Kinetics of ultrafiltration cheese whey


Cite item

Full Text

Open Access Open Access
Restricted Access Access granted
Restricted Access Subscription Access

Abstract

The results of experimental studies of the process cheese whey ultrafiltration using ceramic membranes TAMI Deutschland GmbH with the separating of 100 kDa (pore size of 0,01 microns). As the object of research is the cheese whey, obtained under the conditions of Dairy Plant «Voronezh» in the production of soft cheese with a separator «Westfalia». Basic physical and chemical parameters: the mass fraction of solids of 5,4%, protein - 0,6%, oil - 0,05%, titratable acidity -62 °T. Analyzing the dependence of the specific cheese whey ultrafiltration rate of the duration of the process after two hours, can show a decrease in permeability of 18,5 times. When using direct periodic flushing with pressure relief, achieved growth of the specific rate of 1,4 times compared to the process when there were no measures to create hydrodynamic instabilities at the interface. The frequency of direct leaching was every 12 minutes, the duration - 30 seconds. Increasing the operating pressure of the ultrafiltration over 0,35 MPa not resulted in a significant increase in permeability. The temperature rise of the serum over 50-55 °С lead to protein denaturation and ultrafiltration at temperatures 10-15 °C are not effective due to increased viscosity, which causes a decrease in the rate of passage of whey permeate through the membrane. Therefore, we concluded that the temperature of the cheese whey ultrafiltration when it should be in the range 45-48 °С. When the values of the tangential velocity of 2,5 3,0 m/s, there was the removal of the part of the protein deposits, among the particles which have not yet formed strong ties due to the strength of intermolecular inter-ac-interaction. A further increase in the tangential velocity is not rational, because it led to an increase in hydraulic losses, the energy costs for circulation serum. Selectivity achieved for the membrane protein is 9495% at a concentration of 2,8-3,0.

Full Text

Restricted Access

References

  1. Мулдер М. Введение в мембранную технологию. - М.: Мир, 1999.
  2. Пономарёв А.Н., Ключников А.И., Полянский К.К. Основные направления мембранных технологий при переработке молочной продукции: монография. -Воронеж: Изд-во «Истоки», 2011. - 356 с.
  3. Пономарёв А.Н., Полянский К.К., Ключников А.И. Мембранные системы и инжиниринг при переработке молочного сырья // Молочная промышленность. 2012. № 4. С. 71-72.
  4. Ключников А.И., Пономарёв А.Н., Полянский К.К. Пилотные установки мембранной фильтрации в процессах переработки молочного сырья //Сыроделие и маслоделие. 2014. № 4. С. 32-33.
  5. Мерзликина А.А., Полянский К.К., Пономарёв А.Н., Ключников А.И. Применение ультрафильтрации в производстве творожных продуктов // Сыроделие и маслоделие. № 6.2014. С. 66-67.
  6. Ключников А.И. Повышение эффективности мембранных процессов с использованием трубчатых керамических мембран: матер. LII отчетной научной конференции за 2013 год: в 3 ч. Ч. 2/под ред. С.Т.Антипова. -Воронеж: ВГУИТ, 2014. С. 15.
  7. Ключников А.И., Потапов А.И. Условия массопереноса через мембрану при наличии концентрационной поляризации. - Продовольственная безопасность: научное, кадровое и информационное обеспечение: матер. II Междунар. науч.-техн. конф.-Воронеж: ВГУИТ, 2015. С. 516-519.

Supplementary files

Supplementary Files
Action
1. JATS XML

This website uses cookies

You consent to our cookies if you continue to use our website.

About Cookies