首页> 外文OA文献 >ANALYZING THE EFFECT OF CROSS FLOW VELOCITY, UNIFORM TRANS MEMBRANE PRESSURE AND PH ON PERMEATE FLUX, RETENTATE COMPOSITION AND ENERGY CONSUMPTION DURING CROSS FLOW MICROFILTRATION OF SKIM MILK
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ANALYZING THE EFFECT OF CROSS FLOW VELOCITY, UNIFORM TRANS MEMBRANE PRESSURE AND PH ON PERMEATE FLUX, RETENTATE COMPOSITION AND ENERGY CONSUMPTION DURING CROSS FLOW MICROFILTRATION OF SKIM MILK

机译:分析横向流动速度,均匀的跨膜压力和PH对SKIM牛奶的横向流微滤过程中渗透通量,渗余组成和能量消耗的影响

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摘要

Pasteurized skim milk at pH 6.50 and 6.00 was microfiltered at 50oC using 0.2-mm membranes. A factorial design of three cross flow velocities (CFV) of 5.3, 5.8, 6.3 ms-1 and three uniform trans membrane pressures (UTMP) of 68.9, 103.4, 137.9 kPa was utilized. High CFV combined with high TMP required the shortest time (up to 40%) to achieve a concentration factor (CF) of 8-10x. Starting flux was 20 to 50% higher at pH 6.50 when compared to pH 6.00 due to solubilization of micellar calcium and severe fouling at lower pH. Higher flux was always obtained by using the combination of high CFV and high UTMP, which results in high shear and 33% reduction in gel layer (CG) with back transport of rejected molecules into the retentate stream due to better (almost double) mass transfer coefficient (kc). Higher CFV also reduced whey protein retention by 33%. Cross flow microfiltration (CFM) at lower pH (6.00) reduced calcium retention and lowered calcium to true protein ratio by 50% at 10x, compared to 8x retentate at pH 6.50, though 10x retentate had 20% higher casein concentration. Higher UTMP helped maintain high flux and thus shorten the run time up to a CF of 6-7x, but resulted in severe fouling and a steep decline in flux and increased whey protein retention as the process was continued to higher concentrations (8-10x). Overall energy consumption was always lower due to shorter CFM process when skim milk was microfiltered to 8x at higher CFV and higher UTMP.
机译:将pH为6.50和6.00的巴氏杀菌脱脂奶在50°C下使用0.2 mm膜微过滤。使用了5.3、5.8、6.3 ms-1的三个错流速度(CFV)和68.9、103.4、137.9 kPa的三个均匀跨膜压力(UTMP)的析因设计。高CFV与高TMP相结合需要最短的时间(最多40%)才能达到8-10倍的浓缩系数(CF)。与pH 6.00相比,在pH 6.50时起始通量高出20%至50%,这是由于胶束钙的溶解和在较低pH下的严重结垢。通过将高CFV和高UTMP结合使用,始终可获得更高的通量,这导致高剪切力和凝胶层(CG)减少33%,并且由于更好的(几乎是两倍的)质量转移而将被拒绝的分子向后输送到渗余物流中系数(kc)。较高的CFV还可将乳清蛋白保留量降低33%。与pH为6.50时的8x截留物相比,在较低pH(6.00)下的错流微滤(CFM)在10x时减少了钙保留,并使钙与真蛋白的比率降低了50%,尽管10x截留物的酪蛋白浓度提高了20%。较高的UTMP有助于保持较高的通量,因此可将运行时间缩短至6-7倍的CF,但随着该过程继续进行至较高浓度(8-10x),会导致严重的结垢,通量急剧下降和乳清蛋白保留率提高。 。由于脱脂牛奶在较高CFV和较高UTMP的条件下被微滤至8倍,因此总的能耗始终较低,这是因为CFM过程更短。

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    Singh Mayank;

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  • 年度 2007
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