Effect of different diafiltration process on the protein fractionation of skim milk by cross flow microfiltration

LWT ◽  
2021 ◽  
Vol 152 ◽  
pp. 112330
Author(s):  
Bo Song ◽  
Yumeng Zhang ◽  
Jing Lu ◽  
Xiaoyang Pang ◽  
Miaohong Wei ◽  
...  
2016 ◽  
Vol 99 (8) ◽  
pp. 6164-6179 ◽  
Author(s):  
Camilla Elise Jørgensen ◽  
Roger K. Abrahamsen ◽  
Elling-Olav Rukke ◽  
Anne-Grethe Johansen ◽  
Reidar B. Schüller ◽  
...  

2003 ◽  
Vol 38 (7) ◽  
pp. 1549-1560 ◽  
Author(s):  
Darko M. Krstic ◽  
Miodrag N. Tekic ◽  
Marijana D. Caric ◽  
Spasenija D. Milanovic
Keyword(s):  

1997 ◽  
Vol 7 (12) ◽  
pp. 849-861 ◽  
Author(s):  
A. Guerra ◽  
G. Jonsson ◽  
A. Rasmussen ◽  
E. Waagner Nielsen ◽  
D. Edelsten

2014 ◽  
Vol 470 ◽  
pp. 205-218 ◽  
Author(s):  
Y. Jin ◽  
N. Hengl ◽  
S. Baup ◽  
F. Pignon ◽  
N. Gondrexon ◽  
...  
Keyword(s):  

Foods ◽  
2021 ◽  
Vol 10 (5) ◽  
pp. 1090
Author(s):  
Simon Schiffer ◽  
Bello Teslim Adekunle ◽  
Andreas Matyssek ◽  
Martin Hartinger ◽  
Ulrich Kulozik

During skim milk microfiltration (nominal pore size of 0.1 µm) at 10 °C, the whey protein purity in the permeate is reduced by an enhanced serum casein permeation, primarily of β-casein. To decrease casein permeation, the possibility of a pre-heating step under pasteurization conditions before the filtration step was investigated, so as to shift the equilibrium from soluble serum casein monomers to impermeable micellar casein. Immediately after the pre-heating step, low temperature microfiltration at 10 °C was conducted before the casein monomers could diffuse into the serum. The hypothesis was that the dissociation of β-casein into the serum as a result of a decreasing temperature takes more time than the duration of the microfiltration process. It was found that pre-heating reduced the β-casein permeation during microfiltration without significantly affecting the flux and whey protein permeation, compared with a microfiltration at 10 °C without the pre-heating step. Furthermore, the addition of calcium (5 and 10 mM) not only reduced the casein permeation and thus increased the permeate purity, defined as a high whey protein-to-casein (g L−1/g L−1) ratio, but also decreased the filtration performance, possibly due to the structural alteration of the deposited casein micelle layer, rendering the deposit more compact and more retentive. Therefore, the possible combination of the addition of calcium and pre-heating prior to microfiltration was also investigated in order to evidence the potential increase of whey protein (WP) purity in the permeate in the case of Ca2+ addition prior to microfiltration. This study shows that pre-heating very close to low temperature microfiltration results in an increased purity of the whey protein fraction obtained in the permeate.


1996 ◽  
Vol 6 (1) ◽  
pp. 105-111 ◽  
Author(s):  
Michel Pouliot ◽  
Yves Pouliot ◽  
Michel Britten
Keyword(s):  

1997 ◽  
Vol 7 (4) ◽  
pp. 237-242 ◽  
Author(s):  
Gunilla Samuelsson ◽  
Petr Dejmek ◽  
Gun Trägårdh ◽  
Marie Paulsson

Foods ◽  
2019 ◽  
Vol 8 (6) ◽  
pp. 180 ◽  
Author(s):  
Martin Hartinger ◽  
Hans-Jürgen Heidebrecht ◽  
Simon Schiffer ◽  
Joseph Dumpler ◽  
Ulrich Kulozik

Protein fractionation by means of microfiltration (MF) is significantly affected by fouling, especially when spiral-wound membranes (SWMs) are used. We investigated the influence of the mode of transmembrane pressure (ΔpTM) increase to target level and the deposit layer pressure history on the filtration performance during skim milk MF at temperatures of 10 °C and 50 °C. Two filtration protocols were established: No. 1: ΔpTM was set directly to various target values. No. 2: Starting from a low ΔpTM, we increased and subsequently decreased ΔpTM stepwise. The comparison of both protocols tested the effect of the mode of ΔpTM increase to target level. The latter protocol alone tested the effect of the deposit layer history with regard to the ΔpTM. As expected, flux and protein permeation were both found to be functions of the ΔpTM. Further, both measures were independent of the filtration protocol as long as ΔpTM was held at a constant level or, as part of protocol No. 2, ΔpTM was increased. Thus, we can state that the mode of ΔpTM increase to target level does not affect filtration performance in SWM. We found that after completion of a full cycle of stepping ΔpTM up from 0.5 bar to 3.0 bar and back down, flux and deposit layer resistance were not affected by the deposit layer history at 10 °C, but they were at 50 °C. Protein permeation, however, was lower for both 10 °C and 50 °C, when the ΔpTM cycle was completed. The processing history had a significant impact on filtration performance due to remaining structural compression effects in the deposited layer, which occur most notably at higher temperatures. Furthermore, temperatures of 50 °C lead to deposit layer aging, which is probably due to an enhanced crosslinking of particles in the deposit layer. Apart from that, we could show that fouling resistance does not directly correlate with protein permeation during skim milk MF using SWM.


Membranes ◽  
2020 ◽  
Vol 10 (11) ◽  
pp. 326
Author(s):  
Simon Schiffer ◽  
Ulrich Kulozik

This study determined the maximum possible filtration time per filtration cycle and the cumulated number of operational hours per year as a function of the processing temperature during milk protein fractionation by 0.1 µm microfiltration (MF) of pasteurized skim milk. The main stopping criteria were the microbial count (max. 105 cfu/mL) and the slope of the pH change as a function of filtration time. A membrane system in a feed and bleed configuration with partial recirculation of the retentate was installed, resembling an industrial plants’ operational mode. Filtration temperatures of 10, 14, 16, 20, and 55 °C were investigated to determine the flux, pH, and bacterial count. While the processing time was limited to 420 min at a 55 °C filtration temperature, it could exceed 1440 min at 10 °C. These data can help to minimize the use of cleaning agents or mixing phase losses by reducing the frequency of cleaning cycles, thus maximizing the active production time and reducing the environmental impact.


Desalination ◽  
2004 ◽  
Vol 163 (1-3) ◽  
pp. 297-309 ◽  
Author(s):  
Darko M Krstićś ◽  
Miodrag N Tekić ◽  
Marijana D Carić ◽  
Spasenija D Milanović
Keyword(s):  

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