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A process efficiency assessment of serum protein removal from milk using ceramic graded permeability microfiltration membrane

机译:陶瓷梯度渗透微滤膜从牛奶中去除血清蛋白的过程效率评估

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摘要

Microfiltration (MF) is a well-known process that can be used in the dairy industry to separate caseins from serum proteins (SP) in skim milk using membranes with a pore diameter of 0.1 μm. Graded permeability ceramic membranes have been studied widely as means of improving milk fractionation by overcoming problems encountered with other MF membranes. The ideal operating parameters for process efficiency in terms of membrane selectivity, permeate flux, casein loss, SP transmission, energy consumption, and dilution with water remain to be determined for this membrane. Our objective was to evaluate the effects of transmem-brane pressure (TMP), volumetric concentration factor (VCF), and diafiltration on overall process efficiency. Skim milk was processed using a pilot-scale MF system equipped with 0.72-m~2 graded permeability membranes with a pore size of 0.1 μm. In the first experiment, in full recycle mode, TMP was set at 124, 152, 179, or 207 kPa by adjusting the permeate pressure at the outlet. Whereas TMP had no significant effect on permeate and retentate composition, 152 kPa was found to be optimal for SP removal during concentration and concentration or diafiltration experiments. When VCF was increased to 3×, SP rejection coefficient increased along with energy consumption and total casein loss, whereas SP removal rate decreased. Diafiltering twice allowed an increase in total SP removal but resulted in a substantial increase in energy consumption and casein loss. It also reduced the SP removal rate by diluting permeate. The membrane surface area required for producing cheese milk by blending whole milk, cream, and MF retentate (at different VCF) was estimated for different cheese milk casein concentrations. For a given casein concentration, the same quantity of permeate and SP would be produced, but less membrane surface area would be needed at a lower retentate VCF. Microfiltration has great potential as a process of adding value to conventional cheesemaking processes, but its cost-effectiveness at a large scale remains to be demonstrated.
机译:微滤(MF)是众所周知的方法,可用于乳品行业,使用孔径为0.1μm的膜将酪蛋白与脱脂乳中的血清蛋白(SP)分离。渐变渗透性陶瓷膜已被广泛研究,作为通过克服其他MF膜遇到的问题来改善牛奶分馏的方法。关于该膜的工艺效率的理想操作参数,如膜选择性,渗透通量,酪蛋白损失,SP传输,能量消耗和用水稀释,尚待确定。我们的目的是评估跨膜压(TMP),体积浓缩系数(VCF)和渗滤对整个过程效率的影响。脱脂奶使用配有0.72-m〜2梯度渗透膜且孔径为0.1μm的中试MF系统进行处理。在第一个实验中,在完全循环模式下,通过调节出口的渗透压力将TMP设置为124、152、179或207 kPa。尽管TMP对渗透物和截留物的组成没有显着影响,但发现在浓缩和浓缩或渗滤实验中152 kPa最适合去除SP。当VCF增加到3倍时,SP截留系数随能量消耗和总酪蛋白损失的增加而增加,而SP去除率则下降。两次渗滤可以增加总SP去除量,但会导致能耗和酪蛋白损失大幅增加。通过稀释渗透液还降低了SP去除率。对于不同的干酪乳酪蛋白浓度,估计了通过混合全脂牛奶,奶油和MF截留液(在不同的VCF下)来生产干酪乳所需的膜表面积。对于给定的酪蛋白浓度,将产生相同量的渗透物和SP,但在较低的截留物VCF下将需要较少的膜表面积。微滤具有巨大的潜力,可以为传统的奶酪制作工艺增值,但其大规模的成本效益仍有待证明。

著录项

  • 来源
    《Journal of dairy science》 |2016年第7期|5230-5243|共14页
  • 作者单位

    STELA Dairy Research Center, Institute of Nutrition and Functional Foods (INAF), Department of Food Sciences, Universite Laval, Quebec, QC, Canada, G1V 0A6;

    STELA Dairy Research Center, Institute of Nutrition and Functional Foods (INAF), Department of Food Sciences, Universite Laval, Quebec, QC, Canada, G1V 0A6;

    STELA Dairy Research Center, Institute of Nutrition and Functional Foods (INAF), Department of Food Sciences, Universite Laval, Quebec, QC, Canada, G1V 0A6 ,Food Research and Development Centre (FRDC), Agriculture and Agri-Food Canada, St-Hyacinthe, QC, Canada, J2S 8E3;

    STELA Dairy Research Center, Institute of Nutrition and Functional Foods (INAF), Department of Food Sciences, Universite Laval, Quebec, QC, Canada, G1V 0A6;

  • 收录信息 美国《科学引文索引》(SCI);美国《生物学医学文摘》(MEDLINE);美国《化学文摘》(CA);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    microfiltration; graded permeability membrane; process efficiency; energy consumption; mass balance;

    机译:微滤梯度渗透膜工艺效率;能源消耗;质量平衡;
  • 入库时间 2022-08-17 23:23:20

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