- •1 Introduction and outline
- •2 Review of literature
- •2.1 Structure of dextran
- •2.2 Microbial loading in sugar factories
- •2.3 The common methods of dextran fractions determination
- •2.4 Dextran content during the process of sugar production
- •2.5 Dextrans associated with processing problems
- •2.6 Crystallization process
- •2.6.1 Growth rate of sucrose crystals
- •2.6.2 Crystallization kinetics
- •2.6.3 Parameters influencing crystallization kinetics
- •2.6.4 Crystal morphology
- •2.7 The Economic gain
- •3 Material and methods
- •3.1 Material
- •3.2 Analytical methods
- •3.2.1 Determination of dextran
- •3.2.1.1 Robert method
- •3.2.1.2 Haze method
- •3.2.2 Microbiological experiments
- •3.2.2.1 Isolation
- •3.2.2.2 Identification
- •3.2.2.2.1 Gas and acid formation
- •3.2.2.2.2 Catalase test
- •3.2.2.2.3 Gram characteristics (KOH-Test)
- •3.2.2.2.4 Identification by API 50 CHL test
- •3.2.2.2.5 L/D-Lactic acid test
- •3.2.3 Crystallization experiments
- •3.2.3.1 Measurement of growth rate of sucrose crystals
- •3.2.3.1.1 Required amount of dextran and seed
- •3.2.3.1.2 Calculation of the growth rate of sucrose crystals:
- •3.2.3.2 Dynamic viscosity
- •3.2.3.3 Crystal morphology and surface topography
- •3.2.3.4 Image analysis
- •3.2.4 Statistical analysis
- •4 Results and discussion
- •4.1 Sensitivity and accuracy of different methods for the determination of dextrans of varying molecular mass
- •4.1.1 Robert’s Copper method sensitivity
- •4.1.2 Haze method sensitivity
- •4.2 Microbial sources of dextran an identification of relevant microorganisms in sugar factories
- •4.3 Levels of dextran contents in different sugar beet factories
- •4.4 Quality of factory final products and their relationship to the levels of dextran during different industrial periods
- •4.5 Influence of dextran concentrations and molecular fractions on the rate of sucrose crystallization in pure sucrose solutions
- •4.5.1 Influence of different temperatures on growth rate of sucrose crystals in the presence of dextran
- •4.6 Elucidation of crystallization kinetics in presence of dextran molecules
- •4.7 Influence of dextran molecule fractions on sucrose solution viscosity
- •4.8 Influence of dextran on the morphology and surface topography of sucrose crystals in presence of dextran
- •4.8.1 Crystal morphology
- •4.8.2 Surface topography
- •4.9 Technical and technological consequences and future perspectives
- •5 Summary
- •6 References
- •7 Appendix
- •8 C. V. and List of Publications
Material and methods |
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3.2.2.2.5 L/D-Lactic acid test
For the determination of D- and L- lactic acid, the UVmethod, cat. no. 11112821035 from R-Biopharm AG was used. In the presence of D-lactate dehydrogenase (D-LDH), D-lactic acid (D-lactate) is oxidized to pyruvate by nicotinamide-adenine dinucleotide (NAD). The oxidation of L-lactic acid requires the presence of the enzyme L-lactate dehydrogenase (L-LDH). The equilibrium of these reactions lies on the side of lactate. By trapping pyruvate in a subsequent reaction catalyzed by the enzyme glutamate-pyruvate transaminase (GPT) in the presence of L-glutamate, the equilibrium can be displaced in favour of pyruvate and NADH. The amount of NADH formed in the above reactions is stoichiometric to the amount of D-lactic acid and of L-lactic acid, respectively. The increase in NADH is determined by means of its light absorbance at 334, 340 or 365 nm.
3.2.3Crystallization experiments
3.2.3.1 Measurement of growth rate of sucrose crystals
A laboratory crystallization unit was built according to Wittenberg, (2001). The unit scheme is given in Figure 16. A double glass wall crystallizer was equipped with stirrer, automatic measurement devices for dry substance content (Refractometer IPR2, Schmidt and Haensch) and temperature as well as temperature control. Data processing was realized on a central computer unit. Dry substance and temperature were determined every 120 s. Batch isothermal crystallization experiments were carried at constant temperatures (60, 65 and 70 °C) by seeding syrup with a supersaturation of 1.15. The experiment was stopped, when the supersaturation had reached 1.05. Varying admixtures of different dextran fractions (T40, T500 and T2000) at different concentrations (500 – 5000 mg/kg DS) were used.
Material and methods |
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2 |
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M |
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Crystallizer |
T |
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Central Computer |
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3 |
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T +/- |
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Thermostat |
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4 |
Control unit |
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Figure 16: Pilot scheme of laboratory crystallization device
1- Thermometer |
2 - Automatic Stirrer |
3- Double glass wall 4- Cooling water |
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5- Refractometer (IPR2, Schmidt and Haensch) |
3.2.3.1.1 Required amount of dextran and seed
The amount of dextran mDE in mg added to the crystallizing charge was calculated according to Equation (3-2).
mDE = a b |
(3-2) |
with
a = mSo wDS /100
b = m#DE 100 /(100 − wW,DE )
Total mass of solution in (kg)
Dry substance content in (%)
Water content of dextran in %
Target dextran concentration in mg/kg DS
After reaching the required temperature, the solution in the crystallizer was seeded with sucrose crystals (size 200 µm) using a syringe. The amount of seed mSeed in g was calculated as follows:
Material and methods |
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3 |
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mSeed =mMa |
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di |
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(3-3) |
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wCry |
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df |
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mMa |
Mass of the massecuite in g |
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wCry |
Final crystal content in massecuite |
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di |
Initial size of the crystal (200 µm) |
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df |
Final size of the crystal |
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A sample was taken before the seeding point to carry out the first image analysis for the evaluation of the solubilization process. Further on, samples for image analysis were taken every 30 minutes in order to follow the growth of crystals through the crystallization.
3.2.3.1.2 Calculation of the growth rate of sucrose crystals:
In the present work, crystallization was pursued basing on refractometric dry substance content and the temperature as:
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wDS,ML,t |
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wDS,ML,t +1 |
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m |
= |
m |
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m |
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100 − w |
100 − w |
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S,Cry |
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W |
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W |
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DS,ML,t |
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DS,ML,t +1 |
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Difference |
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mS,Cry |
Crystallized sucrose mass |
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t |
Time (min) |
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wW |
Mass of water which can be calculated as follow: |
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the change of the
(3-4)
m |
= m |
So |
− |
(mSo wDS,ML ) |
(3-5) |
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W |
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100 |
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ML Mother liquor
The following equation helps to calculate the sucrose crystal surfaces area:
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A = f |
A |
m |
2 / 3 n |
(3-6) |
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Cry |
Cry |
Cry |
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A |
Total crystal surfaces in m2 |
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Cry |
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fA |
Form factor (0.0423) according to Austmeyer, (1981) |
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