V. Tuzhilkin. K. Urazbayeva. R. Alibekov. SEMICONTINUOS SUGAR CRYSTALLIZA TION
3. Reducing sugar losses and colour by rcducing the duration and temperaturę of boiling massecuite.
4. Creating of a favourable environment for automating of the crystals growing phase.
The disadvantage of this method is that a second vacuum apparatus before
filling of crystal mass it has unproductive downtime while this mass is being prepared.
Morę rational organizational management of the product section by using the proposed method with floating vacuum apparatus is shown in figurę 2.
1- crystal oscillator;
2 - vacuum apparatuses;
3 - pipelines;
4,5 - crystallizers;
Fig. 2. The method of boiling with the generation of crystal mass
Journal of Industrial Technology and Engineering, 2012, 2(3): 11-18
The most suitable operation of productivity department by the proposed method is the generation of crystal base produces in the special dedicated crystal generator.
According to this method, the crystal base obtained in the crystal generator then direct to a special receiver mixer (Fig. 3). As reąuired the crystalline mass taken up in the vacuum apparatus in which the growing of crystals on the semi-continuous crystallization technology.
There is provided the variant of operation organization of product
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separation, when the vacuum apparatus generate crystal mass in the amount of Ncr -2Ncr, steam-heated first or second housing evaporator, and the remaining vacuum units operating in a semi-continuous crystallization of sugar, steam heat one notch below than machinę - generator crystal mass.
Crystallization by using artificially prepared massecuite.
This crystallization method is based on a predetermined concentration of the massecuite preparation Substance Content = 87 88 % on the base of a mixture of