发明名称 Fremgangsmåde til forøgelse af udbytte i fremstillingen af lactose (III)
摘要 Improving (M1) yield during production of crystalline alpha lactose involves: aqueous lactose solution is adjusted to 82-67[deg] C, then cooled down to 20-30[deg] C for 0-5 hours, then heated to 30-45[deg] C for 0-5 hours, then cooled to 10[deg] C. Subsequently, the precipitated first alpha lactose crystals are separated from mother liquor. Carbohydrate compound is added to mother liquor such that solubility product of residual lactose that is still soluble is exceeded, and second precipitated alpha lactose crystals are separated from mother liquor and dried. The first and second crystals are combined. Improving (M1) the yield during the production of crystalline alpha lactose involves: a) an aqueous lactose solution is adjusted to temperature of 62-67[deg] C, b) the solution is then cooled down to 20-30[deg] C, c) the solution is held at this temperature for 0-5 hours, d) the solution is subsequently heated to 30-45[deg] C, e) the solution is hold at this temperature for 0-5 hours, f) the solution is then cooled down to 10[deg] C, and g) subsequently, the precipitated first amount of alpha lactose crystals is separated from the mother liquor, h) amount of carbohydrate compound is added to the mother liquor such that the solubility product of the residual amount of lactose that is still soluble is exceeded, i) the second amount of precipitated alpha lactose crystals is separated from the mother liquor, dried, and j) both amounts of alpha lactose crystals are combined. An independent claim is included for production (M2) of crystalline alpha lactose involving a1) whey is subjected to separation process in which protein-rich and lactose-rich fraction is obtained, b1) the lactose-rich fraction is (optionally after concentrating the main flow) subjected to demineralization in which slowly soluble salts are precipitated, c1) the demineralized residue is cooled down, optionally after further concentration, until lactose precipitates in crystalline form, d1) the lactose crystals are separated from the mother liquor and evaporated, and following method (M1).
申请公布号 DK2767596(T3) 申请公布日期 2016.05.23
申请号 DK20130155557T 申请日期 2013.02.16
申请人 DMK DEUTSCHES MILCHKONTOR GMBH 发明人 DÖRING, SVEN-RAINER
分类号 C07H3/04;C07H1/00;C13K5/00 主分类号 C07H3/04
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