Electronic Journal of Polish Agricultural Universities (EJPAU) founded by all Polish Agriculture Universities presents original papers and review articles relevant to all aspects of agricultural sciences. It is target for persons working both in science and industry,regulatory agencies or teaching in agricultural sector. Covered by IFIS Publishing (Food Science and Technology Abstracts), ELSEVIER Science - Food Science and Technology Program, CAS USA (Chemical Abstracts), CABI Publishing UK and ALPSP (Association of Learned and Professional Society Publisher - full membership). Presented in the Master List of Thomson ISI.
2004
Volume 7
Issue 2
Topic:
Food Science and Technology
ELECTRONIC
JOURNAL OF
POLISH
AGRICULTURAL
UNIVERSITIES
Słomińska L. , Wi¶niewska D. , Niedbach J. 2004. THE INFLUENCE OF ADDITIONAL ENZYMES TREATMENT OF CORN AND POTATO MIX STARCHES ON FILTRATION PROPERTIES OF HYDROLYSATES , EJPAU 7(2), #04.
Available Online: http://www.ejpau.media.pl/volume7/issue2/food/art-04.html

THE INFLUENCE OF ADDITIONAL ENZYMES TREATMENT OF CORN AND POTATO MIX STARCHES ON FILTRATION PROPERTIES OF HYDROLYSATES

Lucyna Słomińska, Danuta Wi¶niewska, Joanna Niedbach

 

ABSTRACT

Starch hydrolysates were prepared by hydrolysis of potato and corn starch mixture with a heat-stable bacterial alpha amylase (Termamyl 120 LS) or with a heat-stable bacterial alpha amylase (Termamyl 120LS) and next with a fungal alpha amylase (Finizym 1600L). Additionally so-called filtration enzyme action was applied (Finizym, Neutrase, Lecitase, SP 348, Gammazym LPL). Introduction of these enzymatic preparations influenced on the increase of filtration rate of hydrolysates and decrease of their viscosity and transmittance value. “Filtration enzyme” did not influence on the carbohydrate composition.

Key words: starch, alpha-amylase, hydrolysates, carbohydrate, filtration rate, viscosity..

INTRODUCTION

Starch hydrolysates are prepared by conversion of starch with acid or enzymes. Hydrolysates are filtered to remove suspended solid and insoluble impurities. They influence unfavorably on the filtration rate of hydrolysates. Their amount depends on botanical source of starch. The hydrolysates after enzymatic conversion of corn starch contain the insoluble particles in the range of 0.2-1.0 µm. These particles consist of nongelatinized starch [1, 3] or amylose-lipids complexes [5]. The impurities which exist in corn starch hydrolysates are connected with chemical composition of corn starch. Corn starch contains several times more protein (corn starch 0.35%, potato starch 0.06%) and lipids (corn starch 0.87%, potato starch 0.05%) than potato starch [17]. Protein present in hydrolysates is disadvantages considering its negative effect on the color and aroma of the hydrolysates and its contributes to the formation of foam during the process of its production [10, 11]. Similarly lipids content in starch is also unprofitable during starch hydrolysis. In the process of heating starch suspension lipids form amylose-lipids complexes that have negative effect on ability of water assimilation as well as swelling and solubility of starch [2, 4]. They also cause opalescent and cloudiness of starch slurry and give worse filtration characteristic of product. Application of potato and corn starch mixture in hydrolysates production reduces the amount of lipids and protein in product which is undesirable for technological process. Application of so-called filtration enzymes additionally increases of filtration rate of hydrolysates [8, 12].

The attempts of hydrolysates filtration improvement was also made by application of membrane filtration [6, 15, 16].

In this study the effect of “filtration enzymes” on the hydrolysates filtration obtained from potato and corn starch mixture was studied.

MATERIALS AND METHODS

Starch

Potato starch (Factory of Potato Industry - Poland), corn starch (Avebe - Holland) were used.

Enzyme

Termamyl 120 type LS (Novo Nordisk, Denmark) - a mixture of outstanding heat-stable alpha-amylases produced by selected strains of Bacillus licheniformis. The enzyme activity was 120 KNU/g (KNU = Kilo Novo Units alpha-amylase – the amount of enzyme which breaks down 5.26 g starch per hour at Novo Nordisk’s standard method for determination of alpha amylase).

Finizym (Novo Nordisk, Denmark) – a fungal beta glucanase produced by a selected strain of Aspergillus niger. The enzyme activity was 200 FBG/g (FBG = Fungal Beta-Glucanase unit – the amount of enzyme which, under Novozymes’ standard conditions degrades barley beta-glucan to reducing carbohydrates with a reduction power corresponding to 1 µmol glucose per minute).

Neutrase (Novo Nordisk, Denmark) – a protease produced by selected strain of Bacillus subtilis. The enzyme activity was 0.5 AU/g (AU Anson Units).

Lecitase (Novo Nordisk, Denmark) - a purified phosfolipase A2 manufactured from porcine pancreas. The enzyme activity is was 10.000 IU/ml (IU – the amount of enzyme producing 1 µmol of free fatty acid per minute under international standard conditions. SP 348 (Novo Nordisk, Denmark) – a complex carbohydrate mixture with beta glucanase and pentosanase activities.

Gammazym LPL (Gammazym, Germany) – a lysophospolipase derived from Aspergillus niger.

Fungamyl 1600L - a fungal alpha-amylase produced by selected strain of Aspergillus oryzae. The enzyme activity was 1600 FAU/g (FAU = Fungal Alpha-Amylase unit – the amount of enzyme which breaks down 5.26 g starch per hour at Novozymes’ standard method for determination of alpha-amylase).

Analysis

Procedure

Potato and corn starches mixed in 1:1 ratio were slurried in water to obtain a starch concentration of 35% DS. Hydrolysis was performed with the application of Termamyl LS used in amount of 0.15% at 97C and pH 6.0-6.5 within 1 h. Ca++ in amount of 40 ppm was used as an activator.

Action of additional enzymes (Finizym, Neutrase, Lecitase, Sp 348, Gammazym LPL) was carried out before or after alpha-amylase treatment using following enzymes dosages: 0.05: 0.1 and 0.15% at 50°C within 1,2 3, 7 h.

Liquefied by Termamyl action starch was further hydrolysed by the use of simultaneous action of Fungamyl and Finizym at 55°C and pH 5.0 by 20h.

RESULTS AND DISCUSSION

Starch properties

The properties of the tested starches used as substrates for alpha- amylase action are shown in Table 1.The measurement of absolute starch colour by the L*a*b* colour system indicate that potato starch has better colour parameters. Negative value of chromaticity coordinate “a” which indicates affinity to green colour and positive value of chromaticity coordinate “b” which indicate affinity to yellow colour are lower for potato starch.

Table 1. Physical and -chemical properties of starch

Properties

Potato starch

Corn starch

Moisture (%)

19.5

11.9

Proteins (% on d.s.)

0.05

0.4

Lipids (% on d.s.)

0.03

0.1

Ash (% on d.s)

0.26

0.14

Colour

L = 93.66
a =  -1.53
b = +1.34

L = 94.68
a =  -2.78
b = +5.70

Average diameter of starch granule m

36

14

L - lightness factor; **a, b - chromatically coordinates

The size of tested starches granules is different. The potato starch granules diameter is almost three times higher than corn starch granules.

Action of enzymatic preparations in production of maltodextrine from potato and corn starches mixture

Dextrose equivalent and carbohydrate composition

Table 2 illustrates the influence of additional enzyme action, called futher so-called filtration enzymes (Finizym, Neutrase, Lecitase, SP 348, Gammazym LPL) on liquefaction process carried out by alpha-amylase (Termamyl ). It can be observed that DE of samples is similar but differences exist in their carbohydrate composition. The application of so-called filtration enzymes influences on the decrease of G2-G7 by 20-44% but G8-G10 only by 3-13% or increase by 8-16% in comparison to samples without “filtration enzymes”. The level of higher sugar (Gn) increases by 13-20%.

Table 2. Dextrose equivalent and carbohydrate composition of hydrolysates
 

-

Termamyl

Finizym
+
Termamyl

Neutrazym
+
Termamyl

Lecitase
+
Termamyl

SP 348
+
Termamyl

Gammazym LPL
+
Termamyl

DE

10.7

10.3

10.4

10.2

10.1

10.0

G1
G2
G3
G4
G5
G6
G7
G8
G9
G10
G11
Gn

- 
3.1 
6.3 
4.2 
5.4 
5.8 
5.7 
3.7 
3.2 
2.6 
-
60.0

- 
1.9 
3.5 
2.8 
3.3 
3.9 
4.0 
3.2 
2.8 
2.4 
- 
72.2

- 
2.4 
4.0 
3.3 
3.2 
4.5 
4.5 
3.6 
3.1 
2.8 
- 
69.6

- 
2.1 
3.9 
3.1 
3.6 
4.2 
4.3 
3.3 
2.8 
2.6 
- 
70.1

- 
2.0 
3.6 
2.8 
3.4 
3.9 
4.0 
3.2 
2.8 
2.6 
0.6 
71.1

- 
1.9 
3.9 
2.8 
3.5 
4.0 
4.2 
3.1 
3.8 
2.6 
- 
70.2 

Filtration rate

The application of each enzyme from so-called filtration enzymes gives by 28-86% higher filtration rate (Fig. 1) The highest influence can be observed in the case of Finizym application.

Fig. 1. Influence of applied enzymatic preparations on filtration rate. Process conditions: substrate concentration: 35% d.s., Termamyl dosage: 0.15%, pH 6-6.5, 1 h, 97°C, filtration enzyme dosage: 0.15%, pH 5-5.5, 3 h, 50°C

Transmittance value

Figure 2 shows the positive influence of “filtration enzymes” on transmittance value – the decrease of transmittance value by 13 – 35%. The best results are also obtained for Finizym application similarly as in the case of filtration rate.

Finizym, which obtains a beta glucanase, was chosen for further research. It indicates that beta glucans are the substances mainly responsible for the high viscosity of hydrolysates.

Fig. 2. Influence of enzymatic preparations on transmittance value of hydrolysates. Process conditions: substrate concentration: 35% d.s., Termamyl dosage: 0.15%, pH 6-6.5,
1 h, 97°C, filtration enzyme dosage: 0.15%, pH 5-5.5, 3 h, 50°C

Influence of Finizym action on filtration rate of liquefied starch

Reaction time and enzyme dosage

The research work of application of enzyme dosages: 0.05, 0.10,and 0.15% indicate that filtration rate increases when enzyme dosage was enhancement from 0.05 to 0.1% but further increase has no influence on filtration rate (Fig. 3a). Sufficient enzyme dosage was 0.1%.

Prolongation of reaction time of Finizym from 1-to 3 h influences positively on filtration rate ; increases by 30% filtration rate (Fig. 3b). In the case of using of Finizym after Termamyl LS action the filtration rate was by 15% lower.

Fig. 3. Influence of Finizym dosage (A) and time of enzyme action (B) on filtration rate. Process conditions: substrate concentration: 35% d.s., Termamyl dosage: 0,15%, pH 6-6.5, 1 h, 97°C, filtration enzyme dosage: 0.15%, pH 5-5.5, 3 h, 50°C

Sequence of enzyme action

Finizym action was used before and after alpha-amylase action (Fig. 4). Both ways of Finizym application cause the increase of filtration rate however better results are obtained when in the first place Finizym was used and then liquefaction by Termamyl LS was carried out.

Fig. 4. Influence of sequence of Finizym application on filtration rate. Process conditions: substrate concentration: 35% d.s., Finizym dosage: 0.15%, pH 5-5.5, 3 h, 50°C, Termamyl 120L dosage:
0.15%, pH 6-6.5, 1 h, 97°C

Viscosity

Viscosity measurements of hydrolysates after 1, 2 and 3 h action of Finizym show that during prolongation of enzyme action time the hydrolysate viscosity decreases (fig. 5). After 1h of enzyme action the viscosity is 29.6 MPa·s, but after 2 h of reaction is by 22% lower and after 3 h – by 41% lower.

Fig. 5. Viscosity changes during prolonged Finizym action. Process conditions: substrate concentration: 35% d.s., Termamyl dosage: 0.15%, pH 6-6.5, 1 h, 97° C, filtration enzyme dosage: 0.15%, pH 5-5.5, 3 h, 50°C

Finizym and Fungamyl action

The simultaneous action of Fungamyl and Finizym influences on following factors: filtration rate (increase by 69%), viscosity (decrease by 13%) and transmittance value (decrease by 25%) (table 3). Carbohydrate composition stayed without any influence on additional action of “filtration enzyme”

Table 3. Influence of Finizym action on saccharified starch properties
 

Termamyl + Fungamyl

Termamyl + Fungamyl
+ Finzym

DE

47.2

46.8

Filtration rate [LMH]

320

540

Viscosity [mPas]

5.5

4.8

Transmitance value

0.095

0.071

G1
G2
G3
G4
G5
G6
G7
G8
G9
G10
G11
G12
Gn

5.8 
51.6 
19.8 
2.0 
2.9 
3.1 
2.3 
1.5 
1.0 
1.3 
2.2 
2.0 
4.5

5.9 
51.6 
19.5 
1.9 
2.9 
3.1 
2.3 
1.5 
1.0 
1.3 
2.1 
2.1 
4.8

CONCLUSIONS

REFERENCES

  1. Atkins D.P., Kennedy, J.F., 1985. A comparison of the susceptibility of two commercial grades of wheat starches to enzymatic hydrolysis and their resultant oligosaccharide product spectra. Starch/Staerke 37, 12, 421-427.

  2. Bowler P., Towersey, P.J., Galliard, T., 1985. Some effects of the minor components of wheat starch on glucose syrup production. Starch/Staerke 37, 10, 351-356.

  3. Braum P. J., Teaque W. M., 1989. Isolation and characterization of starch – iodine positive material formed during saccharification of corn starch. Starch/Staerke 41, 343-348.

  4. Ducroo P. 1987. Improvements relating to the production of glucose syrups and purified starches from wheat and other cereal starches containing pentosans. European Patent Application EP 0228732

  5. Hebeda R. E., Leach H. W., 1974. The nature of insoluble starch particles in liquefied corn-starch hydrolysates. Cereal Chem. 51, 272-281.

  6. Hinkova A., Bohacenko I., Bubnik Z., Hrstkova M., Jankovska P., 2004. Mineral membrane filtration in refinement of starch hydrolysates. J. Food Eng. 61, 521-526.

  7. ISO 3947:1947

  8. Konieczny-Janda G., Richter G., 1991. Progress in the enzymatic saccharification of wheat starch. Starch/Staerke 43, 308-315.

  9. Lowry O. H., Rosenberg N. H., Farr A. L., Randell K. J., 1951. Protein measurement with the Folin phenol reagent. J. Biol. Chem. 193, 265-275.

  10. Matser A. M., Steeneken P.A.M., 1998. Filtration characteristics of maize and wheat starch hydrolysates. Cereal Chem. 75, 2, 241-246.

  11. Matser, A. M., Steeneken, P. A. M. 1998 Origins of poor filtration characteristics of wheat starch hydrolysates. Cereal Chem. 75 (3) 289-293.

  12. Nebesny E., Rosicka J., Pierzgalski T., 1998. Enzymatic hydrolysis of wheat starch into glucose. Starch/Staerke 50, 8, 337-341.

  13. Pearson D., 1976. The chemical analysis of food. Churchill Living Stone, London.

  14. Rauscher K., 1956. Untersuchung von Lebensmitteln, Fachbuchverlag, Leipzig, 2, 125.

  15. Singh N., Cheryan, M., 1996. Process design and economic analysis of a ceramic membrane system for microfiltration of corn starch hydrolysates. J. Food Eng. 38, 57-67.

  16. Singh, N., Cheryan, M,. 1998. Properties and composition of concentrates and syrup obtained by microfiltration of saccharified corn starch hydrolysates. J. Cereal Sci. 27, 345-320.

  17. Swinkels J. J. M., 1985. Composition properties of commercial native starches. Starch/Staerke 37, 1-5.


Lucyna Słomińska
Starch and Potato Products Laboratory
Armii Poznań 49, 62-030 Luboń, Poland
ph. (+48 61) 893 46 05 ext. 106
fax. (+48 61) 893 46 08
e-mail: ls@man.poznan.pl

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