Abstract: A dry fractionation method and system provides for generating a protein concentrate product therefrom. The method and system includes milling a plant-based flour to generate milled flour and generating a first protein concentrate from the milled flour using an air classifier. The method and system includes processing the first protein concentrate to generate a protein rich curd and generating a neutral hydrolyzed protein slurry by mixing the protein curd with a base, water and enzymatic cocktail. The method and system includes generating a homogenized protein slurry from the protein slurry and generating a cooled protein slurry by pasteurizing the homogenized protein slurry. Therein, the method and system provides for extracting the protein concentrate product from the cooled protein slurry.

Abstract: A method provides for removing oil content from a source material and extracting protein from the source material prior to generating a protein concentrate, including decorticating the source material, the source material having a protein and an oil content therein, the decorticating to remove a cortex from the source material. The method includes creating a flour from the source material having the cortex removed therefrom, removing at least a portion of the oil content from the flour by generating a solvent mixture by mixing the flour with a solvent and extracting a de-oiled flour from the solvent mixture, including oil and sugars extracted from the flour. The solvent may include supercritical CO2, subcritical CO2, ethanol, or a combination thereof. The method includes drying the de-oiled flour using at least one dryer and extracting a protein concentrate from the de-oiled flour.

Abstract: A system and method for vicine/covicine removal includes generating a feed stock from a plant-based protein source, the plant-based protein source having anti-nutritionals disposed therein, including vicine and covicine. The system and method includes generating an ethanol slurry by combining the feed stock with an ethanol wash containing a first volume of ethanol and processing the ethanol slurry through an extractor to generate an ethanol matrix and a feed stock mass. The method and system further includes providing the feed stock mass to a desolventizer and generating a desolventized feed stock mass therefrom. Therein, the method and system includes drying the desolventized feed stock mass to generate a clean feed stock with at least a portion of the vicine/covicine removed therefrom.

Abstract: A dry fractionation method and system provides for generating a protein concentrate product therefrom. The method and system includes milling a plant-based flour to generate milled flour and generating a first protein concentrate from the milled flour using an air classifier. The method and system includes processing the first protein concentrate to generate a protein rich curd and generating a neutral hydrolyzed protein slurry by mixing the protein curd with a base, water and enzymatic cocktail. The method and system includes generating a homogenized protein slurry from the protein slurry and generating a cooled protein slurry by pasteurizing the homogenized protein slurry. Therein, the method and system provides for extracting the protein concentrate product from the cooled protein slurry.

Abstract: A method and system provides for for de-oiling and extracting protein from chickpeas prior to generating chickpea protein concentrate. The method and system includes receiving a chickpea flour generated from the chickpeas, including having cortex material removed from the chickpeas and generating an ethanol mixture by mixing the chickpea flour with ethanol to remove at least a portion of the oil content from the chickpea flour. The method and system includes separating the ethanol mixture into a de-oiled chickpea flour and an ethanol recycling stream having organics from the chickpea flour absorbed therein. Therein, the method and system includes extracting a protein concentrate from the de-oiled flour.

Abstract: A system and method for vicine/covicine removal includes generating a feed stock from a plant-based protein source, the plant-based protein source having anti-nutritionals disposed therein, including vicine and covicine. The system and method includes generating an ethanol slurry by combining the feed stock with an ethanol wash containing a first volume of ethanol and processing the ethanol slurry through an extractor to generate an ethanol matrix and a feed stock mass. The method and system further includes providing the feed stock mass to a desolventizer and generating a desolventized feed stock mass therefrom. Therein, the method and system includes drying the desolventized feed stock mass to generate a clean feed stock with at least a portion of the vicine/covicine removed therefrom.

Abstract: A system and method for anti-nutritional removal includes generating a feed stock from a plant-based protein source, the plant-based protein source having anti-nutritionals disposed therein. The system and method includes generating an ethanol slurry by combining the feed stock with an ethanol wash containing a first volume of ethanol and processing the ethanol slurry through an extractor to generate an ethanol matrix and a feed stock mass. The method and system further includes providing the feed stock mass to a desolventizer and generating a desolventized feed stock mass therefrom. Therein, the method and system includes drying the desolventized feed stock mass to generate a clean feed stock with at least a portion of the anti-nutritionals removed therefrom. In one embodiment, the feed stock may be fava beans with the removal of vicine and covicine as anti-nutritionals.

Abstract: A method and system provides for for de-oiling and extracting protein from chickpeas prior to generating chickpea protein concentrate. The method and system includes receiving a chickpea flour generated from the chickpeas, including having cortex material removed from the chickpeas and generating an ethanol mixture by mixing the chickpea flour with ethanol to remove at least a portion of the oil content from the chickpea flour. The method and system includes separating the ethanol mixture into a de-oiled chickpea flour and an ethanol recycling stream having organics from the chickpea flour absorbed therein. Therein, the method and system includes extracting a protein concentrate from the de-oiled flour.

Abstract: A dry fractionation method and system provides for generating a protein concentrate product therefrom. The method and system includes milling a plant-based flour to generate milled flour and generating a first protein concentrate from the milled flour using an air classifier. The method and system includes processing the first protein concentrate to generate a protein rich curd and generating a neutral hydrolyzed protein slurry by mixing the protein curd with a base, water and enzymatic cocktail. The method and system includes generating a homogenized protein slurry from the protein slurry and generating a cooled protein slurry by pasteurizing the homogenized protein slurry. Therein, the method and system provides for extracting the protein concentrate product from the cooled protein slurry.

Abstract: A system and method for de-oiling for generating a protein concentrate therefrom. The method and system includes decorticating a material having an oil content to remove cortex therefrom, the material including a protein therein. The method and system further includes creating a flour from the material having the cortex removed therefrom and removing the oil content from the flour by mixing the flour with ethanol. The method and system further extracts a de-oiled flour therefrom and dries the de-oiled flour using at least one dryer. Therein, the method and system provides for extracting the protein concentrate from the de-oiled flour.

Abstract: A system and method for anti-nutritional removal includes generating a feed stock from a plant-based protein source, the plant-based protein source having anti-nutritionals disposed therein. The system and method includes generating an ethanol slurry by combining the feed stock with an ethanol wash containing a first volume of ethanol and processing the ethanol slurry through an extractor to generate an ethanol matrix and a feed stock mass. The method and system further includes providing the feed stock mass to a desolventizer and generating a desolventized feed stock mass therefrom. Therein, the method and system includes drying the desolventized feed stock mass to generate a clean feed stock with at least a portion of the anti-nutritionals removed therefrom. In one embodiment, the feed stock may be fava beans with the removal of vicine and covicine as anti-nutritionals.

Abstract: A dry fractionation method and system provides for generating a protein concentrate product therefrom. The method and system includes milling a plant-based flour to generate milled flour and generating a first protein concentrate from the milled flour using an air classifier. The method and system includes processing the first protein concentrate to generate a protein rich curd and generating a neutral hydrolyzed protein slurry by mixing the protein curd with a base, water and enzymatic cocktail. The method and system includes generating a homogenized protein slurry from the protein slurry and generating a cooled protein slurry by pasteurizing the homogenized protein slurry. Therein, the method and system provides for extracting the protein concentrate product from the cooled protein slurry.

Abstract: A system and method for de-oiling for generating a protein concentrate therefrom. The method and system includes decorticating a material having an oil content to remove cortex therefrom, the material including a protein therein. The method and system further includes creating a flour from the material having the cortex removed therefrom and removing the oil content from the flour by mixing the flour with ethanol. The method and system further extracts a de-oiled flour therefrom and dries the de-oiled flour using at least one dryer. Therein, the method and system provides for extracting the protein concentrate from the de-oiled flour.

Abstract: A catalyst for the dehydrogenation of C.sub.6 -C.sub.15 paraffins is disclosed. The catalyst contains, on support, at least one platinum group component, at least one promoter component from the group tin, germanium and lead, and at least one additional modifier. The additional modifier contains at least one alkaline earth metal. The stability of the catalyst is essentially higher than that achieved by conventional use of an alkali metal.

Abstract: A catalyst for the dehydrogenation of C6.sub.6 -C.sub.15 paraffins is disclosed. The catalyst contains, on a support, at least one platinum group component, at least one promoter component from the group tin, germanium and lead, and at least one additional modifier. The additional modifier contains at least one alkaline earth metal. The stability of the catalyst is essentially higher than that achieved by conventional use of an alkali metal.

Abstract: A process is disclosed for continuously hydrogenating unsaturated fats, fatty acids or fatty acid esters on a shaped catalyst in a solid bed. The reactants flow over the catalyst in the presence of a medium or solvent mixture in supercritical conditions. This leads to considerably improved activity and selectivity of the hydrogenation reaction compared with conventional trickle bed hydrogenation processes.

Abstract: Catalytic reforming of C.sub.9 + containing naphtha with a high yield of BTX is disclosed. Naphtha is converted under customary reforming conditions on a catalyst which contains at least one platinum group metal at least one metal of the group IV B, and at least one halogen component on an oxidic carrier.

Abstract: A ternary platinum alloy catalyst on a conductive carbon carrier for use in fuel cells is disclosed. For the production of the catalyst, nitrate salts are used as precursors of the alloy components and all alloy components are deposited concurrently on the carbon carrier. This method of procedure yields ageing-stable catalysts with high oxygen mass activity.

Abstract: A process is disclosed for the selective catalytic hydrogenation of carbonyl groups in aromatic aldehydes of the formula: ##STR1## in which X is carboxyl, methyl or a halogen, to give the corresponding alcohols and methyl compounds. The catalytic hydrogenation is performed with the addition of a solvent optionally in the presence of organic acids on a shaped support catalyst containing a platinum group metal on a support made from titanium oxide in the presence of hydrogen at hydrogen partial pressures of 5 to 50 bar and temperatures of 100.degree. to 300.degree. C.

Abstract: A catalyst for the selective reduction of nitrous oxide with ammonia contains, in addition to titanium oxide as component (A), at least one oxide of W, Si, B, Al, P, Zr, Ba, Y, La, Ce and at least one oxide of Y, Nb, Mo, Fe, Cu as component (B), whereby the atomic ratio between the elements of components (A) and (B) amounts to 1:0.001 up to 1. The catalyst can be obtained by kneading reactive titanium oxide with a high specific surface of predominantly anatase with the substances of component (B) or their preliminary stages, adding processing agents, winding up with a homogeneous kneaded mass, extruding the latter, drying the extrudate and calcining in air at 300.degree.-800.degree. C.