Suitability of nitrogen fractions determination to assess serum protein separation efficiency from a mass balance perspective during microfiltration of skim milk

2022 ◽  
pp. 105319
Author(s):  
Surabhi Subhir ◽  
Paul L.H. McSweeney ◽  
Mark A. Fenelon ◽  
Jonathan B. Magan ◽  
John T. Tobin
2013 ◽  
Vol 96 (3) ◽  
pp. 1387-1400 ◽  
Author(s):  
Rachel E. Campbell ◽  
Michael C. Adams ◽  
MaryAnne Drake ◽  
David M. Barbano

2020 ◽  
Vol 64 (3) ◽  
pp. 357-363 ◽  
Author(s):  
Mihály Zakar ◽  
Dániel Imre Farkas ◽  
Erika Hanczné Lakatos ◽  
Gábor Keszthelyi-Szabó ◽  
Zsuzsanna László

This study aimed to investigate the effect of ozone and Fenton-reaction as a pre-treatment before ultrafiltration of model dairy waste waters containing sodium caseinate. Filtration resistances and pollutant retentions were determined and compared. It was found, that both pre-treatment increased the retention, achieving almost 100 % pollutant elimination efficiency after short term pre-oxidation. The effect of Fe-ion concentration on Fenton pretreatment efficiency also was examined, and it was found that higher concentration resulted in decreased filtration resistances, revealing that coagulation-flocculation effect of reactants has dominant role in the protein separation efficiency. The presence of lactose also affects the pollutant removal efficiency, it promotes fouling in presence of Fenton reagents.


2011 ◽  
Vol 32 (20) ◽  
pp. 2904-2910 ◽  
Author(s):  
Tao Zhang ◽  
Qingqing Gai ◽  
Feng Qu ◽  
Yukui Zhang

2015 ◽  
Vol 98 (11) ◽  
pp. 7483-7497 ◽  
Author(s):  
Michael C. Adams ◽  
Emily E. Hurt ◽  
David M. Barbano

Foods ◽  
2018 ◽  
Vol 7 (9) ◽  
pp. 134 ◽  
Author(s):  
Abhiram Arunkumar ◽  
Mark Etzel

In this work, milk protein concentrate (MPC) was made using wide-pore negatively charged ultrafiltration membranes. The charged membranes were used for a six-fold volume concentration of skim milk and subsequent diafiltration to mimic the industrial MPC process. The charged 100 kDa membranes had at least a four-fold higher permeate flux at the same protein recovery as unmodified 30 kDa membranes, which are currently used in the dairy industry to make MPC. By placing a negative charge on the surface of an ultrafiltration membrane, the negatively charged proteins were rejected by electrostatic repulsion and not simply size-based sieving. Mass balance models of concentration and diafiltration were developed and the calculations matched the experimental observations. This is the first study to use wide-pore charged tangential-flow membranes for MPC manufacturing. Additionally, a unique mass balance model was applied, which accurately predicted experimental results.


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