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Modeling of Enzymatic Hydrolysis of Whey Proteins
The aim of this work was to emphasize the limitations of modeling complex phenomena under unrealistic model assumptions. As a case study, the whey protein hydrolysis mechanism was modeled. A stirred batch reactor was used to study the degree of hydrolysis of sweet whey protein concentrate by using t...
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Published in: | Food and bioprocess technology 2012-08, Vol.5 (6), p.2596-2601 |
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Main Authors: | , , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | The aim of this work was to emphasize the limitations of modeling complex phenomena under unrealistic model assumptions. As a case study, the whey protein hydrolysis mechanism was modeled. A stirred batch reactor was used to study the degree of hydrolysis of sweet whey protein concentrate by using the protease alcalase. A completely random two-factorial experimental design was used, three levels of initial enzyme concentrations (
E
0
) (1.58, 3.18, 6.36 AU (Anson units)/L) times three levels of initial substrate concentrations (
S
0
) (18.73, 38.45, 81.16 g/L). All treatments were carried out at optimal alcalase—activity conditions: pH 8 and 50 °C. Reactions were monitored for 180 min. The degree of hydrolysis (
h
) curves was finally adjusted for each treatment to the exponential model
using nonlinear regression techniques but not assuming a Michaelis–Menten relationship. From the estimation process, the coefficient
b
was constant (27.26 ± 1.37) and independent of
E
0
and
S
0
, while coefficient
a
depended directly on the ratio
E
0
/
S
0
, ranging from 0.0017 to 0.0497. A noncritical strategy of forward modeling based on unrealistic assumptions was misleading in the face of complex phenomena; instead, a modeling strategy moving from data to the identification and estimation of parameters of practical interest must be considered. |
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ISSN: | 1935-5130 1935-5149 |
DOI: | 10.1007/s11947-011-0624-5 |