IPC classes for russian patent Method for producing of food protein from chick-pea grain. RU patent 2246226. (RU 2246226):
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Method for producing of food protein from chick-pea grain / 2246226
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Method for producing of modified soya protein / 2248725
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High molecular soya protein / 2259780
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Method for production of protein product / 2264737
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Method for obtaining of protein chick-pea based product / 2265374
Method involves providing soaking and thermal processing of chick-pea beans, with soaking process being carried out for 2-2.5 hours at room temperature and thermal processing being performed in vacuum tanks at vacuum extent of 85-95% at temperature of 90-95 C for 40-45 min; removing excessive moisture, followed by drying in drying chambers at temperature of 35-50 C for 1.5-2 hours until moisture content is 12%; mixing chick-pea beans with spices and components. Drying process may be performed with the use of infrared radiation.
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Dry soy product with porous structure and method of obtaining such product / 2272508
Soy-beans are cleaned from admixtures, washed in clean water and soaked in water taken in double or triple amount by volume. Swollen beans are ground in 8-10-fold amount of water for obtaining fine suspension. Extract is filtered. Solid phase is separated and soy base is thus obtained. It is boiled for 35-45 min at temperature of 98-100°C. Coagulant is introduced into boiling solution for forming protein coagulum and clear whey. Used as coagulant is calcium chloride solution, calcium or magnesium sulfates and sea salt concentrate. Excessive whey is drained. Protein coagulum is placed in mold, cooled and whey is drained. At moisture content of up to 70%, it is molded in plates or bricks, 1.5-2 cm thick and frozen at temperature not higher than minus 10°C. Then they are thawed out and dried at temperature of 35-45°C to moisture content of 5-6%. Proposed method makes it possible to obtain product with porous structure without "bean taste".
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Leguminous paste / 2243681
Paste contains leguminous, nuts, garlic, oil, water, and spices, with said components being used in predetermined ratio. Resultant paste of plastic forming consistency has spicy soft taste not characteristic of dishes produced from leguminous. Above combination of components and quantitative ratio provide for required balance between food caloricity and contents of indispensable amino acids.
|
Method for producing of protein composition / 2243682
Method involves soaking chick-pea beans; grinding swollen beans in hot water; heating suspension to temperature of 85-920C; holding and cooling resultant suspension to 630C; acidifying to pH value of 4.8 and introducing malt solution in two stages: at first stage in an amount of 6.1-6.5% by weight of starch in mass and holding at said temperature for 2.0-2.2 hours, and at second stage increasing temperature of diluted mass to temperature of 650C; neutralizing pH value to 5.6 and introducing malt solution in an amount of 18-20% by weight of mass. Malt solution is prepared by mixing with water of ground preliminarily germinated chick-pea beans.
|
Method for producing of canned food "green peas" / 2244431
Method involves soaking and mixing dried pea grains at temperature of 35±50C in vessels primarily filled with water to predetermined level; two hours later, adding aqueous 5-6%-salt and sugar solution, and half an hour later aqueous 10-16%-solution of salt of polyvalent metal; during subsequent seven hours, continuing soaking and mixing procedures at temperature of 45±50C and further at temperature of 35±50C to provide for increase in weight of pea grain by at least 103% as compared to initial weight; changing water; blanching in boiling water; rinsing with running potable water having temperature of 14±30C for at least 20 min; charging cans with pea grains and media liquid used in the ratio of 55:45, said media liquid having temperature of at least 850C and having been prepared from potable water including sugar and edible salt; cooling to temperature of 400C with following reduction of pressure to value of atmospheric pressure; holding at temperature of 20±50C for 7-10 days.
|
Method for obtaining food selenium-containing composition out of chick-pea / 2244446
The present innovation deals with treating legumes to manufacture food products. The method deals with separating and inspecting chick-pea grain of legumes. Then chick-pea grain should be treated with an anolyte at pH being 7.0-8.0, wetted in 1%-sodium selenite solution prepared upon catholyte at pH being 7.0-8.0. Then product should be blanched and sterilized at 90 C for 30 min.
|
Method for moisture-thermal processing of soya / 2246225
Method involves preliminarily soaking soya beans; heating and processing under excessive pressure, with following cooling. Soya beans are soaked to moisture content of 20-25%. Processing under excessive pressure is provided by autoclaving process during 10-20 min at steam temperature of 105-1200C and pressure of 0.01-0.015 MPa. Method further involves discharging and cooling product to room temperature; exposing product to superhigh frequency current of 420-440 MHz at power of 2-3 kW for 2-4 min.
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FIELD: food-processing industry, may be used in food concentrates industry, confectionery industry and canned food industry.
SUBSTANCE: method involves extracting protein from chick-pea grain by means of catholyte with pH value of 10.0-11.0 and oxidation-reduction potential of 300-500 mV at liquor ratio of 1:(7-8) and temperature of 40-500C for 25-30 min; settling protein from extract at pH value of liquid medium of 4.6-4.8 by adding anolyte with pH value of 1.5-2.0 and potential of 1,100-1,250 mV or subjecting extract to unipolar processing in anode chamber of diaphragm-type electrolyzer to pH value of 4.6-4.8 and potential of 700-800 mV, said extract being washed with catholyte having pH value of 9.0-10.0 and potential of 100-300 mV. Method allows usage of alkaline and acids in the process of producing of protein to be avoided.
EFFECT: improved quality and increased yield of food protein.
4 tbl
The invention relates to the food industry and can be used in food concentrates, confectionery and canning industries.
A method of obtaining dietary protein from seeds of chickpea in which the protein of the milled grain is extracted with an aqueous solution of alkali when heated, then centrifuged and dry residue precipitated protein solution of hydrochloric acid, after which the serum is decanted, and the resulting protein was washed with water, centrifuged and dried by spray - prototype [1, SU 1796125 A, 1993].
The disadvantages of this method on the prototype are relatively low yield of protein (about 80% of its content in grain chickpea), its low digestibility (49-59%) and protein content (74-82%), high enough temperature extraction (up to 60°C)and is also used in the process of obtaining protein alkali and acid is expensive and dangerous to use reagents.
The technical result of the invention is to increase the protein yield and its quality, reducing process parameters and excluding alkali and acid from the process of obtaining protein.
This is achieved by extraction of the protein is carried Catolica with a pH of 10.0-11.0 and oxidation-reduction potential (ORP) - 300--500 mV at a water ratio of 1:(7-8) and a temperature of 40-50°C for 25-30 min, the precipitated protein from the extract at pH of liquid medium 4,6-4,8 added anolyte with a pH of 1.5-2.0 and potential 1100-1250 mV or subjected extract unipolar processing in the anode chamber of a diaphragm electrolyzer to a pH of 4.6-4.8 and potential 700-800 mV, and it rinses are Catolica with a pH of 9.0 to 10.0, and potencialom -100 - -300 mV.
The process of obtaining protein from the chickpeas in the following manner. Grain chickpea, purified from membranes, grind to flour. Using a diaphragm electrolytic cell, such as line type STEL, prepare catholyte - cathode fraction of electrochemically activated water is a necessary quality and heated to the desired temperature. Then the desired number of gram raw materials (flour) pour in the heated catholyte and with constant stirring of the suspension is extracted protein within a specified time. The resulting protein extract was separated from solid residue by centrifugation, the extract precipitated protein at pH of 4.6 to 4.8. Deposition of protein produced either by adding to the extract analyte - anode fraction of electrochemically activated water with maximum quality parameters (pH and ORP), or subjected to extract unipolar processing in the anode chamber of a diaphragm electrolyzer to the potential corresponding to the pH for precipitation of the protein, followed by exposure. Then the whey is drained, and the resulting protein was washed with alkaline by Catolica and with the corresponding redox potential. Finally the processed protein is freed from residual water by centrifugation and dried.
Examples of making a protein based on the proposed technology, the characteristics of ready protein, output and parameters of the extraction process are shown in tables 1-4. As can be seen from table 1, the precipitation of the protein from the extract mixed with the anolyte (option a) and the processing in the electrolytic cell (B) at pH 10-11, when the extraction is almost equivalent. In General, the proposed method of obtaining protein from the chickpeas in the application of Catolica and anolyte substantially better than the prototype, which uses alkali and acid, protein yield, and the content of protein.
Based on the data of table 2 to 4, in which the data receiving protein during the deposition of the extract according to option a, we can conclude that the optimal parametrai extraction of protein chickpea environment Catolica with a pH of 10-11 and AFP - -300 - -500 mV are: water ratio 1:(7-8), temperature 40-50°and extraction time 25-30 minutes to Increase paramente process of the above (optimal) is impractical because it does not increase the yield of protein and does not improve its quality, and decrease affects the results.
Parameter anolyte by mixing it with the extract (pH) is selected from the condition of minimizing its consumption when bringing the pH to 4.6 and 4.8 - magnitude necessary to precipitate the protein. The potential of the anolyte and extract both versions deposition of the protein corresponds to the values of pH upon receipt of the anolyte and the processing of the extract in the cell. The flushing of sediment (protein) weakly alkaline Catolica conducted with the aim of neutralizing him after deposition of protein in an acidic environment.
Obtained by this technology protein has good physical, chemical and organoleptic properties, it is cheaper than the prototype, environmentally safe, and can be applied in the food industry as an additive to increase the nutritional value of food products.
Table 1 Indicators of the Prototype of the Proposed method Options for the deposition of protein And B pH during extraction, a unit - 10 11 11 protein Yield, % 22,1 24,6 24,8 24,9 Protein, % 82,2 Of 83.4 83,5 83,2 Digestibility, % 58,6 59,2 59,1 59,2 trypsin Inhibitor, mg/kg 1,7 1,5 1,5 1,6 table 2 Indicators of the Values at the temperature of extraction 50°and time 30 min water ratio, ratio 1:7 1:8 1:10 protein Yield, % 24,6 24,8 23,7 Protein, % 83,3 83,5 82,8 Digestibility, % 59,0 59,1 of 58.9 Table 3 Indicators of Values at a water ratio of 1:8 and time 30 min. Temperature °40 50 60 Yield protein % 24,8 24,8 24,6 Protein, % Of 83.4 83,5 82,7 Digestibility, % 59,1 59,1 58,8 table 4 Indicators Values at a water ratio of 1:8 and the temperature of extraction 50°With Time, min 20 25 30 40 protein Yield, % 21,2 24,5 24,8 24,8 Protein, % 75,1 83,3 83,5 Of 83.4 Digestibility, % 51,4 58,8 59,1 59,0
The method of obtaining dietary protein from seeds of chickpea, including extraction of protein in an alkaline medium, centrifugation, sedimentation of protein in an acidic environment, and its separation with subsequent washing, additional centrifugation and drying, characterized in that the protein extraction is carried Catolica with a pH of 10.0-11.0 and ORP -300 ÷ -500 mV at a water ratio of 1:(7-8) and a temperature of 40-50°C for 25-30 min, the precipitated protein from the extract at pH of liquid medium 4,6-4,8 adding anolyte with a pH of 1.5-2.0 with potential 1100-1250 mV or subjected extract unipolar processing in the anode chamber diaphragm electrolyzer to a pH of 4.6-4.8 and potential 700-800 mV, and it rinses are Catolica with a pH of 9.0 to 10.0, and the potential of -100 ÷ -300 mV.
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