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Process for regeneration of ion exchange resin used for sugar decolorization

机译:用于糖脱色的离子交换树脂的再生方法

摘要

Process for regeneration of ion-exchange resins, used in sugar decolorization, using a sucrose solution with sodium or calcium chloride, or another chloride, namely potassium or a mixture of those chlorides, alkalinised with calcium hydroxide. The regeneration of the resin is made with a flow between 1 to 3 cubic meters of a regenerating solution by a cubic meter of resin/hour and a temperature between 40 DEG to 70 DEG centigrade. The sucrose solution used in this resin regeneration process contains between 30 to 600 g of sucrose per liter of solution; calcium hydroxide between 1 to 40 g of CaO per liter of solution; and calcium or sodium chloride, or another chloride, namely the one of potassium, or a mixture of these compounds, in such a quantity that chloride ion concentration is between 3 to 30 g per liter of solution. This regenerating solution is passed through the resin in a quantity between 2 to 4 cubic meters per cubic meter of resin. The effluent from this resin regeneration process, containing sucrose and a low content of chloride ions, can be used, directly or after a chemical or physical treatment, in sugar production or sugar refining processes.
机译:用于蔗糖脱色的离子交换树脂的再生方法,该方法是使用蔗糖溶液与氯化钠或氯化钙,或另一种氯化物,即钾或这些氯化物的混合物,用氢氧化钙碱化。树脂的再生是通过在再生溶液中1至3立方米/小时,树脂立方米/小时,温度在40-70℃之间进行的。在该树脂再生过程中使用的蔗糖溶液每升溶液中含有30至600克蔗糖。每升溶液中含有1至40克CaO之间的氢氧化钙;氯化钙或氯化钠,或另一种氯化物,即钾中的一种,或这些化合物的混合物,其数量应使每升溶液中氯离子的浓度在3至30克之间。使该再生溶液以每立方米树脂2至4立方米的量通过树脂。该树脂再生过程中产生的含有蔗糖和少量氯离子的废水可以直接用于糖生产或糖精制过程,也可以在经过化学或物理处理后使用。

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