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Nanofiltration for the recovery of caustic cleaning-in-place solutions: robustness towards large variations of composition

机译:纳米过滤可用于苛性碱就地清洗溶液的回收:对各种成分的适应性强

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In the dairy industry re-use and multi-use cleaning-in-place (CIP) systems are operated by circulating chemicals and water without taking the equipment apart. The solutions, which become polluted due to the removal of fouling compounds, are drained periodically when they are considered to be too polluted. This work shows the large variations in composition (pollution, surface tension, etc) of the industrial caustic solutions coming from milk standardization and pasteurization plant CIP throughout their life time (7 days) and from 1 week to another. The work is also intended to show how nanofiltration (1 kg mol~(-1) molecular weight cut-off) was robust and performed well, with good recovery of caustic solutions, even when faced with large variations of solutions composition: high caustic yield, permeation flux (J) in the range 42-110 l h~(-1) m~(-2), average chemical oxygen demand (COD) reduction equal to 0.58 and low surface tension change. Equations have been established for the prediction of J as a function of initial membrane hydraulic resistance (R_m) caustic concentration, volume reduction ratio (VRR) and initial soluble COD. When VRR increased, both J and pollution retention decreased despite the increase in irreversible fouling induced by the increase of soluble pollution concentration in retentate . The higher the initial soluble COD, the sharper the decrease in J vs. VRR. Since irreversible fouling was usually small (0.1-3.4 x 10~(13) m~(-1), that is to say of the same order of magnitude as R_m), the membrane cleaning could be efficiently performed by using single phase sodium hypochlorite alternately with a more expensive acid-base cleaning sequence. The obtained permeate was a clear regenerated cleaning solution with low soluble COD (0.2-3.5 g/1) and surface tension (56-30 mJ m~(-2)) which could be successfully exploited owing to its cleaning potential.
机译:在乳制品行业,重复使用和多次使用的就地清洁(CIP)系统通过循环化学品和水进行操作,而无需拆开设备。由于去除了污垢化合物而被污染的溶液,在被认为过于污染时,应定期排干。这项工作表明,牛奶标准化和巴氏灭菌厂CIP在其整个生命周期(7天)以及从1周到另一周之间,工业苛性碱溶液的成分(污染,表面张力等)差异很大。该工作还旨在显示纳米过滤(截留分子量为1 kg mol〜(-1)的分子筛)如何稳健且表现良好,即使苛性溶液的组成变化很大,也能很好地回收苛性溶液:苛性产率高,渗透通量(J)在42-110 lh〜(-1)m〜(-2)范围内,平均化学需氧量(COD)降低等于0.58和低表面张力变化。已经建立了用于预测J的方程,该方程是初始膜水力阻力(R_m)苛性碱浓度,体积减少率(VRR)和初始可溶性COD的函数。当VRR增加时,尽管滞留物中可溶污染浓度的增加导致不可逆结垢的增加,但J和污染保持力均降低。初始可溶COD越高,J与VRR的下降幅度越大。由于不可逆结垢通常很小(0.1-3.4 x 10〜(13)m〜(-1),也就是说,与R_m的数量级相同),因此可以使用单相次氯酸钠有效地进行膜清洗或者使用更昂贵的酸碱清洗程序。所获得的渗透液是一种透明的再生清洗液,具有低可溶性COD(0.2-3.5 g / 1)和表面张力(56-30 mJ m〜(-2)),由于其清洗潜力而可以成功开发。

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