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Cleaning-in-place coupled with membrane regeneration for re-using caustic soda solutions

机译:就地清洗与膜再生相结合,可重复使用苛性钠溶液

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Industrial use of soda cleaning-in-place(CIP)solution in dairy plants yields a modification of the composition of the cleaning solution(suspended solids,SS;chemical oxygen demand,COD;surface tension,gamma).The increase of SS and decrease of gamma generate decreased and enhanced cleaning performances,respectively.The paper aims at determining the more appropriate regeneration operation(filtration,centrifugation)by modelling and simulating coupled regeneration CIP process on industrial assumptions and at designing and sizing the coupled CIP process according to the required physicochemical characteristics(SS,gamma,COD)and cost.The coupling of re-use CIP with membrane regeneration(microfiltration,ultrafiltration and nanofiltration)makes it possible to control the functional characteristics of the solution(SS and y maintained under critical values)as opposed to centrifugation and decantation.The discontinuous mode is to be preferred regarding the caustic solution composition and functionality,but the continuous mode is simpler to use at a lower capital cost.The microfiltration operation seems to be the more appropriate operation:surfactants are only slightly retained and costs are reduced;however COD content of re-used solutions are relatively high compared to values obtained with ultrafiltration and nanofiltration.In case of very high levels of COD in re-used caustic soda solutions,cleaning efficiency and kinetics should be further investigated.
机译:在乳制品厂中工业使用苏打水就地清洗(CIP)溶液可以改变清洗溶液的成分(悬浮固体,SS,化学需氧量,COD,表面张力,γ).SS的增加和减少本文旨在通过根据工业假设对耦合再生CIP工艺进行建模和仿真,并根据需要设计和确定耦合CIP工艺的规模,从而确定更合适的再生操作(过滤,离心)。物理化学特性(SS,γ,COD)和成本。重复使用的CIP与膜再生(微滤,超滤和纳滤)的耦合使控制溶液的功能特性(将SS和y保持在临界值)成为可能。相对于离心和倾析,就苛性溶液的组成和功能而言,不连续模式是首选的优点,但连续模式更易于使用,且投资成本更低。微滤操作似乎是更合适的操作:表面活性剂仅保留很少,成本降低;但是与之相比,重用溶液的COD含量相对较高如果重复使用的苛性钠溶液中的COD含量很高,则应进一步研究清洁效率和动力学。

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