2005
DOI: 10.1016/j.desal.2004.12.027
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Optimisation of ultrafiltration of a highly viscous protein solution using spiral-wound modules

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Cited by 11 publications
(7 citation statements)
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“…Besides, use was made of two commercial detergents, P3-Ultrasil 67 and P3-Ultrasil 69 (Henkel, Germany). The former consists of two main cleaning components: alkyl amine oxide (15-30%) and proteolytic enzyme (<5%), while the latter contains phosphonates (5-15%) and salts of organic acids (5-15%) (Lipnizki et al, 2005). The cleaning solutions consisted of the following mixtures of the two detergents (in % w/w): 0.25 P3-Ultrasil 67 + 0.4 P3-Ultrasil 69, 0.5 P3-Ultrasil 67 + 0.8 P3-Ultrasil 69, and 0.75 P3-Ultrasil 67 + 1.2 P3-Ultrasil 69.…”
Section: Cleaning Agentsmentioning
confidence: 99%
“…Besides, use was made of two commercial detergents, P3-Ultrasil 67 and P3-Ultrasil 69 (Henkel, Germany). The former consists of two main cleaning components: alkyl amine oxide (15-30%) and proteolytic enzyme (<5%), while the latter contains phosphonates (5-15%) and salts of organic acids (5-15%) (Lipnizki et al, 2005). The cleaning solutions consisted of the following mixtures of the two detergents (in % w/w): 0.25 P3-Ultrasil 67 + 0.4 P3-Ultrasil 69, 0.5 P3-Ultrasil 67 + 0.8 P3-Ultrasil 69, and 0.75 P3-Ultrasil 67 + 1.2 P3-Ultrasil 69.…”
Section: Cleaning Agentsmentioning
confidence: 99%
“…Also, commercially available detergents P3-ultrasil 67 and P3-ultrasil 69 (Henkel, Germany) were used. The former consists of two main cleaning components: alkyl amine oxide (15-30%w/w) and proteolytic enzyme (<5%w/w), while the latter contains phosphonates (5-15%w/w) and salts of organic acids (5-15%w/w) (Lipnizki et al, 2005). The enzymatic cleaning solutions were prepared by mixing detergents as follows: 0.8%w/ w P3-ultrasil 69 + 0.5%w/w P3-ultrasil 67 and 1.2%w/w P3-ultrasil 69 + 0.75%w/w P3-ultrasil 67.…”
Section: Cleaning Agentsmentioning
confidence: 99%
“…Efficiency of such a process is greatly affected by decrease in flux during filtration due to formation of deposit layer at the membrane surface and in the pores. Although investigations are mostly focused on the fouling, equally important are investigations on cleaning of membranes fouled with milk or whey proteins (Bartlett et al, 1995;Muños-Aguado et al, 1996;Bird and Bartlett, 2002;Blanpain-Avet et al, 2004;D'Souza and Mawson, 2005;Argüello et al, 2005;Lipnizki et al, 2005;Bansal et al, 2006;Nigam et al, 2008). As cleaning agents, alkali solutions were used (Bartlett et al, 1995;Bird and Bartlett, 2002;Blanpain-Avet et al, 2004;Argüello et al, 2005;Bansal et al, 2006;Nigam et al, 2008).…”
Section: Introductionmentioning
confidence: 99%
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“…However, SWM are not capable of processing highly viscous fluids owing to the generation of high pressure drops within the module at high retentate viscosities (Akoum, Jaffrin, & Ding, 2005;Lipnizki, Casani, & Jonsson, 2005). As the enrichment of total milk protein is accompanied by a strong rise in viscosity (Aaltonen, 2012;Solanki & Rizvi, 2001) the employment of SWMs for this purpose is limited.…”
Section: Introductionmentioning
confidence: 97%