum, gum tragacanth, locust bean gum, malto dextrins and hydrocolloids.
3. A meat product prepared in accordance with the process of claim 1 wherein said meat product has an expanded matrix as a result of the mixing of the meat with water, salt, phosphates and adjunctive hydrophilic ingredients and said meat product rehydrates completely within 8 minutes upon being placed in 180° F. water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US06/665,899 USH35H (en) | 1984-10-29 | 1984-10-29 | Freeze dried cooked meats |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US06/665,899 USH35H (en) | 1984-10-29 | 1984-10-29 | Freeze dried cooked meats |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| USH35H true USH35H (en) | 1986-03-04 |
Family
ID=24672013
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US06/665,899 Abandoned USH35H (en) | 1984-10-29 | 1984-10-29 | Freeze dried cooked meats |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | USH35H (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5087473A (en) * | 1989-10-06 | 1992-02-11 | Franca Leo | Food product for domestic animals and a method for its manufacture |
| US6206348B1 (en) * | 1998-11-18 | 2001-03-27 | Donaldson Company, Inc. | Evaporative cooler for a gas turbine engine |
| US6383549B1 (en) * | 2000-02-23 | 2002-05-07 | Antonio Agostinelli | Dried food product and a process for producing the product |
| US20060222752A1 (en) * | 2005-04-05 | 2006-10-05 | Furtaw Louis F | Crisp meat-based food snacks |
| US7229830B1 (en) * | 1999-11-23 | 2007-06-12 | Lars-Ove Sjaunja | Standard sample composition and manufacture thereof |
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