Abstract: A mineral-vitamin complex for osteoporosis includes at least 92 mass % of the mineral-vitamin complex of amino acids and Krebs cycle acids and/or Krebs cycle acid salts, wherein the amino acids include glycine of between 1% and 80% of the mineral-vitamin complex, and wherein the Krebs cycle acids and/or Krebs cycle acid salts are up to 5 mass % of the mineral-vitamin complex; and valine, leucine and isoleucine such that a mass ratio of glycine to a sum of valine+leucine+isoleucine is in a range of 10-1000. Optionally, the valine, leucine and isoleucine are derived from dry milk, any stable dry product derived from milk and/or a mix thereof. Optionally, the following compounds are used as a source of Krebs cycle acid salts: Y-Me-Y.nH2O, where Me—divalent metal, from Ca, Mg, Zn group, Y—anion of an acid participating in Krebs cycle, and n=0-12.

Abstract: A mineral-vitamin complex for osteoporosis includes at least 92 mass % of the mineral-vitamin complex of amino acids and Krebs cycle acids and/or Krebs cycle acid salts, wherein the amino acids include glycine of between 1% and 80% of the mineral-vitamin complex, and wherein the Krebs cycle acids and/or Krebs cycle acid salts are up to 5 mass % of the mineral-vitamin complex; and valine, leucine and isoleucine such that a mass ratio of glycine to a sum of valine+leucine+isoleucine is in a range of 10-1000. Optionally, the valine, leucine and isoleucine are derived from dry milk, any stable dry product derived from milk and/or a mix thereof. Optionally, the following compounds are used as a source of Krebs cycle acid salts: Y-Me-Y.nH2O, where Me—divalent metal, from Ca, Mg, Zn group, Y—anion of an acid participating in Krebs cycle, and n=0-12.

Abstract: A method of obtaining a complex acidic salt of a divalent metal and a dicarboxylic acid includes heating water in a reactor; adding a dicarboxylic acid to the heated water; stirring the water to dissolve the dicarboxylic acid in the heated water to produce a solution or a suspension of the dicarboxylic acid in the heated water; adding MeO to the solution or the suspension, where Me is a divalent metal; continuing the stirring of the solution or suspension until formation of the complex acidic salt Me(AcH)2.nH2O begins, where Ac is an anion of the dicarboxylic acid, and n=0-8; cooling the complex acidic salt to below a temperature of crystallization; sedimenting the complex acidic salt; filtering the complex acidic salt to remove water from the complex acidic salt; and drying the complex acidic salt.

Abstract: A composition for regulating male sexual function includes at least one amino acid selected from a group consisting of L-Glutamic acid (glutamate), L-Arginine, glycine, L-aspartate, L-carnitine, L-tyrosine, L-glutamine and/or its pharmaceutically acceptable salt, such as any of monosodium-L-glutamate monogidrate, L-potassiumarginine, L,-ammoniumaspartate, L-arginine HCl, sodium-L-tyrasine, lithium aspartate, in the amount of 1-1000 mg, preferably 10-300 mg; at least one vitamin, in the amount of 1-500% of a daily recommended dose, preferably 10-200%; and at least one chelated compound of a formula: acid-Me-acid.nH2O, wherein Me is a metal chosen from any of Ca, Mg and Zn, wherein the acid is a dicarboxylic acid anion chosen from the group consisting of succinic acid, fumaric acid or aspartic acid, and wherein n=0-8. The composition increases testosterone level in a body of a male mammal.

Abstract: An improved process for preparing ammonium salts from fumaric or succinic acid, is described. The method consists of neutralizing the corresponding acid carbonate or ammonium bicarbonate at a molar stoichiometric or greater than the stoichiometric ratio of 4-5% in a saturated aqueous solution of the synthesized salt at a temperature not exceeding 40° C., followed by separation of the product and drying at a temperature not exceeding 70° C. After separation of the ammonium salts, the filtrate can be re-used. Isolation of the product is usually carried out by cooling the reaction mixture to a temperature of 15-18 C.°. The product comes out in almost crystalline form. Saturated aqueous solution of the synthesized salt is formed by the interaction of carbonate or ammonium bicarbonate with the appropriate acid at a temperature not exceeding 40° C. It is possible to obtain cleaner salt concentration weighing more than 99% and not yielding lower than 98%.

Abstract: A method for preparing succinic acid, including producing a modified palladium-containing catalyst by using an acid and liquid-phase hydrogenation of unsaturated acid compounds on the modified catalyst at an increased temperature and pressure; separating the catalyst from the succinic acid; wherein the modification of the catalyst is performed on a substrate having the palladium-containing catalyst delivered thereon, the delivery being performed in an oxygen-free atmosphere; the delivery being performed in an aqueous medium of succinic, maleic or fumaric acids and/or their mixtures at a Pd2+/acid ratio of 1:1-1:100; hydrogenating the liquid-phase unsaturated acid compounds selected from maleic, fumaric acids or their anhydrides or their mixtures; and crystallizing the succinic acid from an aqueous solution containing 0.001-0.01 wt. % succinic acid seed.

Abstract: An improved process for preparing ammonium salts from fumaric or succinic acid, is described. The method consists of neutralizing the corresponding acid carbonate or ammonium bicarbonate at a molar stoichiometric or greater than the stoichiometric ratio of 4-5% in a saturated aqueous solution of the synthesized salt at a temperature not exceeding 40° C., followed by separation of the product and drying at a temperature not exceeding 70° C. After separation of the ammonium salts, the filtrate can be re-used. Isolation of the product is usually carried out by cooling the reaction mixture to a temperature of 15-18C°. The product comes out in almost crystalline form. Saturated aqueous solution of the synthesized salt is formed by the interaction of carbonate or ammonium bicarbonate with the appropriate acid at a temperature not exceeding 40° C. It is possible to obtain cleaner salt concentration weighing more than 99% and not yielding lower than 98%.

Abstract: A method for preparing succinic acid, including producing a modified palladium-containing catalyst by using an acid and liquid-phase hydrogenation of unsaturated acid compounds on the modified catalyst at an increased temperature and pressure; separating the catalyst from the succinic acid; wherein the modification of the catalyst is performed on a substrate having the palladium-containing catalyst delivered thereon, the delivery being performed in an oxygen-free atmosphere; the delivery being performed in an aqueous medium of succinic, maleic or fumaric acids and/or their mixtures at a Pd2+/acid ratio of 1:1-1:100; hydrogenating the liquid-phase unsaturated acid compounds selected from maleic, fumaric acids or their anhydrides or their mixtures; and crystallizing the succinic acid from an aqueous solution containing 0.001-0.01 wt. % succinic acid seed.