• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    production of soluble protein solutions from pulses. pulse protein product that can be an isolate and that produces thermally stable solutions at low pH values, being useful for sizing soft drinks and sports drinks without protein precipitation. the pulse protein product is obtained by extracting a pulse protein source material with an aqueous solution of calcium salt to form an aqueous solution of calcium salt to form an aqueous solution of pulse protein, separating the aqueous solution pulse protein from the residual protein pulse source, adjusting the pH of the aqueous protein pulse solution to a pH of about 1.5 to about 4.4 to produce an acidified protein pulse solution that can be dried , followed by optional concentration and diafiltration, in order to provide the pulse protein product.
    公开号:BR112012028444B1
    申请号:R112012028444-4
    申请日:2011-05-09
    公开日:2020-03-24
    发明作者:Kevin I. Segall；Martin Schweizer
    申请人:Burcon Nutrascience；Corp.；
    IPC主号:
    专利说明:

    METHOD OF MANUFACTURING A PULSE PROTEIN PRODUCT AND
    PROTEIN PULSE PRODUCT
    REFERENCE TO THE CORRELATE ORDER
    This application claims priority under 35 USC 119 (e) of US Provisional Patent Application number
    61 / 344,013 filed on May 7, 2010.
    FIELD OF THE INVENTION
    The present invention relates to the production of protein solutions from pulses and the new pulse protein products.
    BACKGROUND OF THE INVENTION
    US Patent Applications numbers 12 / 603,087 filed on October 21, 2009 (US Patent Publication number 2010-0098818) and 12 / 923,897 filed on October 13, 2010 (US Patent Publication number 20110038993), assigned to this assignee and whose disclosures are hereby incorporated by reference describe obtaining soy protein products with a protein content of at least about 60% by weight (N x 6.25) db, preferably at least about 90% by weight , which produce clear, heat-stable solutions with a low pH value and which can be used to enrich soft drinks with proteins, as well as other aqueous systems, without protein precipitation.
    The soy protein product is produced by extracting a soy protein source with an aqueous solution of calcium chloride to cause the soy protein to solubilize from the protein source and to form an aqueous protein solution from the soybean, separation of the aqueous soy protein solution from the
    Petition 870190080595, of 08/19/2019, p. 29/36
    2/52 residual soy protein source, optionally diluting the soy protein solution, adjusting the pH of the aqueous soy protein solution to a pH of about 1.5 to about 4.4, preferably about 2 at about 4, so as to produce a clear acidified soy protein solution, optionally concentrating the clear aqueous protein solution, while maintaining the lomca intensity substantially constant by using a selective membrane technique, optionally occurring the diafiltration of the solution of concentrated soy protein and drying the concentrated soy protein solution and, optionally diafiltered.
    SUMMARY OF THE INVENTION
    It has been found that this procedure and its modifications can be used to form the soluble acid protein products from pulses, including lentils, chickpeas, dried peas and dried beans.
    Accordingly, in one aspect of the present invention, there is provided a method of producing a protein pulse product with a protein pulse content of at least about 60% by weight, preferably at least about 90% by weight, ( N x 6.25) on a dry weight basis, which comprises.
    (a) extracting a pulse source of protein with an aqueous solution of calcium salt, preferably an aqueous solution of calcium chloride, to cause the pulse of protein to be solubilized from the protein source and form an aqueous solution protein pulse,
    3/52 (b) separating the aqueous protein pulse solution from the pulse source of residual protein, (c) optionally, diluting the aqueous protein pulse solution, (d) adjusting the pH of the aqueous pulse protein solution protein to a pH of about 1.5 to about 4.4, preferably about 2 to about 4, to produce an acidified protein pulse solution, (e) optional clarification of the acidified protein pulse solution, if it is not already clear, (f) alternatively, from steps (b) to (e), optionally, dilution and, subsequently, adjusting the pH of the aqueous combined protein pulse solution and residual protein pulse source for a pH of about 1.5 to about 4.4, preferably about 2 to about 4, then separating the pulse solution of acidified protein, preferably clear from the pulse source of residual protein, (g) optionally, concentrating the aqueous protein pulse solution, while maintaining the ionic intensity substantially constant through a selective membrane technique, (h) optionally, diafiltrating the concentrated protein pulse solution, and (i) optionally, drying the concentrated protein solution and optionally diafiltered protein pulse solution.
    The pulse protein product is preferably an isolate having a protein content of at least
    4/52 about 90% by weight, preferably at least about 100% by weight, (N x 6.25) d.b.
    The present invention further provides a new protein pulse product with a protein content of at least about 60% by weight, preferably at least about 90% by weight, more preferably at least about 100% by weight (N * 6.25) db, and which is soluble in water and forms thermally stable solutions at acid pH values of less than about 4.4, and is useful for protein enrichment in aqueous systems, including soft drinks and sports drinks, without cause the protein to precipitate.
    In another aspect of the present invention, an aqueous solution of the protein pulse product provided herein is provided which is thermally stable at a pH below about 4.4. The aqueous solution can be a drink, which can be a clear drink in which the pulse protein product is completely soluble and transparent, or the aqueous solution can be an opaque drink in which the pulse protein product contributes or not to opacity. .
    Pulse protein products produced according to the process of this document are suitable not only for protein enrichment of acidic media, but can be used in a wide variety of conventional protein product applications, including, but not limited to protein enrichment of processed foods and drinks, oil emulsification, as a body builder in baked goods and foaming agent in products that trap gas. Besides that,
    5/52 protein pulse isolates can be formed in protein fibers, useful in meat analogues and can be used as a substitute or extender in food products where egg white is used as a binder. Pulse protein products can also be used in nutritional supplements. Other uses of pulse protein products are in pet food, pet food and in industrial and cosmetic applications and in personal care products.
    GENERAL DESCRIPTION OF THE INVENTION
    The initial step in the process of providing protein pulse products involves solubilizing the protein pulse from a protein pulse source. The pulses to which the invention can be applied include lentils, chickpeas, dried peas and dry features. The pulse source of protein can be pulses or any pulse product or by-product derived from pulse processing, such as flour pulse. The protein pulse product recovered from the pulse protein source may be the naturally occurring protein in pulses, or the protein material may be a protein modified by genetic manipulation, but having the hydrophobic and polar properties characteristic of the natural protein.
    Protein solubilization from the pulse protein source material is most conveniently performed using a calcium chloride solution, although solutions of other calcium salts can be used. In addition, other alkaline earth metal compounds can be used, such as magnesium salts. In addition, the extraction of the protein from the pulse source of
    6/52 protein can be made using a calcium salt solution, in combination with another salt solution, such as sodium chloride. In addition, the extraction of the protein from the protein pulse source can be done using water or another brine solution, such as sodium chloride, with the calcium salt being subsequently added to the aqueous protein pulse solution produced in the step extraction. The precipitate formed after adding the calcium salt is removed before further processing.
    As the concentration of the calcium salt solution increases, the degree of protein solubilization from the protein pulse source initially increases until a maximum value is reached. Any subsequent increase in salt concentration does not increase the total solubilized protein. The concentration of the calcium salt solution that causes maximum protein solubilization varies depending on the salt in question. It is generally preferred to use a concentration value of less than about 1.0 M and more preferably a value of about 0.10 to about 0.15 M.
    In a batch process, the protein salt solubilization is carried out at a temperature between about 1 ° C to about 65 ° C, preferably about 15 ° C to about 65 ° C, more preferably about 20 ° At about 35 ° C, preferably accompanied by stirring to decrease the solubilization time, which is generally about 1 to about 60 minutes. It is preferred to perform solubilization to extract substantially as much protein from the pulse protein source as is
    7/52 workable, in order to provide a high overall product yield.
    In a continuous process, the extraction of the protein from the pulse protein source is performed in any consistent manner to effect a continuous extraction of protein from the pulse protein source. In one embodiment, the pulse source of protein is continuously mixed with the calcium salt solution and the mixture is conducted through a tube or duct with a length and flow rate for a sufficient residence time to effect the extraction according to the parameters described in this document. In such a continuous process, the salt solubilization step is carried out quickly, in a time of up to about 10 minutes, preferably to effect the solubilization to extract substantially as much protein from the pulse protein source as is practicable. The solubilization of the continuous process is carried out at temperatures between about 1 ° C and about 65 ° C, preferably about 15 ° C to about 65 ° C, more preferably about 20 ° C to about 35 ° C.
    The extraction is generally carried out at a pH of about 4.5 to about 11, preferably about 5 to about 7. The pH of the extraction system (pulse source of protein and a solution of calcium salt) can be adjusted to any desired value within the range of about 4.5 to about 11, for use in the extraction step by using any suitable food grade acid, usually hydrochloric acid or acid
    8/52 phosphoric, or food grade alkali, usually sodium hydroxide, as required.
    The concentration of the protein pulse source in the calcium salt solution during the solubilization step can vary widely. Typical concentration values are about 5 to about 15% weight / volume.
    The protein solution resulting from the extraction step generally has a protein concentration of about 5 to about 50 g / L, preferably about 10 to about 50 g / L.
    The aqueous solution of calcium salt may contain an antioxidant. The antioxidant can be any suitable antioxidant, such as sodium sulfite or ascorbic acid. The amount of antioxidant employed can vary from about 0.01 to about 1% by weight of the solution, preferably about 0.05% by weight. The antioxidant serves to inhibit the oxidation of phenolic compounds in any protein solution.
    The aqueous phase resulting from the extraction step can then be separated from the pulse source of residual protein, in any convenient way, such as by the use of a centrifugal decanter, followed by disk centrifugation and / or filtration, to remove material from the source. pulse of residual protein. The separation step is generally carried out at the same temperature as the protein solubilization step, but can be carried out at any temperature within the range of about 1 C to about 65 C, preferably about 15 ° C to about 65 C , more preferably about 20 ° C to about 35 C. Alternatively, the optional dilution steps and
    The acidification described below can be applied to a mixture of aqueous protein pulse solution and a residual protein pulse source, with subsequent removal of material from the residual protein pulse source by the separation step 5 described above. The separate residual protein pulse source can be dried for disposal.
    Alternatively, the separate residual protein pulse source can be processed to recover some of the residual protein, such as a conventional isoelectric precipitation procedure to recover such residual protein.
    The aqueous protein pulse solution can be treated with an adsorbent, such as powdered activated carbon or granulated activated carbon, to remove color and / or odor compounds. Such adsorbent treatment can be carried out under any convenient conditions, generally at room temperature, of the separated aqueous protein solution. For powdered activated carbon an amount of about 0.025% to about 5% weight / volume is used, preferably about 20 0.05% to about 2% weight / volume. The adsorbent agent can be removed from the protein pulse solution by any convenient means, such as by filtration.
    The resulting aqueous protein pulse solution can be diluted with water, usually about 0.5 to 25 about 10 volumes, preferably about 0.5 to about 2 volumes, in order to decrease the conductivity of the aqueous solution of protein pulses to a value generally below about 90 mS, preferably about 4 to about 18 mS. Such dilution is usually carried out using water, 30 despite diluted salt solutions, such as chloride
    10/52 sodium or calcium chloride, having a conductivity of up to about 3 mS, can be used.
    The water with which the pulse protein solution is mixed generally has the same temperature as the pulse protein solution, but the water can have a temperature of about 1 ° C to about 65 ° C, preferably about 15 ° C. ° C to about 65 ° C, more preferably about 20 ° C to about 35 ° C.
    The diluted protein pulse solution is then adjusted in pH to about 1.5 to about 4.4, preferably about 2 to about 4, by the addition of any suitable food-grade acid, such as hydrochloric acid or phosphoric acid, to result in an acidic, aqueous solution of protein pulse, preferably an acidic, clear, aqueous solution of protein pulse.
    The diluted and acidified protein pulse solution has a conductivity generally below about 95 mS, preferably about 4 to about 23 mS.
    As mentioned above, as an alternative for the initial separation of the residual protein pulse source, the aqueous protein pulse solution and the residual protein pulse source material can be optionally diluted and acidified together and then aqueous, acidified pulse protein solution is clarified and separated from the residual pulse protein source material by any convenient technique, as discussed above.
    The aqueous, acidified pulse protein solution can be heat treated to inactivate
    11/52 thermally labile antinutritional factors, such as trypsin inhibitors, present in such a solution, as a result of the extraction from the pulse protein source material during the extraction step. Such a heating step also provides the added benefit of reducing the microbial load. Generally, the protein solution is heated to a temperature of about 70 ° C to about 160 ° C, preferably about 80 ° C to about 120 C, more preferably from about 85 ° C to about 95 ° C for about 10 seconds to about 60 minutes, preferably about 10 seconds to about 5 minutes, more preferably about 30 seconds to about 5 minutes. The heat treated protein pulse solution can then be cooled by further processing, as described below, to a temperature of about 2 ° C to about 65 ° C, preferably about 20 ° C to about 35 ° C.
    If the optionally heat-treated, acidified, optionally diluted protein pulse solution is not transparent, it can be clarified by any conventional procedure, such as filtration or centrifugation.
    The resulting aqueous, acidified protein pulse solution can be directly dried to produce a pulse protein product. In order to provide a protein pulse product that has a reduced impurity content and a reduced salt content, such as a protein pulse isolate, the acidified aqueous protein pulse solution can be processed as described below prior to drying.
    12/52
    The aqueous, acidified pulse protein solution can be concentrated to increase the protein concentration of the protein, while keeping the lonic intensity of the substance substantially constant. Such concentration is generally carried out to provide a concentrated protein pulse solution having a protein concentration of about 50 to about 300 g / L, preferably about 100 to about 200 g / L.
    The concentration step can be carried out in any convenient and consistent manner with batch or continuous operation, such as by employing any convenient selective membrane technique, such as ultrafiltration or diafiltration, using membranes such as hollow fiber membranes or spiral membranes, with a suitable molecular weight cut, such as about 3,000 to about 1,000,000 Dalton, preferably from about 5,000 to about 100,000 Dalton, taking into account different membrane materials and configurations, and, for continuous operation, sized to allow the desired degree of concentration, as the aqueous protein solution passes through the membranes.
    As is well known, ultrafiltration and similar selective membrane techniques allow low molecular weight species to pass through, preventing higher molecular weight species from passing through. Low molecular weight species include not only ionic salt species, but also low molecular weight materials extracted from the source material, such as carbohydrates, pigments, low molecular weight proteins and antinutritional factors, such as,
    13/52 trypsin inhibitors, which are properly low molecular weight proteins. The cut of the molecular weight of the membrane is usually chosen to ensure the retention of a significant proportion of the protein in the solution, while allowing the passage of contaminants taking into account the different membrane materials and configurations.
    The solution in pulse of concentrated protein then can be submitted The one step diafiltration using Water or a solution in brine diluted. THE solution in
    diafiltration can be at its natural pH or at a pH equal to that of the protein solution to be diafiltered or at any pH value in that range. Such diafiltration can be performed using between about 2 to about 40 volumes of diafiltration solution, preferably about 5 to about 25 volumes of diafiltration solution. In the diafiltration operation, larger amounts of contaminants are removed from the aqueous protein pulse solution by passing through the membrane with the permeate. This purifies the aqueous protein solution and can also reduce its viscosity. The diafiltration operation can be carried out until no significant amount of contaminants and visible color are present in the permeate or until the retained material has been sufficiently purified so that, after drying, it provides a pulse protein isolate with a protein of at least about 90% by weight (N χ 6.25) db Such diafiltration can be performed using the same membrane as for the concentration step. However, if desired, the diafiltration step can be performed using a separate membrane, with a cut in weight
    14/52 molecular weight, such as a membrane with a molecular weight cut in the range of about 3,000 to about 1,000,000 Dalton, preferably about 5,000 to about 100,000 Dalton, taking into account different membrane materials and configurations.
    Alternatively, the diafiltration step can be applied to the acidified aqueous protein solution prior to concentration or to the partially concentrated aqueous protein solution. Diafiltration can also be applied at various points during the concentration process. When diafiltration is applied before concentration, or to the partially concentrated solution, the resulting diafiltered solution can then be completely concentrated. The viscosity reduction obtained by the various diafiltrations as the protein solution is concentrated can allow a high concentration of final protein to be obtained. This reduces the volume of material to be dried.
    The concentration step and the diafiltration step can be performed in this document, such that the subsequently recovered protein pulse product contains less than about 90% by weight of protein (N x 6.25) db, such as at least about 60% protein by weight (N x 6.25) db When partial concentration and / or partial diafiltration of the aqueous protein pulse solution, it is only possible to partially remove contaminants. This protein solution can then be dried to provide a protein pulse product with lower levels of purity. The protein pulse product is highly soluble and capable of producing protein solutions,
    15/52 preferably clear protein solutions, under acidic conditions.
    An antioxidant may be present in the diafiltration medium for at least part of the diafiltration step. The antioxidant can be any suitable antioxidant, such as sodium sulfite or ascorbic acid. The amount of antioxidant used in the diafiltration medium depends on the materials used and can vary from about 0.01 to about 1% by weight, preferably about 0.05% by weight. The antioxidant serves to inhibit the oxidation of any phenolic compounds present in the concentrated protein pulse isolate solution.
    The concentration step and the optional diafiltration step can be carried out at any convenient temperature, generally about 2 ° C to about 65 ° C, preferably about 20 ° C to about 35 ° C and for the period of time to obtain desired degree of concentration. The temperature and other conditions used to a certain degree depend on the membrane equipment used to carry out the membrane processing, the desired protein concentration of the solution and the removal efficiency of the contaminants for the permeate.
    As mentioned earlier, the pulses contain anti-nutritional trypsin inhibitors. The level of activity of the trypsin inhibitor for the final protein pulse product can be controlled by manipulating the different process variables.
    As mentioned above, heat treatment of the acidified aqueous protein pulse solution can be used to inactivate labile trypsin inhibitors in
    16/52 heat. The partially or fully concentrated acidified protein pulse solution can also be heat treated to inactivate heat-labile trypsin inhibitors. When heat treatment is applied to the pulse solution of partially acidified protein
    concentrated, the solution resulting can so be additionally concentrated. Beyond addition, the concentration and / or steps of
    diafiltration can be operated in a favorable way to remove trypsin inhibitors in the permeate, together with the other contaminants. The removal of trypsin inhibitors is promoted by the use of a larger pore size membrane, such as 30,000 to 1,000,000 Da, operating the membrane at elevated temperatures, such as at 30 ° C to 65 ° C and employing a larger volume diafiltration medium, such as 20 to 40 volumes.
    Acidification and membrane processing in the protein pulse solution at a lower pH, such as 1.5 to 3, may reduce the activity of the trypsin inhibitor compared to treating the solution at a higher pH, such as 3 to 4.4. When the protein solution is concentrated and diafiltered at the lower end of the pH range, it may be desirable to raise the pH of the retentate before drying. The pH of the concentrated and diafiltered protein solution can be increased to the desired value, for example, pH 3, by adding any suitable food grade alkali, such as sodium hydroxide.
    In addition, the reduction in trypsin inhibitor activity can be obtained by exposing pulses of
    17/52 materials to the reducing agents which interrupts or reorganizes the disulfide bonds of the inhibitors. Suitable reducing agents include sodium sulfite, cysteine and nacetylcysteine.
    The addition of such reducing agents can be carried out at various stages of the overall process. The reducing agent can be added with the protein pulse source material in the extraction step, it can be added to the clear protein pulse aqueous solution after removing the residual protein pulse source material, it can be added to the diafiltered retentate before drying or can be mixed dry with the dry protein pulse product. The addition of the reducing agent can be combined with the heat treatment step and the membrane processing steps, as described above.
    If it is desired to keep trypsin inhibitors active in the concentrated protein solution, this can be achieved by eliminating or reducing the intensity of the heat treatment step, not using reducing agents, operating the concentration and diafiltration steps at the highest end of the pH range, such as 3 to 4.4, using a diafiltration and concentration membrane with a smaller pore size, operating the membrane at lower temperatures and using less volumes of diafiltration medium.
    The concentrated and optionally diafiltered aqueous protein solution can be treated with an adsorbent, such as powdered activated carbon or granulated activated carbon, to remove color and / or odor compounds. Such adsorbent treatment can be carried out under
    18/52 any convenient conditions, usually at room temperature of the concentrated protein solution. For powdered activated carbon, an amount of about 0.025% to about 5% weight / volume is used, preferably about 0.05% to about 2% weight / volume. The adsorbent can be removed from the protein pulse solution by any convenient means, such as by filtration.
    The aqueous solution of concentrated and optionally diafiltered protein pulse can be dried by any convenient technique, such as spray drying or lyophilization. A pasteurization step can be carried out on the protein pulse solution before drying. Such pasteurization can be carried out under any desired pasteurization conditions. Generally, the concentrated and optionally diafiltered protein pulse solution is heated to a temperature of about 55 ° C to about 70 ° C, preferably about 60 ° C to about 65 ° C for about 30 seconds at about 60 minutes, preferably about 10 minutes to about 15 minutes. The concentrated and pasteurized protein pulse solution can then be
    cold for drying, preference to one temperature in about 25 ° C until about 40 ° C. 0 wrist product dry protein has a content in protein bigger that about 60% by weight. In preferably, The
    dry protein pulse product is an isolate with an excess protein content of about 90% protein by weight, preferably at least about 100% by weight, (N x 6.25) d. B . .
    The protein pulse product produced here is soluble in an acidic aqueous medium, which makes the product
    19/52 ideal for incorporation in carbonated and non-carbonated drinks, to provide the same high protein content. These drinks have a wide range of acidic pH values, ranging from about 2.5 to about 5. The pulse protein product provided herein can be added to such drinks in any convenient amount to provide enrichment of the content of protein to such drinks, for example, at least about 5 g of protein pulse per serving. The added protein pulse product dissolves in the drink and the opacity of the drink is not increased by thermal processing. The pulse protein product can be mixed with dry drinks before reconstituting the drink by dissolving in water.
    In some cases, The modification d in normal formulation of drinks so The tolerate the composition of this invention can be necessary if the components present at drink adversely affect the composition capacity gives present invention in stay dissolved in the drink.EXAMPLES Example 1 This example evaluates the extraction capacity in
    protein from lentils, chickpeas and dried peas and the effect of acidification on the clarity of protein solutions resulting from the extraction step.
    Dried lentils, chickpeas, broken yellow peas and broken green peas were purchased in integral form and molds using a Bamix cutter until they were in the form of a relatively fine powder. The degree of grinding was not controlled by time or particle size. Milled material (10 g) was extracted with 0.15 M
    20/52
    CaCl 2 (100 mL) for 30 minutes on a magnetic stirrer at room temperature. The extract was separated from the residual material by centrifugation at 10,200 g for 10 minutes and then clarified by filtration through a 0.45 pm pore size syringe filter. The ground starting material and the clear extract were tested for protein content using a Leco Nitrogen Determinator FP 528. The clarity of the extract at full intensity and diluted with 1 volume of purified water by reverse osmosis (RO) was determined by measurement absorbance at 600 nm (A600). Full and diluted solutions were then adjusted to pH 3 with HCl and A600 measured again. In this and other examples where the clarity of the solution was assessed by measuring A600, water was used to check the spectrophotometer.
    The protein content and apparent extraction capacities determined for each of the protein sources are shown in Table 1.
    Table 1 - Protein content and apparent extraction capacity of protein sources
    Protein source Protein content(%) Apparent extraction capacity (%) Lentil 24.20 47.5 chickpeas 18, 97 52.2 yellow peas 23.07 59.4 green peas 22.38 64.3
    As can be seen from the results of the
    Table 1, the extraction capacity of all protein sources was very good.
    21/52
    The clarity of samples of full intensity and of diluted extract before and after acidification is shown in Table 2.
    Table 2 - Effect of acidification on the clarity of the 5 samples of diluted and undiluted extract - extraction of calcium chloride
    Undiluted Diluted Sample pH Ά600 pH Ά600 pH A600 pH A600starts starts Final slim I started starts Final Final1 11 there 1 Lentil 5.22 0.093 3.04 0.25 5.30 1, 196 2.96 0.037 s 3 grain of 5.15 0.189 3.07 0.22 5.25 2,714 2.79 0.099 spout 8 peas 5.21 0.250 3.14 0.82 5.28 2,334 3, 11 0. 250 yellow 8 peas 5.23 0.288 3, 18 0.57 5.31 2,248 2.97 0.161 greens 7
    As can be seen from the results in Table 2, the full-intensity extract solutions of lentil, chickpeas and split peas were clear to slightly cloudy. Acidification, without dilution, increased the turbidity level of the samples. Dilution of the filtered extract with an equal volume of water resulted in remarkable precipitation and a corresponding increase in the A600 value. The acidification of the diluted solution largely solved the precipitate and resulted in a clear solution for lentils and chickpeas and a slightly cloudy solution for green and yellow peas.
    Example 2
    22/52
    This example contains an assessment of the clarity of acidified broken green pea extracts, diluted or undiluted with water and sodium chloride in place of the calcium chloride solution of Example 1 as the extraction solution. Green dry peas were purchased in whole form and molds into a fine powder using a KitchenAid mixer grinder accessory. The degree of grinding was not controlled by time or particle size. Milled material (10 g) was extracted with 0.15 M NaCl (100 ml) or RO water (100 ml) for 30 minutes on a magnetic stirrer at room temperature. The extract was separated from the residual material by centrifugation at 10,200 g for 10 minutes and then clarified by filtration through a 0.45 pm pore size syringe filter. The clarity of the extract at full intensity and diluted with 1 volume of water purified by (RO) was determined by measuring the absorbance at 600 nm (A600). Full and diluted solutions were then adjusted to pH 3 with HCl and A600 measured again.
    The clarity of samples of full intensity and of diluted extract before and after acidification is shown in Table 3.
    Table 3 - Effect of acidification on the clarity of samples of diluted and undiluted extract extractions in water and sodium chloride
    Undiluted DilutedSolution pH A600 pH A600 pH A600 pH A600 the of I started I started slim slim I started I started slim slim extraction al al 1 1 al al 1 1 to
    23/52
    Water 6.56 0.113 3, 14 > 3.0 6, 62 0.050 3.00 2.647 0.15MNaCl 6.19 0.021 2.96 > 3.0 6.28 0.870 2.87 2.851
    As can be seen from the results in Table 3, the extracts prepared with water or with a sodium chloride solution showed a lot of turbidity when acidified regardless of the use of a dilution step.
    Example 3
    This example assesses the extraction capacity of various types of dry grains and the effect of acidification on the clarity of the protein solutions resulting from the extraction step.
    Brindle beans, small white beans, small red beans, Roman beans, large northern beans and fava beans were purchased in whole form, dried and ground using a Bamix cutter until a relatively fine powder form was obtained. The degree of grinding was not controlled by time or particle size. Black bean flour was also purchased. Milled material or flour (10 g) was extracted with 0.15 M CaCla (100 mL) for 30 minutes on a magnetic stirrer at room temperature. The extract was separated from the residual material by centrifugation at 10,200 g for 10 minutes and then clarified by filtration through a 0.45 pm pore size syringe filter. The molded starting material or flour and the clear extract were tested for protein content using a Leco Nitroqene Determinator FP 528. The clarity of the extract at full intensity and diluted with 1 volume of water purified by (RO) was
    24/52 determined by measuring the absorbance at 600 nm (A600). Full and diluted solutions were then adjusted to pH 3 with HCl and A600 measured again.
    protein content and apparent extraction capacities determined for each type of dry beans presented in Table 4.
    Table 4 - Protein content and apparent extraction capacity of the various types of dry beans
    Type of beans Protein content(%) Apparent extraction capacity (%) black bean 24.00 7 7.9 brindle beans 21.45 _________ 66.2 _________ White beansmall 24.41 63.5 Red beansmall 20.18 76.8 roman bean 18.07 86, 9 big beannorth 21.77 85, 9 bean 21.43 71, 9
    As can be seen from the results in Table 4, the protein in all types of beans was readily extracted. The clarity of samples of full intensity and diluted extract before and after acidification is shown in Table 5.
    Table 5 - Effect of acidification on the clarity of diluted and undiluted extract samples - calcium chloride extraction
    Undiluted Diluted 1 + 1
    25/52
    Sample pHinitial Initial A600 pHslim1 Ά600Final pHI startedal Ά600 start pHslim1 A600Final beanblack 4.69 0.100 2.99 0.154 4.76 0.025 3.15 0.031 brittle beans 5.08 0.014 3.02 0.072 5.34 0.003 3.00 0.017 small white beans 5.08 0.026 3.03 0.092 5.23 0.022 3.03 0.019 red beans ho small 5.06 0.028 3.07 0.093 5.33 0.014 2.97 0.021 beanRoman 4.96 n. d. 3.07 0.023 5.21 0.005 2.86 0.008 northern big beans 4.93 0.026 3.10 0.045 5.16 0.008 3.11 0.013 bean 5.13 n. d. 3.07 0.089 5.37 0.020 3.04 0.013
    na = not determined
    As can be seen from the results in Table 5, the full intensity extract solutions of all beans were very clear. Acidification, without dilution, slightly increased the level of turbidity in the samples, but they remained very clear. Dilution of the filtered extract with an equal volume of water did not result
    26/52 in the formation of any precipitate. This contrasts with the precipitation observed at the time of dilution for the pulses tested in Example 1. The diluted solutions of beans proteins remained clear when acidified.
    Example 4
    This example contains an assessment of the clarity of acidified small white bean extracts, diluted or undiluted with water and sodium chloride in place of the calcium chloride solution of Example 3, as the extraction solution.
    Small, dry white beans were purchased whole and ground into a fine powder using a Bamix cutter. The degree of grinding was not controlled by time or particle size. Ground material (10 g) was extracted with 0.15 M CaCl (100 ml) or RO water (10 ml) for 30 minutes on a magnetic stirrer at room temperature. The extract was separated from the residual material by centrifugation at 10,200 g for 10 minutes and then clarified by filtration through a 0.45 pm pore size syringe filter. The protein content of the filtrates was determined using a Leco Nitrogen Determinator FP 528. The clarity of the extract at full intensity and diluted with 1 volume of water purified by (RO) was determined by measuring the absorbance at 600 nm (A600). Full and diluted solutions were then adjusted to pH 3 with HCl and A600 measured again.
    Extraction with water and sodium chloride solution provided apparent extraction capacities of 45.9% and 61.5%, respectively. The clarity of the extract samples
    27/52 diluted and with full intensity before and after acidification are shown in Table 6.
    Table 6 - Effect of acidification on the clarity of diluted and undiluted extract samples - extractions of water and sodium chloride
    Undiluted Diluted 1 + 1 Solutionthe ofextractionto Initial PH Initial A600 starting pHal Initial A600 pHI startedal Initial A600 Initial PH A6 0 0 start Water 6.48 0.079 2.95 > 3.0 6.51 0.051 3.03 2,771 0.15MNaCl 6.13 0.116 3.01 > 3.0 6.22 0.212 3.02 > 3.0
    As can be seen from the results in Table 6, the extracts prepared with water or a sodium chloride solution were very cloudy after acidification regardless of whether a dilution step had been employed.
    Example 5
    This example illustrates the production of green pea protein isolate on a bench scale.
    180 g of broken green dried peas were finely ground using a KitchenAid mixer grinder attachment. 150 g of finely molded split pea flour was combined with 1,000 ml of 0.15 M CaCl 2 solution at room temperature and stirred for 30 minutes to provide an aqueous protein solution. Residual solids were removed and the resulting protein solution was clarified by centrifugation and filtration, to obtain a filtered protein solution having a
    28/52 protein content of 1.83% by weight. 655 ml of the filtered protein solution was added to 655 ml of RO water and the pH of the sample dropped to 3.03 with HCl solution.
    The diluted and acidified protein extract solution was reduced in volume from 1250 mL to 99 mL by concentration on a PES membrane that has a molecular weight cut of 10,000 Dalton. A 96 ml aliquot of the concentrated protein solution was then diafiltered on the same membrane with 480 ml of RO water. The resulting concentrated, acidified and diafiltered protein solution had a protein content of 7.97% by weight, and represented a yield of 65.5% by weight of the initial filtered protein solution which was subsequently processed. The concentrated, acidified, diafiltered protein solution was dried to yield a product that could have a protein content of 95.69% (N x 6.25) d.b. The product was called GP701-01 protein isolate.
    8.30 g of GP701-01 were produced. A solution of GP701-01 was prepared by dissolving enough protein powder to provide 0.48 g of protein in 15 mL of RO water and the pH was measured with a pH meter and the color and clarity assessed using a HunterLab Color instrument Quest XE operated in transmission mode. The results are shown in Table 7 below.
    Table 7 - HunterLab pH and classifications for GP701-01 solution
    Sample pH L * The* B* Turbidity GP701-01 3.17 89.46 1.10 14, 98 63.3
    29/52
    As can be seen from the results in Table Ί, the GP701-01 solution was clear and had a light color.
    The GP701-01 solution was heated to 95 ° C, maintained at that temperature for 30 sequels and then immediately cooled to room temperature in an ice bath. The clarity was measured again with the HunterLab instrument and the results are shown in Table 8.
    Table 8 - HunterLab classifications for GP701-01 solution after heat treatment
    Sample L * The* B* Turbidity GP701-01 95.56 -0.06 9, 65 47.0
    As can be seen from the results of Table 8, it was found that the heat treatment improved the clarity and reduced the level of turbidity of the solution, while making it greener and less yellow. Although the level of turbidity in the solution was reduced, the protein solution was still translucent rather than transparent.
    Example 6
    This example illustrates the production of green pea protein isolate on a bench scale, but with the filtration step it changed after dilution and acidification of the extract.
    180 q of broken green dried peas were finely ground using a grinder attachment from the KitchenAid mixer. 150 g of finely ground split pea flour was combined with 1,000 ml of 0.15 M CaCl 2 solution at room temperature and stirred for 30 minutes to provide an aqueous protein solution. Residual solids were removed by centrifugation to
    30/52 produce a concentrate having a protein content of 2.49% by weight. 800 ml of the concentrate was added to 800 ml of water and the pH of the sample dropped to 3.00 with diluted HCl. The diluted and acidified concentrate was further clarified by centrifugation and filtration, to obtain a clear protein solution having a protein content of 1.26% by weight. By filtration of the solution after dilution and acidification, A600 of the solution before processing the membrane in this experiment was 0.012, compared to 0.093 for the diluted and acidified filtrate in Example 5.
    The filtered protein solution was reduced in volume from 1,292 mL to 157 mL by concentration on a PES membrane that has a 10,000 Dalton molecular weight cut. A 120 ml aliquot of the concentrated protein solution was then diafiltered on the same membrane with 600 ml of RO water. The resulting concentrated, acidified and diafiltered protein solution had a protein content of 7.70% by weight, and represented a yield of 42.5% by weight of the initial concentrate which was further processed. The concentrated, acidified and diafiltered protein solution was dried to yield a product that could have a protein content of 94.23% (N x 6.25) d.b. The product was called GP701-01 protein isolate.
    8.55 g of GP701-02 were produced. A solution of GP701-02 was prepared by dissolving enough protein powder to provide 0.48 g of protein in 15 mL of RO water and the pH was measured with a pH meter and the color and clarity assessed using a HunterLab Color instrument
    31/52
    Quest XE operated in transmission mode. The results are shown in Table 9 below.
    Table 9 - HunterLab pH and classifications for GP701-02 solution
    Sample pH L * The* B* Turbidity GP701-02 3.23 90.78 0.77 14.00 47.2
    As can be seen from the results in Table 9, the GP701—02 solution was clear and had a light color. The turbidity level was lower than that determined for the GP701-01 solution in Example 5.
    A solution of GP701-02 was heated to 95 ° C, maintained at that temperature for 30 seconds and then immediately cooled to room temperature in an ice bath. The clarity was measured again with the HunterLab instrument and the results are shown in Table 10 below.
    Table 10 - HunterLab classifications for GP701-02 solution after heat treatment
    Sample L * The* B* Turbidity GP701-02 96, 24 -0, 48 9.74 2.2
    As can be seen from the results in Table 10, it was found that the heat treatment of the GP701-02 solution resulted in an extremely clear solution.
    Example 7
    This example illustrates the production of small white bean protein isolate on a bench scale.
    About 150 g of broken small white beans were finely ground using a KitchenAid mixer grinder attachment. 120 g of white bean flour
    32/52 small finely molds were combined with 1,000 mL of 0.15 M CaCl 2 solution at room temperature and stirred for 30 minutes to provide an aqueous protein solution. Residual solids were removed and the resulting protein solution was clarified by centrifugation and filtration, to obtain a filtered protein solution having a protein content of 2.02% by weight. 600 mL of the filtered protein solution was added to 600 mL of RO water and the pH of the sample dropped to 3.01 with HCl solution. Some fine particles were visible in the sample after adjusting the pH and these were removed by passing the sample through a paper filter with a pore size of 25 gm.
    The sample of the diluted and acidified protein extract solution was then reduced in volume from 1,110 mL to 82 mL by concentration on a PES membrane that has a molecular weight cut of 10,000 Dalton. A 79 ml aliquot of the retentate was then diafiltered on the same membrane with 395 ml of RO water. The resulting concentrated, acidified and diafiltered protein solution had a protein content of 10.37% by weight, and represented a yield of 67.6% by weight of the initial filtered protein solution which was subsequently processed. The concentrated, acidified and diafiltered protein solution was dried to yield a product that could have a protein content of 93.75% (N x 6.25) d.b. The product was called the SWB701 protein isolate.
    8.26 g of SWB701 were produced. A solution of SWB701 was prepared by dissolving enough protein powder to provide 0.48 g of protein in 15 mL of
    33/52 RO water and pH was measured with a pH meter and color and clarity assessed using a HunterLab Color Quest XE instrument operated in transmission mode. The results are shown in Table 11 below.
    Table 11 - HunterLab pH and classifications for SWB701 solution
    Sample pH L * The* B* Turbidity SWB701 3.09 97.42 0.22 5.29 73.2
    How can to be seen from results gives Table 11, the SWB701 solution it was limpid and had a color clear. The solution in SWB701 was heated The 95 ° C, maintained at that temperature during 30 seconds and, then,
    immediately cooled to room temperature in an ice bath. The clarity was measured again with the HunterLab instrument and the results are shown in the
    Table 12.
    Table 12 - HunterLab classifications for SWB701 ions after heat treatment
    Sample L * The* B* Turbidity SWB701 98.57 -0.17 4.05 50.0
    As can be seen from the results of Table 12, it was found that the heat treatment improved the clarity and reduced the level of turbidity of the solution, while making it greener and less yellow. Although the level of turbidity in the solution was reduced, the protein solution was still translucent rather than transparent.
    Example 8
    This example contains an assessment of the water solubility of GP701-02 produced by the method of Example 6 and the SWB701 produced by the method of Example 7. The solubility
    34/52 was tested using a modified version of the procedure by Morr et al, J. Food Sei. 50: 1715 - 1718.
    Protein powder sufficient to provide 0.5 g of protein was weighed in a beaker and then about 45 mL of purified water by reverse osmosis (RO) was added. The beaker content was slowly stirred for 60 minutes using a magnetic stirrer. The pH was determined immediately after protein dispersion and was adjusted to the appropriate level (2, 3, 4, 5, 6 or 7) with diluted NaOH or HCl. The sample was also prepared at natural pH. For pH adjusted samples, the pH was measured and corrected periodically, during the 60 minutes of stirring. After 60 minutes of stirring, the samples were raised to a total volume of 50 ml with RO water, yielding a protein dispersion of 1% weight / volume. The protein content of the dispersions was measured using a Leco Nitrogen Determinator FP528. The aliquots of the dispersions were then centrifuged at 7,800 g for 10 minutes, which sedimented insoluble material. The protein content of the supernatant was then determined by Leco analysis.
    The protein solubility was then calculated using the following equation:
    Solubility (%) = (% protein in supernatant /% protein in initial dispersion) x 100
    The natural pH values of the protein isolates produced in Examples 6 and 7 are shown in Table 13 below:
    Table 13 - Natural pH of samples prepared in water at 1% protein weight / volume
    35/52
    Sample natural pH GP701-02 3.23 SWB701 3.09
    The solubility results obtained are shown in Table 14, which follows:
    Table 14 - Solubility of products at different pH values ___________________________________,
    Sample Solubility (%) pH 2 pH 3 pH 4 pH 5 pH 6 pH 7 pHNat. GP701-02 100 100 100 31.1 35.7 37.8 100 SWB701 95.2 95.3 100 88.8 55.4 77.5 94.0
    5 How can be visa From results gives Table 14,both products of 701 were extremely soluble atpH range 2 to 4. Example 9 This example contains an evaluation gives clarity at 10 GP701-02 water produced fur method of Example 6 it's theSWB701 produced by method of Example 7.
    The clarity of the 1% weight / volume dispersions of protein prepared as described in Example 8 was assessed by analyzing the samples on a HunterLab 15 XE ColorQuest instrument operated in transmission mode to provide a percentage turbidity reading. The lower rating indicated greater clarity.
    The cleanliness results are shown in the
    Table 15 below:
    36/52
    Table 15 - Cleanliness of solutions at different pH values, as assessed by HunterLab analysis
    Sample HunterLab Turbidity Reading pH 2 pH 3 pH 4 pH 5 pH 6 pH 7 pHNat. GP701-02 11.9 16.3 17, 4 91.8 92.1 92, 0 14.0 SWB701 0.0 38.0 64, 6 91.7 92.4 82, 9 43, 9
    As can be seen from the results of the
    Table 15, the GP701-02 solutions were substantially clear or slightly cloudy in the pH range 2 to 4. The GP701—02 solutions were cloudy to the highest pH values, where solubility was reduced. The SWB701 solution did not show detectable turbidity at pH 2, but it was noticeably more cloudy as the pH increased. Note that the solubility of the protein was still very high in the pH range 3 to 4, although the solutions were not clear.
    Example 10
    This example illustrates the production of black bean protein product on a bench scale.
    g of black bean flour were combined with 500 ml of 0.15 M CaC12 solution at room temperature and stirred for 30 minutes to provide an aqueous protein solution. Residual solids were removed and the resulting protein solution was clarified by centrifugation and filtration, to obtain a filtered protein solution having a protein content of 1.18% by weight. 450 mL of protein solution
    37/52 filtrate was added to 450 ml of RO water and the pH of the sample dropped to 3.09 with diluted HCl.
    The diluted and acidified protein extract solution was then reduced in volume from 900 mL to 50 mL by concentration on a PES membrane which has a molecular weight cut of 10,000 Dalton. A 40 ml aliquot of the retentate was then diafiltered on the same membrane with 200 ml of RO water. The resulting concentrated, acidified and diafiltered protein solution had a protein content of 6.23% by weight, and represented a yield of approximately 46.9% by weight of the filtered initial protein solution which was subsequently processed. The concentrated, acidified and diafiltered protein solution was dried to yield a product that could have a protein content of 86.33% (N x 6.25) d.b. The product was called BB701.
    2.19 g of BB701 were produced. A BB701 solution was prepared by dissolving enough protein powder to provide 0.48 g of protein in 15 mL of RO water and the pH was measured with a pH meter and color and clarity assessed using a HunterLab Color Quest XE instrument operated in transmission mode. The results are shown in Table 16 below.
    Table 16 - pH and HunterLab ratings for
    BB701
    Sample pH L * The* B* Turbidity BB701 3.14 95.20 0.88 8.22 54.6
    As can be seen from the results in Table 16, the BB701 solution was clear and had a light color.
    38/52
    The BB701 solution was heated to 95 ° C, maintained at that temperature for 30 seconds and then immediately cooled to room temperature in an ice bath. The clarity was measured again with the HunterLab instrument and the results are shown in Table 17.
    Table 17 - HunterLab classifications for BB701 solution after heat treatment
    Sample L * The* B* Turbidity BB701 95.89 0.54 7.81 25.2
    As can be seen from the results in Table 17, it was found that the heat treatment improved the clarity and reduced the level of turbidity of the solution, while making it less red and less yellow. Although the level of turbidity in the solution was reduced, the protein solution was still translucent rather than transparent.
    Example 11
    This example illustrates the production of yellow pea protein isolate on a pilot scale.
    g of yellow split pea flour were combined with 200 L of 0.15 M CaCZ solution at room temperature and stirred for 30 minutes to provide an aqueous protein solution. Residual solids were removed by centrifugation to produce a concentrate having a protein content of 1.53% by weight. 180.4 L of concentrate was added to 231.1 L of RO water and the pH of the sample dropped to 3.0 with diluted HCl. The diluted and acidified concentrate was further clarified by filtration to provide an
    39/52 clear protein solution with a protein content of 0.57% by weight and a pH of 2.93.
    The filtered protein solution was then reduced in volume from 431 L to 28 L by concentration on a PES membrane that has a molecular weight cut of 10,000 Dalton, operated at a temperature of about 30 ° C. At that point, the acidified protein solution with a protein content of 6.35% by weight was diafiltered with 252 L of RO water, with the diafiltration operation conducted at about 30 ° C. The resulting diafiltered solution was then further concentrated to provide 21 kg of acidified, diafiltered protein solution, concentrated with a protein content of 7.62% by weight, which represented a yield of 58.0% of the initial concentrate which was further processed . The concentrated, acidified and diafiltered protein solution was dried to yield a product having a protein content of 103.27% (N x 6.25) d.b .. The product was called YP01-D11-11A YP701 protein isolate.
    Example 12
    This example contains an evaluation of the phytic acid and protein content, as well as the trypsin inhibitor activity of the yellow pea protein isolate produced by the method of Example 11 and a commercial yellow pea protein product called Propulse (Nutripea, Portage la Prairie, MB).
    Protein content was determined by a combustion method using a LecoTruSpec N Nitrogen Nitrogen Determinator. The phytic acid content was determined using the method of Latta and Eskin (J. Agric. Food Chem, 28: 1313-1315). The activity of the inhibitor of
    40/52 trypsin (TIA) was determined using AOCS Ba 12-75 method for the commercial protein sample and a modified version of this method for the product YP701, which has a lower pH when rehydrated.
    The results obtained are shown in Table 18 below:
    Table 18 - Protein content, phytic acid content and trypsin inhibitor activity of protein products
    Lot Product % protein (N x 6.25)d. B. % phytic acidd. B. TIA (TIU / mg protein (N x 6.25)) YP01-D11-11A YP701 103.27 0.27 4.6Propulse 82.33 2.72 3.3
    As can be seen from the results presented in the
    Table 19, ο YP701 had a high protein and low phytic acid content compared to the commercial product. The trypsin inhibitor activity in both products was very low.
    Example 13
    This example contains an evaluation of the dry color and color in the yellow pea protein isolate solution produced by the method of Example 11 and a commercial yellow pea protein product called Propulse (Nutripea, Portage la Prairie, MB).
    The color of dry powders was assessed using a HunterLab ColorQuest XE instrument in reflectance mode. The color values are shown in Table 19 below:
    41/52
    Table 19 - HunterLab classifications for dry protein products
    Sample L * The* B* YP01-D11-11A 86.27 2.21 9.73 YP701 Propulse 82.39 3.29 20.94
    As can be seen from Table 19, the YPO1-D11-11A powder
    YP701 was lighter, less red and less yellow compared to the commercial yellow pea protein product.
    The solutions of the yellow pea protein products were prepared by dissolving enough protein powder to provide 0.48 g of protein in 15 ml of RO water. The pH of the solutions was measured with a pH meter and the color and clarity assessed using a HunterLab Color Quest XE instrument operated in transmission mode. Hydrochloric acid solution was added to the Propulse sample to lower the pH to 3, and then the measurement was repeated. The results are shown in Table 20 below.
    Table 20 - pH and HunterLab ratings for yellow pea protein product solutions
    Sample pH L * The* B* turbidity YP01-D11-11AYP701 3.45 93.97 0.54 12.70 5.0 Propulse 6, 15 35.33 12, 61 48.79 9 6.6 Propulse (pHadjusted) 3.00 37.83 11.55 47, 87 9 6.9
    As can be seen from the results in Table 20, the YP01-D11-11A YP701 solution was transparent, while the
    42/52 Propulse solution very cloudy, regardless of pH. The YP01-D11-11A YP701 solution was also much lighter, less red, less yellow than the Propulse solution, regardless of its pH.
    Example 14
    This example contains an assessment of the thermal stability in water of the yellow pea protein isolate produced by the method of Example 11 and a commercial yellow pea protein product called Propulse (Nutripea,
    Portage la Prairie, MB).
    YP01-D11-11A YP701 2% weight / volume solutions
    Propulse were prepared in water
    RO. The natural pH of the solutions was determined with a meter, each divided into two pH portions. The pH samples of a portion was reduced to 3.00 with HCl solution.
    Control clarity and pH-adjusted solutions were evaluated by measuring turbidity with a HunterLab instrument
    Color Quest XE operated in transmission mode. The solutions were then heated
    95 ° C, maintained temperature for 30 seconds followed, immediately cooled to room temperature in an ice bath. The clarity of the heat-treated solutions was measured again.
    The clarity of protein solutions before and after heating is shown in the following Table:
    Table 21
    Effect of heat treatment on the clarity of protein solutions a
    2% by weight of yellow pea protein products
    PH sample
    Turbidity before
    Turbidity after treatment treatment
    43/52
    thermal (%) thermal (%) YP01-D11-11A3.70 3.6 1, 4 YP701 YP01-D11-11A3.00 2.8 1.3 YP701 (pH adjusted) Propulse 6.24 96, 1 96.4 Propulse (pH 3.00 9 6.6 9 6.6 adjusted)
    As can be seen from the results in Table 21, the YP01-D11-11A YP701 solutions were clear before and after heating at both pH levels. Propulse solutions were very cloudy before and after heating at both pH levels.
    Example 15
    This example contains an assessment of the water solubility of the yellow pea protein isolate produced by the method of Example 11 and a commercial yellow pea protein product called Propulse (Nutripea, Portage la Prairie, MB). Solubility was tested based on the solubility of the protein (called the protein method, a modified version of the procedure by Morr et al, J. Food Sci. 50: 1715-1718) and total product solubility (called the microsphere method).
    Protein powder sufficient to provide 0.5 g of protein was weighed in a beaker and then a small amount of water purified by reverse osmosis (RO) was added and the mixture stirred until a smooth paste was formed. Additional water was then added to bring the volume to approximately 45 ml. The beaker content was
    44/52 then slowly stirred for 60 minutes, using a magnetic stirrer. The pH was determined immediately after protein dispersion and was adjusted to the appropriate level (2, 3, 4, 5, 6 or 7) with diluted NaOH or HCl. The sample was also prepared at natural pH. For pH adjusted samples, the pH was measured and corrected periodically, during the 60 minutes of stirring. After 60 minutes of stirring, the samples were made up to 50 mL of total volume with RO water, obtaining a protein dispersion of 1% weight / volume. The protein content of the dispersions was measured using a Leco TruSpec N Nitrogen Determinator. Aliquots (20 mL) of the dispersions were then transferred to pre-weighed centrifuge tubes that had been dried overnight in an oven at 100 ° C, then the oven was cooled in a desiccator and the tubes capped. The samples were centrifuged at 7,800 g for 10 minutes, which sedimented insoluble material and produced a clear supernatant. The protein content of the supernatant was measured by Leco analysis, and then the supernatant and tube caps were discarded and the pellet material dried overnight in an oven set at 100 ° C. The next morning, the tubes were transferred to a desiccator and cooled. The weight of the dry ball material was recorded. The initial dry weight of the protein powder was calculated by multiplying the weight of the powder used by a factor of ((100 - moisture content of the powder (%)) / 100). The product's solubility was then calculated in two different ways:
    45/52
    1) Solubility (protein method) (%) = (% protein in supernatant /% protein in initial dispersion) χ 100
    2) Solubility (ball method) (%) = (1 - (dry weight of insoluble spherical material / ((weight of 20 mL of dispersion / weight of 50 mL of dispersion) x initial weight of dry powder protein)) ) x 100
    The natural pH values of the protein isolate produced in Example 11 and the commercial yellow pea protein product in water (1% protein) are shown in Table 22:
    Table 22 - Natural pH solutions of YP01-D11-11A
    YP701 and Propulse prepared in water at 1% protein
    Batch Product Natural pH YP01-D11-11A YP701 3.56Propulse 6.15
    The solubility results obtained are shown in Tables 23 and 24 below:
    Table 23 - Product solubility at different pH values based on the protein method
    Solubility (protein method) (%) Batch Product pH 2 pH 3 pH 4 pH 5 pH 6 pH 7 pHNatural YP01-D11-11A YP701 98.2 99.1 99.5 50.9 20, 4 39.3 100Propulse 14.9 3, 6 2, 6 5.3 10, 3 7, 0 8.0
    Table 24 - Solubility of products at different pH values based on the ball method
    46/52
    Solubility (ball method) %) Batch Produto pH 2 pH 3 pH 4 pH 5 pH 6 pH 7 natural pH YP01-D11-11A YP701 99.6 99.3 99.1 74.7 34.7 39, 1 99.0PropuIse 15.5 14.7 11, 6 12.1 16.4 18, 0 16, 5
    As can be seen from the results presented in the
    Tables 23 and 24, YP01-D11-11A YP701 was highly soluble in the pH range 2 to 4 and less soluble at higher pH values. Propulse was found to be very poorly soluble at all tested pH values.
    Example 16
    This example contains an assessment of the water clarity of the yellow pea protein isolate produced by the method of Example 11 and a commercial yellow pea protein product called Propulse (Nutripea, Portage la Prairie, MB).
    The clarity of the 1% w / v protein solutions prepared as described in Example 15 was assessed by measuring the absorbance at 600 nm, with a lower absorbance rating indicating greater clarity. Analysis of the samples on a HunterLab ColorQuest XE instrument in transmission mode also provided a reading of the turbidity percentage, another measure of clarity.
    47/52
    The results of the clarity are presented in the
    Tables 25 and 26 below:
    Table 25 - Cleanliness of protein solutions at different pH s, as assessed by A600
    A600 Batch Product pH 2 pH 3 pH 4 pH 5 pH 6 pH 7 PHNatural YP01-D11-11A YP701 0.012 0.015 0.024 1.962 1.829 2.557 0.021Propulse 2.576 2.479 2.693 2.685 2.558 2.500 2,590
    Table 26 - Cleanliness of protein solutions at different pH values, as assessed by HunterLab turbidity analysis _______________________________
    HunterLab turbidity reading (%) Batch Product pH 2 pH 3 pH 4 pH 5 pH 6 pH 7 PHNatural YP01-D11-11A YP701 0.0 0.1 1, 1 95, 9 96.7 96.4 0, 7Propulse 96.2 96.3 96, 7 96.7 96.2 96.4 96.4
    As can be seen from the results of Tables 25 and
    26, YP01-D11-11A YP701 solutions were transparent in the pH range 2 to 4, but very cloudy at higher pH values. Propulse solutions were very cloudy, regardless of pH.
    Example 17
    This example contains an assessment of the solubility in a soft drink (Sprite) and sports drink (Gatorade orange flavor) of the yellow pea protein isolate produced by the method of Example 11 and a commercial product
    48/52 yellow pea protein called Propulse (Nutripea, Portage la Prairie, MB). Solubility was determined with the protein added to the drinks without pH correction and again with the pH of the protein-enriched drinks adjusted to the original level of the drinks.
    When the solubility was evaluated without pH correction, an amount of protein powder sufficient to provide 1 q of protein was weighed in a beaker and a small amount of drink was added and stirred until a smooth paste was formed. More drink was added to bring the volume to 50 ml, and then the solutions were slowly stirred with a magnetic stirrer over 60 minutes to produce a 2% w / v protein dispersion. The protein content of the samples was analyzed using a Leco TruSpec N Nitrogen Determinator then an aliquot of the protein-containing drinks was centrifuged at 7,800 g for 10 minutes and the protein content of the supernatant was measured.
    Solubility (%) = (% protein in supernatant /% protein in initial dispersion) x 100.
    When the solubility was evaluated with pH correction, the pH of the soft drink (Sprite) (3.42) and the sports drink (Gatorade orange flavor) (3.11) without protein was measured. An amount of protein powder sufficient to provide 1 q of protein was weighed in a beaker and a small amount of drink was added and stirred until a smooth paste was formed. More drink was added to bring the volume to approximately 45 mL, and then the solutions were stirred slowly with a
    49/52 magnetic stirrer for 60 minutes. The pH of protein-containing drinks was determined immediately after dispersing the protein and was adjusted to pH without protein originating with HCl or NaOH if necessary. The pH was maintained and corrected periodically during the 60 minutes of stirring. After 60 minutes of stirring, the total volume of each solution was brought to 50 ml with the addition of drink, yielding a protein dispersion at 2% weight / volume. The protein content of the samples was analyzed using a Leco TruSpec N Nitrogen Determinator then an aliquot of the protein-containing drinks was centrifuged at 7,800 g for 10 minutes and the protein content of the supernatant was measured.
    Solubility (%) = (% protein in supernatant /% protein in initial dispersion) x 100
    The results obtained are shown in Table 27 below:
    Table 27: Solubility of yellow pea protein products in Sprite and Gatorade Orange flavor
    uncorrected pH pH color hard Batelad Product Solubility Solubility Solubility Solubility Theand (%) in and (%) in and (%) in and (%) in Sprite Gatorade Sprite Gatorade flavorflavor orange aorange a YP01- YP701 98.1 100 96, 6 100 D11-11A Propuls 3.2 4, 6 5, 6 7, 4and
    As can be seen from the results of the
    Table 27, YP01-D11-11A YP701 was highly soluble in the
    50/52
    Sprite and Gatorade orange flavor. As ο YP701 is an acidified product, its addition did not significantly change the pH of the drinks. Propulse was very poorly soluble in the tested drinks. Addition of Propulse increased the pH of the drinks, but the solubility of the protein was not improved by reducing the pH of the drink back to its original protein-free value.
    Example 18:
    This example contains an assessment of the clarity in a soft drink and sports drink of the yellow pea protein isolate produced by the method of Example 11 and a commercial yellow pea protein product called Propulse (Nutripea, Portage la Prairie, MB).
    The clarity of the 2% weight / volume protein dispersions prepared in soft drinks (Sprite) and sports drinks (Gatorade orange flavor) in Example 17 was evaluated using the A600 and HunterLab turbidity methods described in Example 16.
    The results obtained are presented in Tables and 29 that follow:
    Table 28: Readings in A600 for yellow pea protein products in Sprite and Gatorade orange flavor
    uncorrected pH pH color hard Batch Product A600 in A600 in A600 in A600 in Sprite Gatorade Sprite Gatorade flavorflavor orange aorange a 0.007 0.450 0.007 0.450 Without
    51/52
    protein YP01-D11-11A YP701 0.048 0.338 0.043 0.345Propulse 2,800 2,834 2,827 2,793
    Table 29 - Turbidity readings for yellow pea protein products in Sprite and orange Gatorade
    uncorrected pH pH color hard Batch Product Turbidity Turbidity Turbidity Turbidity (%) at the (%) at the (% ) at the (%) at the Sprite Gatorade Sprite Gatorade flavorflavor orange aorange a Without0.0 78.6 0.0 78.6 proteinYP01- YP701 5.7 56, 7 4, 9 57.7 D11-11A Propulse 97.1 97.5 96.3 96, 3
    As can be seen from the results of the
    Tables 28 and 29, the addition of YP01 D11-11A YP701 to the soda and sports drink added little or no turbidity, while the addition of Propulse made the drinks very cloudy, even when the pH was corrected.
    SUMMARY OF THE REVELATION
    In summary, the present invention provides new pulse protein products, which are completely soluble and form heat-stable, preferably transparent, pH-acid solutions and are useful for protein enrichment of aqueous systems, including soft drinks and sports drinks, without causing
    52/52 protein precipitation. Modifications are possible within the scope of the present invention.
    权利要求:
    Claims (5)
    [1]
    1. Method of manufacturing a protein pulse product with a protein content of at least 60% by weight (N x 6.25) on a dry weight basis, characterized by the fact that it comprises:
    (a) extraction of a pulse source of protein with an aqueous solution of calcium salt with a concentration of
    0.15 M to 1.0 M, optionally containing an antioxidant, to cause the protein pulse to solubilize from the protein source and to form an aqueous protein pulse solution, in which said extraction step
    a) is carried out at a temperature of 1 to 65 ° C and a pH of
    4.5 to
    11;
    (b) at least partial separation of the aqueous protein pulse solution from the pulse source of residual protein,
    c) optional dilution of the aqueous protein pulse solution to a conductivity of less than 90 mS, wherein said aqueous protein pulse solution is diluted with an aqueous diluent having a temperature of
    1 at 65 ° C, (d) adjusting the pH of the protein solution to a pH of 1.5 to 4.4 of aqueous pulse to produce an acidic aqueous pulse protein solution, (e) optional clarification by filtration of the acidified protein pulse solution if it is not already clear, (f) alternatively, from steps (b) to (e), optional dilution and then adjusting the pH of the solution
    Petition 870200001137, of 03/01/2020, p. 9/19
    [2]
    2/5 aqueous pulse of combined protein and pulse source of residual protein to a pH of 1.5 to 4.4 and to a conductivity of less than 90 mS, and in which said aqueous pulse protein solution is diluted with an aqueous diluent having a temperature of 1 to 65 ° C, then separating the acidified aqueous protein pulse solution from the residual protein pulse source, (g) optional concentration of the aqueous protein pulse solution, while maintaining the constant ionic strength through a selective membrane technique, (h) optional diafiltration of the concentrated protein pulse solution, and (i) drying, optional of the concentrated and optionally diafiltered pulse solution.
    2. Method according to claim 1, characterized in that said aqueous solution of calcium salt is an aqueous solution of calcium chloride.
    [3]
    Method according to claim 1 or 2, characterized in that said aqueous protein pulse solution has a protein concentration of 5 to 50 g / L.
    [4]
    Method according to any one of claims 1 to 3, characterized in that after said separation step (b) and before said optional dilution step (c) or in step (f) before said step of optional dilution, said aqueous protein pulse solution is treated with an adsorbent to remove the color and / or odor compounds from the aqueous protein pulse solution.
    Petition 870200001137, of 03/01/2020, p. 10/19
    3/5
    5. Method, in wake up with any an of claims 1 to 4, featured fur fact of that said acidified solution in pulse in protein has an conductivity of less in 95 mS. 6. Method, in wake up with any an of claims 1 to 5, featured fur fact of that the pH of said aqueous solution of protein pulse is adjusted on stage (d) or (f) for pH 2 at 4. 7. Method, in wake up with any an of
    claims 1 to 6, characterized by the fact that the acidified pulse protein solution is subjected to step (e).
    Method according to any one of claims 1 to 7, characterized in that said acidified aqueous protein pulse solution is dried to provide a protein pulse product having a protein content of at least 60% in weight (N x 6.25) db.
    Method according to any one of claims 1 to 8, characterized in that said acidified aqueous protein pulse solution is subjected to step (g) to produce a concentrated acidified protein pulse solution with a concentration of protein from 50 to 300 g / L, and the concentrated acidified protein pulse solution is optionally subjected to step (h), optionally in the presence of an antioxidant, until no additional amount of contaminants or visible color is present in the permeate.
    Petition 870200001137, of 03/01/2020, p. 11/19
    4/5
    10. Method according to claim 9, characterized in that said concentrated and optionally diafiltered protein pulse solution is treated with an adsorbent to remove color and / or odor compounds.
    11. Method according to claim 9 or 10, characterized in that said concentrated and optionally diafiltered acidified protein pulse solution is pasteurized before drying at a temperature of 55 ° C to 70 ° C for 30 seconds at 60 minutes.
    Method according to any one of claims 9 to 11, characterized in that the concentrated and optionally diafiltered protein pulse solution is dried to provide a protein product having a protein content of at least 60% by weight (N x 6.25) db.
    13. Method according to any of claims 1 to 12, characterized in that said acidified aqueous protein solution following step (d) or step (f) and / or partially concentrated or concentrated solution and optionally pulse diafiltered protein is subjected to the heat treatment step to inactivate the thermally labile antinutritional factors including thermally labile trypsin inhibitors, at a temperature of 70 ° to 160 ° C for 10 seconds to 60 minutes, and where the acidified pulse solution of heat-treated protein is cooled to a temperature of 2 ° to 65 ° C, for processing
    Petition 870200001137, of 03/01/2020, p. 12/19
    [5]
    5/5 additional and where the heat treated protein pulse solution is subjected to an optional polishing step.
    14. Method according to any of claims 1 to 13, characterized in that a reducing agent is present during the extraction step (a) and / or the optional concentration and / or diafiltration steps (g) and ( h) and / or is added to the concentrated and optionally diafiltered protein pulse solution prior to the drying step (i) and / or the dried protein pulse product to interrupt or rearrange the disulfide bonds of the trypsin inhibitors in order to obtain a reduction in the activity of the trypsin inhibitor.
    15. Pulse protein product, characterized by the fact that it has a protein content of at least 60% by weight (N x 6.25) d.b. which is soluble in water and produces thermally stable solutions, without leading to protein precipitation, at acid pH values of less than 4.4 or said aqueous solution thereof, in which it is combined with water-soluble powder materials for production of the aqueous solutions of the combination.
    类似技术:
    公开号 | 公开日 | 专利标题
    BR112012028444B1|2020-03-24|METHOD OF MANUFACTURING A PROTEIN PULSE PRODUCT AND PROTEIN PULSE PRODUCT
    JP6154097B2|2017-06-28|Production of soy protein products | using calcium chloride extraction
    DK2912952T3|2018-01-15|PREPARATION OF ACID-SOLUBLE SOY PROTEIN ISOLATES |
    BRPI1006982B1|2019-01-22|process of preparing a soluble soy protein product from soy protein micellar mass |, soy protein product and acidic solution
    BRPI1008755B1|2018-01-09|PROCESS FOR PREPARING A SOY PROTEIN PRODUCT
    BRPI1011581B1|2018-05-29|SOY PROTEIN ISOLATED PRODUCTION PROCESS USING CALCIUM CHLORIDE EXTRACTION |
    BR112015029903B1|2021-02-09|method of preparing the protein product of legumes with reduced astringency
    RU2631000C2|2017-09-15|Production of soluble soy product |
    DK2709464T3|2017-02-06|PREPARATION OF SOY PROTEIN ISOLATE USING CALCIUM CHLORIDE EXTRACTION |
    BR112015007140B1|2021-03-23|METHOD OF PRODUCTION OF A PROTEIN PULSES PRODUCT
    US20160227833A1|2016-08-11|Production of soluble protein solutions from pulses
    BR112015001964A2|2019-12-17|PRODUCTION OF SOLUBLE HEMP PROTEIN PRODUCTS |
    US9700066B2|2017-07-11|Preparation of soy protein isolate using calcium chloride extraction |
    BRPI1008535B1|2021-11-23|METHOD OF PRODUCTION OF A SOYBEAN PROTEIN PRODUCT USING CALCIUM CHLORIDE EXTRACTION
    同族专利:
    公开号 | 公开日
    RU2012152607A|2014-06-20|
    BR112012028444A2|2015-09-15|
    CA2796643C|2021-01-05|
    EP2566346A4|2015-04-08|
    KR20130079408A|2013-07-10|
    AU2011250599A1|2012-12-20|
    JP2016104047A|2016-06-09|
    EP2566346A1|2013-03-13|
    US20110274797A1|2011-11-10|
    US20130129901A1|2013-05-23|
    JP6605368B2|2019-11-13|
    CN103079410A|2013-05-01|
    JP2018110600A|2018-07-19|
    RU2612882C2|2017-03-13|
    AU2011250599B9|2014-08-07|
    CN107259067A|2017-10-20|
    JP2013527771A|2013-07-04|
    CA2796643A1|2011-11-10|
    MX2012013000A|2013-03-05|
    AU2011250599B2|2014-07-10|
    ZA201208533B|2014-01-29|
    WO2011137524A1|2011-11-10|
    NZ603762A|2015-01-30|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3736147A|1971-04-05|1973-05-29|Coca Cola Co|Process for preparing protein products|
    CH564314A5|1973-04-17|1975-07-31|Nestle Sa|
    CA1028552A|1976-09-30|1978-03-28|Edward D. Murray|Protein product and process for preparing same|
    CA1099576A|1978-03-23|1981-04-21|Chester D. Myers|Improved process for isolation of proteins|
    CA1104871A|1978-06-02|1981-07-14|Woodstone Technologies Limited|Process for preparing products from legumes|
    US4677065A|1986-03-24|1987-06-30|Aktieselskabet De Danske Sukkerfabrikker|Production of improved protein isolate derived from seeds of a grain legume|
    US4889921A|1987-04-29|1989-12-26|The University Of Toronto Innovations Foundation|Production of rapeseed protein materials|
    EP0752212B1|1995-07-07|2004-05-26|Fuji Oil Company, Limited|Process for preparing fractionated soybean proteins and foods using the same|
    JP2001302689A|2000-04-19|2001-10-31|Protein Technol Internatl Inc|Process for separating and recovering protein and isoflavones from plant material|
    DE60239669D1|2001-02-28|2011-05-19|Fuji Oil Co Ltd|SOYBEAN PROTEIN, METHOD FOR THE PRODUCTION THEREOF, AND PROTEIN FOOD CONTAINING ITS ACID|
    US8741356B2|2001-05-04|2014-06-03|Burcon Nutrascience Corp.|Production of oil seed protein isolate|
    MXPA04005664A|2001-12-13|2004-12-06|Burcon Nutrascience Mb Corp|Enhanced oil seed protein recovery.|
    WO2004037021A1|2002-10-24|2004-05-06|Unilever N.V.|Liquid acidic food products|
    GB0329832D0|2003-12-23|2004-01-28|Unilever Plc|Beverages and their preparation|
    US8470385B2|2004-01-20|2013-06-25|Burcon Nutrascience Corp.|Beverage having purified or isolate protein component|
    ZA200610169B|2004-05-07|2008-06-25|Burcon Nutrascience Mb Corp|Protein isolation procedures for reducing phytic acid|
    FR2889416B1|2005-08-05|2007-10-26|Roquette Freres|COMPOSITION OF PEAS PROTEINS|
    EP1937081A4|2005-09-21|2012-04-25|Burcon Nutrascience Mb Corp|Preparation of canola protein isolate involving isoelectric precipitation|
    CA2584280A1|2006-03-30|2007-09-30|Douglas J. Harle|Lentil extract|
    CN101238846A|2008-01-18|2008-08-13|王雪源|Mung bean pea edible separation protein and producing method thereof|
    AU2009267707B2|2008-07-11|2015-03-05|Burcon Nutrascience Corp.|Soluble canola protein isolate production|
    NZ616202A|2008-10-21|2015-04-24|Burcon Nutrascience Mb Corp|Production of soluble protein solutions from soy |
    ES2558335T3|2009-01-26|2016-02-03|Burcon Nutrascience Corp.|Production of soluble soy protein products from the micellar mass of soy protein |
    CN102387713B|2009-02-11|2015-07-29|伯康营养科学公司|Soy protein products is produced with calcium chloride extraction|
    KR20130079408A|2010-05-07|2013-07-10|버콘 뉴트라사이언스 코포레이션|A method of producing soluble protein solutions from pulses and product thereof|US9220292B2|2004-10-07|2015-12-29|Next Problems, Inc.|Protein beverage and method of making same|
    US10689678B2|2008-11-04|2020-06-23|The Quaker Oats Company|Method and composition comprising hydrolyzed starch|
    KR20130079408A|2010-05-07|2013-07-10|버콘 뉴트라사이언스코포레이션|A method of producing soluble protein solutions from pulses and product thereof|
    US20120135117A1|2010-05-07|2012-05-31|Segall Kevin I|Production of soluble protein solutions from pulses|
    US10506821B2|2010-05-07|2019-12-17|Burcon MutrascienceCorp.|Production of soluble protein solutions from pulses|
    AU2012255589B2|2011-05-19|2016-06-16|Burcon NutrascienceCorp.|Production of soluble soy protein product |
    AU2013252437A1|2012-04-25|2014-11-27|Burcon NutrascienceCorp.|Improved production of soluble protein products from pulses|
    KR20150043315A|2012-07-09|2015-04-22|버콘 뉴트라사이언스코포레이션|Frozen dessert mixes using pulse protein products|
    US11134705B2|2012-07-10|2021-10-05|Burcon NutrascienceCorp.|pH adjusted pulse protein product|
    BR112015000382A2|2012-07-10|2019-10-08|Burcon Nutrascience Mb Corp|pH-adjusted legume protein products|
    JP2015523090A|2012-08-02|2015-08-13|バーコン ニュートラサイエンス （エムビー） コーポレイションＢｕｒｃｏｎ Ｎｕｔｒａｓｃｉｅｎｃｅ （Ｍｂ） Ｃｏｒｐ．|Manufacture of soluble protein productsfrom hemp|
    MX357208B|2012-10-02|2018-06-29|Burcon Nutrascience Mb Corp|Production of pulse protein product using calcium chloride extraction .|
    MX2015012410A|2013-03-11|2016-02-03|Burcon Nutrascience Mb Corp|Production of pulse protein product.|
    US9635875B2|2013-05-30|2017-05-02|Burcon NutrascienceCorp.|Production of pulse protein products with reduced astringency|
    US20160227822A1|2013-09-13|2016-08-11|Otsuka Pharmaceutical Factory, Inc.|Food composition|
    DK3071045T3|2013-11-18|2020-07-13|Cosucra Groupe Warcoing Sa|Method for extraction of pea proteins|
    US11213048B2|2014-07-25|2022-01-04|Smallfood, Inc.|Protein rich food ingredient from biomass and methods of preparation|
    CA2992860A1|2015-07-24|2017-02-02|Synthetic Genomics, Inc.|A protein rich food ingredient from biomass and methods of production|
    US11122817B2|2014-07-25|2021-09-21|Smallfood Inc.|Protein rich food ingredient from biomass and methods of production|
    CN113349283A|2014-07-28|2021-09-07|伯康营养科学公司|Preparation of pulse protein product ("YP 810|
    US10433571B2|2014-08-27|2019-10-08|Burcon NutrascienceCorp.|Preparation of soy protein products |
    BE1022936B1|2015-05-13|2016-10-20|Cosucra Groupe Warcoing S.A.|PROCESS FOR PREPARING A PEAS EXTRACT|
    CN105941115A|2016-05-13|2016-09-21|晶叶（青岛）生物科技有限公司|Rice coleoptiles and content extraction method and application thereof|
    CN107385002A|2017-08-23|2017-11-24|无锡金农生物科技有限公司|A kind of co-production technology of chick-pea starch and chick-pea soluble protein|
    US11102998B1|2017-08-25|2021-08-31|The Hershey Company|Binders and methods of making and using the same|
    EP3540035A1|2018-03-13|2019-09-18|The Procter & Gamble Company|Hand dishwashing detergent composition|
    CN111748023A|2020-03-09|2020-10-09|烟台双塔食品股份有限公司|Environment-friendly and energy-saving method for extracting albumin|
    法律状态:
    2018-03-27| B15K| Others concerning applications: alteration of classification|Ipc: C07K 1/14 (2006.01), A23J 1/14 (2006.01), A23J 3/1 |
    2018-04-10| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|
    2019-05-21| B07A| Application suspended after technical examination (opinion) [chapter 7.1 patent gazette]|
    2019-10-08| B06A| Patent application procedure suspended [chapter 6.1 patent gazette]|
    2020-01-28| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|
    2020-03-24| B16A| Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 09/05/2011, OBSERVADAS AS CONDICOES LEGAIS. |
    优先权:
    申请号 | 申请日 | 专利标题
    US34401310P| true| 2010-05-07|2010-05-07|
    US61/344,013|2010-05-07|
    PCT/CA2011/000529|WO2011137524A1|2010-05-07|2011-05-09|Production of soluble protein solutions from pulses|
    [返回顶部]