Provided herein are methods for producing a mung bean protein isolate having high functionality for a broad range of food applications. In some embodiments, the methods for producing the isolate comprise one or more steps selected from: (a) extracting one or more mung bean proteins from a mung bean protein source in an aqueous solution, for example, at a pH between about 6.5-10.0; (b) purifying protein from the extract using at least one of two methods: (i) precipitating protein from the extract at a pH near the isoelectric point of a globulin-rich fraction, for example a pH between about 5.0-6.0; and/or (ii) fractionating and concentrating protein from the extract using filtration such as microfiltration, ultrafiltration or ion-exchange chromatography; and (c) recovering purified protein isolate.

The present disclosure provides an exemplary method for producing non-dairy cheese. In some embodiments, this novel process of making non-dairy cheese may be similar to the manufacturing of traditional dairy cheese. In some aspects, the seeds used in this process may be used for the production of other products that may or may not be related to the non-dairy cheese production. In some embodiments, different cultures may be added to the non-dairy cheese to give it different textures, chemical balances, tastes, and other attributes, as non-limiting examples. In some implementations, throughout the process, the pH and moisture levels may be monitored, which may ensure the mixture reaches target levels at each step of the process. In some aspects, other criteria based on weight of cheese, amount of culture added, and other non-limiting factors may impact the production of the non-dairy cheese.

Provided herein are methods and compositions for the production of cheese replicas. Generally the cheese replicas are produced by inducing the enzymatic curdling of non-dairy milks.

Provided herein are methods for producing a mung bean protein isolate having high functionality for a broad range of food applications. In some embodiments, the methods for producing the isolate comprise one or more steps selected from: (a) extracting one or more mung bean proteins from a mung bean protein source in an aqueous solution, for example, at a pH between about 6.5-10.0; (b) purifying protein from the extract using at least one of two methods: (i) precipitating protein from the extract at a pH near the isoelectric point of a globulin-rich fraction, for example a pH between about 5.0-6.0; and/or (ii) fractionating and concentrating protein from the extract using filtration such as microfiltration, ultrafiltration or ion-exchange chromatography; and (c) recovering purified protein isolate.

A method for producing a vegan food product particulate (X, Y) based on almond flour, as a recipe component or directly as a final food product, includes: a) providing partially de-oiled almond flour having between 5 and 20% by weight fat and between 43 and 57% by weight protein, b) providing water, c) producing a liquid mixture of the partially de-oiled almond flour and the water, the percentage by weight of the almond flour being between 1 and 40% by weight and of water being between 60 and 99% by weight, d) heating the liquid mixture to a temperature between 72 C. and 138 C. and obtaining a heated liquid, e) high-pressure homogenizing the heated liquid in a hot high-pressure homogenization step and obtaining a heated hot high-pressure homogenized liquid, f) cooling the heated hot high-pressure homogenized liquid.

The present disclosure relates to unique soluble pea protein product can be used alone to make aerated bakery products, confections, desserts, sauces, and beverages. The soluble pea protein product can be combined with insoluble pea protein product to make a range of food products with higher protein content than when insoluble, globular pea protein product is used alone, due to the viscosity reducing nature of the soluble pea protein product when it is combined with insoluble globular pea protein product. The soluble pea protein products when combined with insoluble pea protein products, make a resulting pea protein product that has a PDCAAS of about 0.75-1.00. The process to make this unique soluble pea protein includes means of selectively separating the soluble pea protein product from the insoluble fractions of ground peas, as well as selectively separating the soluble pea protein from soluble carbohydrates and ash. This Abstract is not intended to identify key features or essential features of subject matter, nor does this Abstract intend to be used to limit the scope of claimed subject matter.

Disclosed herein are methods of making and using, as well as products obtained by, continuous high pressure based Ultra Shear Technology (UST). These products are homogenous and stable blends of plant and animal proteins. These methods allow for the formulation and manufacture of stable liquid food products without the use of synthetic additives. The plant/animal protein blends are useful in formulating novel protein liquid foods with varied consumer applications.

Disclosed are dairy alternative food compositions comprising at least one fermentation-derived casein subunit. Also disclosed are methods of producing such food compositions. Further disclosed are uses of fermentation-derived casein subunit(s) in combination with plant-based protein(s) to improve the quality of dairy alternative products.

The invention provides a gelled composition of mung bean protein comprising a mung bean protein and an alkali metal ion, wherein the gelled composition of mung bean protein comprises the alkali metal ion at 50 mM or greater based on the total amount of the gelled composition of mung bean protein.

Provided herein are methods for producing a mung bean protein isolate having high functionality for a broad range of food applications. In some embodiments, the methods for producing the isolate comprise one or more steps selected from: (a) extracting one or more mung bean proteins from a mung bean protein source in an aqueous solution, for example, at a pH between about 6.5-10.0; (b) purifying protein from the extract using at least one of two methods: (i) precipitating protein from the extract at a pH near the isoelectric point of a globulin-rich fraction, for example a pH between about 5.0-6.0; and/or (ii) fractionating and concentrating protein from the extract using filtration such as microfiltration, ultrafiltration or ion-exchange chromatography; and (c) recovering purified protein isolate.