http://rdf.ncbi.nlm.nih.gov/pubchem/patent/DE-3882188-D1

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filingDate 1988-04-13-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 1993-08-12-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_8dc5afb9e20ccd0137297465862d5df2
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publicationDate 1993-08-12-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber DE-3882188-D1
titleOfInvention TOTAL WHITE DEGRADATION PRODUCT.
abstract Protein hydrolysates (I) obtd. by hydrolysing proteinaceous materials with mineral acid are claimed, where (I) are free of inorganic salts and comprise 1-99 wt.% amino acids and 1-99 wt.% oligopeptides. (I) have a cysteine content of 2-20%. (I) are produced by (a) hydrolysing the proteinaceous material, esp. keratin, wheat gluten or soya protein, with a mineral acid, esp. HCl; (b) opt. evaporating off the acid, (c) electrolytically neutralising and reducing the hydrolysate in a cell contg. a diaphragm; and (d) opt. evaporating the prod. Step (c) is pref. effected at 20-60 deg.C with a current density of 0.01-0.2 A/cm2 and a voltage of 6-30 V. The cathode compartment contains 30-50% hydrolysate solids and the anode compartment contains a 4-10% mineral acid soln. The cathode material is Hg, Cu, Pb, Fe or Sn and the anode material is carbon or Pt. The diaphragm is a membrane with a pore size of 0.5-10 microns. Electrolysis is continued until the pH is 0.5-4.5. Alternatively, the proteinaceous material is merely dissolved in the mineral acid, and hydrolysis is effected enzymatically after electrolytic neutralisation.
priorityDate 1987-04-15-04:00^^<http://www.w3.org/2001/XMLSchema#date>
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Total number of triples: 27.