I
Thermal Energy Regeneration
 
  ¢Â  Evaporator
  ¢Â  Strip. Column&Vessel
  ¢Â  Distillation Column
  ¢Â  Evaporator
  ¢Â  Crystallizer
 
 
 Evaporator heated by MVR
Product : Cane sugar solution
Feed : 108,768 kg/h, 65.6 ¡ÆBrix
Concentrate : 94,757 kg/h, 75.3 ¡ÆBrix
Evaporation : 14,011 kg/h
MVR motor : 2 x 240 KW
Steam : nil

For concentratrion of dairy products such as milk and whey, only one stage MVR can compress the evaporated vapor for 6¡­7¡É temperature elevation that must be sufficient because there is no boiling temperature rise to the concentrated solution over the evaporated vapor temperatre, i.e. BPR = 0¡É.

However, the products consisting of low molecuar weight solute such as sugar and hydrocarbons differently to proteins have boiling point rise of 5¡­10¡É proportional to concentration, thus one stage MVR must not be sufficient to have a good temperature gradient between shell and tube side.

The above illustrates the evaporator concentrating cane sugar solution from 65.5 ¡ÆBrix to 75.3 ¡ÆBrix without consuming a fresh steam from boiler except during a start-up stage of 20¡­30 minutes. The most of evaporated and compressed vapor is condensed in the shell side of the evaporator that a very small condensing duty is required.

This two stage MVR elevates the evaporated suction temperature by 14¡É to provide 6¡­8¡É temperature gradietnt between heat exchange surface of the evaporator.

 Evaporator heated by TVR
 Descriptions
Unit
1
2
3
4
5
6
7
8
 Medium
 
Feed
Solution
Solution
Solution
Discharge
Steam
Water
Water
 Mass flow
kg/h
10,000
7,177
4,465
3,248
2,400
1,550
9,166
120,000
 Total solid
wt%
12.0
16.7
26.9
36.9
50.0
 
 
 
 Temperature
¡É
74
74.2
67.8
62.1
42.6
170
55
32

This reference is 4-effect falling film evaporator built in 2004, heated by TVR for concentrating 12 wt% coffee extract up to 50 wt% total solid before spray drying process.

For the total water evaporation of 7,600 kg/h, 1,550 kg/h motive steam is used that steam efficiency is only 0.2, close to 5-effect system.

Since a TVR can replace one effect evaporator, it sould be always recommended to put a TVR in multi-effect evaporator system in order to realize less investment for the same economy, unless boiling point rise is less than 5¡É.

 
 
   
 
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copylight ¨Ï 2004. Sunjin Technical Solution Ltd.