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Joint International Conference on Long-term Experiments ...

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The classical calco-carb<strong>on</strong>ic purificati<strong>on</strong> of the diffusi<strong>on</strong> juice c<strong>on</strong>sists in the juice’<br />

treatment with lime milk and the subsequent precipitati<strong>on</strong> of the excess (surfeit) of<br />

Ca(OH)2. The resulted mud’ separati<strong>on</strong> raises some special problems. That is the reas<strong>on</strong><br />

for which, in practice, there have been introduced some purificati<strong>on</strong> methods to which<br />

some compromises are being made between the purificati<strong>on</strong> effect and the separati<strong>on</strong><br />

capacity, through decantati<strong>on</strong> or through mud filtering.<br />

RESULTS AND DISCUSSIONS<br />

The technological role of the diffusi<strong>on</strong> juice’ calco-carb<strong>on</strong>ic purificati<strong>on</strong> in the process<br />

crystal sugar obtaining c<strong>on</strong>sists in the eliminati<strong>on</strong> of a part of the diffusi<strong>on</strong> juice’ n<strong>on</strong>sugar<br />

substance employing some operati<strong>on</strong>s specific to each n<strong>on</strong>-sugar groups and<br />

which would provide ,at the given momentum, some optimal c<strong>on</strong>diti<strong>on</strong>s for the<br />

destructi<strong>on</strong> and eliminati<strong>on</strong> of a certain sugar type. Punctually, the role of the calcocarb<strong>on</strong>ic<br />

purificati<strong>on</strong> c<strong>on</strong>sists in:<br />

• Neutralizing the acidity of the diffusi<strong>on</strong> juice and precipitating the calcium salts;<br />

• Precipitating and separating diffusi<strong>on</strong> juice’ colloids;<br />

• Decompounding the reducing substances (agents) and the amides and obtaining the<br />

heat-proof (thermo stable) juices;<br />

• N<strong>on</strong>-sugar absorbing and adsorbing <strong>on</strong> the calcium carb<strong>on</strong>ate (limest<strong>on</strong>e)<br />

• Mud decanting (separating) out of the purified juice;<br />

• Sweetening the mud;<br />

• Thin juice decalcifying and preventing the c<strong>on</strong>centrating stati<strong>on</strong>’ peeling through<br />

vaporizati<strong>on</strong>.<br />

In order to obtain the diffusi<strong>on</strong> juice purificati<strong>on</strong> <strong>on</strong>e employ calcium oxide under the<br />

lime milk shape and carb<strong>on</strong>adoing gas c<strong>on</strong>taining carb<strong>on</strong> dioxide.<br />

In the chart 3 there are represented the characteristics of the lime milk used for<br />

purificati<strong>on</strong> in sugar factories.<br />

Table 3. The characteristics of the lime milk used for<br />

calco-carb<strong>on</strong>ic purificati<strong>on</strong> in sugar factories<br />

C<strong>on</strong>centrati<strong>on</strong> in dry Specific CaO c<strong>on</strong>tent Ca(OH)2 c<strong>on</strong>tent<br />

substance mass<br />

ºBe ºBx g/cm 3 g/l g/100g g/l g/100g<br />

1,49 2,69 1,0084 9 0,98 13,1 1,30<br />

4,69 8,39 1,0314 39 3,87 52,7 5,12<br />

7,59 13,69 1,0534 69 6,64 92,4 8,78<br />

10,34 18,69 1,0749 99 9,29 132,0 12,28<br />

15,54 28,19 1,1184 159 14,29 211,3 18,89<br />

20,34 37,09 1,1614 219 18,93 290,6 25,02<br />

25,49 46,79 1,2124 289 23,91 383,1 31,60<br />

For an accurate evaluati<strong>on</strong> of the functi<strong>on</strong> of the diffusi<strong>on</strong> juice purificati<strong>on</strong>’ stati<strong>on</strong><br />

from a sugar factory it is necessary to be aware of the exact amount of carb<strong>on</strong>adoing<br />

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