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The production of hot w ater dip hydrolysate (HWDH) from tilapia (Oreochromis niloticus) with DH of 25.43% improved its bioactivity. A pressure-driven ultrafiltration (UF) membrane separated HWDH base...
In order to study the influence of the vacuum evaporation (VE) process on the functionality of whey protein concentrates (WPC’s) , Cheddar WPC’s were produced with and without VE, viz. by i) ultrafilt...
Two fractions (50-K and permeate) from a proteolytic hydrolysate (degree of hydrolysis, DH=3.8 %) of wheat gluten were separated using ultrafiltration (UF) membrane with molecular mass cut-off of 50 k...
The linear and non-linear rheological properties of defatted soy proteins produced by ultrafiltration-diafiltration were investigated at three temperatures. Five concentrations ranging from 10 to 30% ...
With the aim of producing dietary supplements for phenylketonurics, using whey hydrolysates as protein sources, the effect of some procedures over phenylalanine (Phe) removal was evaluated. Twelve whe...
Permeate and retentate (concentration factor ca. 2x) from UF of skim milk were combined, and cream was added to produce skim milk (0.1% fat) and 1% milk with a range of true protein contents (1.0 to 4...
Permeate and retentate (ca. two times concentration factor) from the ultrafiltration (UF) of skim milk were combined, and cream was added to produce milks with 2% and 3.3% fat and a range of true prot...
The linear and non-linear rheological properties of defatted soy proteins produced by ultrafiltration-diafiltration were investigated at three temperatures. Five concentrations ranging from 10 to 30% ...
With the aim of producing dietary supplements for phenylketonurics, using whey hydrolysates as protein sources, the effect of some procedures over phenylalanine (Phe) removal was evaluated. Twelve whe...
An ultrafiltration unit, the ES-30 membrane (molecular weight cut-off 30,000) was used to recover the proteins from the wastewater produced during mungbean starch processing. During ultrafiltration, t...

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