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The method of separation of mash nonadiabatic distillation

机译:麦芽非绝热蒸馏的分离方法

摘要

FIELD: food industry; chemistry; medicine; pharmaceuticals.SUBSTANCE: invention can be used in the food, chemical, pharmaceutical and other industries. Method comprises separation of a mixture into a low-boiling fraction and a high-boiling fraction with counter-current contact of the steam stream fed for rectification with a liquid wort film flowing along a heat and mass exchange surface. On the reverse side of the heat and mass exchange surface, additional supply of heat flux is carried out to form evaporation steam. Temperature in the flowing film at the input section of the heat and mass exchange surface is maintained in the range of 55–80 °C. Ratio of the heat and mass exchange surface Sof the input section and the total heat and mass exchange surface S is S/S = 0.1–0.3. And the ratio of the flow rate G of steam fed for rectification to the flow rate Gd of evaporation steam formed by additional supply of heat flux from the reverse side of the heat and mass exchange surface is kept equal to G/G= 1–3.EFFECT: invention enables to intensify the wort separation process through partial condensation of the rising vapours of the mixture in the upper part of the film column, as well as through evaporation of the flowing wort film with rising vapours and exhaustion from the wort film of components by supplying additional heat flux.1 cl, 3 dwg
机译:领域:食品工业;化学;药物;药物:发明可用于食品,化学,制药和其他行业。该方法包括将混合物分离成低沸点馏分和高沸点馏分,并使进料进行精馏的蒸汽流与沿热和质交换表面流动的麦芽汁膜逆流接触。在热质交换表面的反面,额外提供热通量以形成蒸发蒸汽。传热和质量交换表面输入部分的流动膜温度保持在55-80°C之间。输入部分的热质交换表面S与总热质交换表面S之比为S / S = 0.1-0.3。整流送入的蒸汽流量G与由从热质交换表面反面额外提供的热通量形成的蒸发蒸汽流量Gd之比保持等于G / G = 1-3效果:本发明能够通过在膜塔上部的混合物中上升的蒸气的部分冷凝,以及通过上升的蒸气对流动的麦芽汁膜的蒸发以及从麦芽汁的麦汁膜中的排出而增强麦芽汁分离过程。通过提供额外的热通量来组成组件.1 cl,3 dwg

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