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    • 4. 发明授权
    • Process for continuously producing sugar
    • 连续生产糖的工艺
    • US4050953A
    • 1977-09-27
    • US698080
    • 1976-06-21
    • Norio NakazatoKosai HiratsukaTokinobu Furukawa
    • Norio NakazatoKosai HiratsukaTokinobu Furukawa
    • C13B25/00C13B30/02C13F1/02C13G1/00
    • C13B30/022
    • In a continuous sugar evaporator-crystallizer having a plurality of evaporating-crystallizing vessels as stages, each evaporating-crystallizing stages being communicated one to another in series and being provided with a means for feeding an aqueous sugar solution, a heating means and a means for withdrawing generated steam, by feeding an aqueous sugar solution to each evaporating-crystallizing stage, heating the aqueous sugar solution in each evaporating-crystallizing stage, thereby evaporating water off the aqueous sugar solution and crystallizing sugar crystals, and withdrawing the generated steam from each of the stages, while feeding seed sugar crystals to the first evaporating-crystallizing stage and withdrawing the resulting sugar crystal slurry from the last evaporating-crystallizing stage, sugar crystals of high quality is obtained in the slurry with an effective suppression of occurrence of conglomerated sugar grains by providing sugar crystal distances of 0.26 to 0.59 mm in the solution in the first evaporating-crystallizing stage, and feeding the aqueous sugar solution to each of intermediate evaporating-crystallizing stages excluding the first and last evaporating-crystallizing stages at a substantially equal feed rate, and making the feed rate of the aqueous sugar solution to the first evaporating-crystallizing stage at least 1.5 times the feed rate to each of the intermediate evaporating-crystallizing stages.
    • 在具有多个蒸发结晶容器作为阶段的连续糖蒸发器结晶器中,每个蒸发结晶阶段彼此串联连通,并且设置有用于供给糖水溶液的装置,加热装置和用于 通过向每个蒸发结晶阶段加入糖水溶液来提取产生的蒸汽,在每个蒸发结晶阶段加热糖水溶液,从而将水从糖水溶液中蒸发出来并使糖结晶结晶,并从每个蒸发结晶阶段中抽出所产生的蒸汽 在将第一蒸发结晶阶段的种子糖晶体进料并从最后的蒸发结晶阶段中取出所得糖晶体浆料的同时,在浆料中获得高质量的糖晶体,有效抑制聚集糖粒的发生 通过提供0.26至0.59毫米的糖晶距离 在第一蒸发结晶阶段中的溶液,并且将糖水溶液以大致相等的进料速率将除去第一蒸发结晶阶段和最后一个蒸发结晶阶段的中间蒸发结晶阶段进料到每个中间蒸发结晶阶段,并使糖水溶液的进料速率 到第一蒸发结晶阶段为每个中间蒸发结晶阶段的进料速率的至少1.5倍。