

The TetraMagna Evaporator is a fully automatic and continuous evaporation system suitable for producing a wide range of dairy products. It is designed to be customer-specific, accommodating various product compositions and capacities.
The evaporator is fed from the wet process area, where the product is preheated using plate heat exchangers. The evaporation process follows the falling film principle, with product and vapor flowing downwards through tubes. Concentrate is separated from vapor in a separator, and further concentrated in subsequent passes. Mechanical vapor recompression (MVR) is preferred when steam costs are high, with a density controller managing the MVR fan speed. The final concentrate is pumped into the concentrate tank of the dryer.
The system's capacity depends on milk composition and intake. For example, concentrating skim milk from 9% to 50% total solids for a 44,000 kg/hr feed.
For a capacity of 44,000 kg/hr skim milk from 9.0 to 51%:
Required footprint: 18 x 7 meters
Required building height: 30 meters
Note: Design modifications may be introduced without prior notice. Tetra Pak and TetraMagna are trademarks of the Tetra Pak Group.
Tetra Magna™ Evaporator – MVR Continuous milk evaporation system Long production runs due to high hygienic standards Proven technology Fully cleanable (Cleaning in Place) Application The Tetra Magna Evaporator provides a fully automatic and continuous evaporation system. The Tetra Magna Evaporator is suitable for the production of the complete range of dairy products. The system is customer specific designed, and therefore available for a wide range of product compositions and capacities. Working principle The Tetra Magna Evaporator is fed from the wet process area. From the balance tank product is preheated with plate heat exchanger (PHE) pre-heaters against concentrate and excess vapours from the calendria. Final heating is achieved with a PHE against hot water. Product starts to evaporate in the top of the first calandria. The evaporator works according the falling film principle, which means that product and vapour are flowing downwards through the tubes. At the bottom, concentrate falls down and vapour is sucked into the separator, whereby the smaller concentrate droplets are separated from the vapour. Concentrated product is pumped to the next pass, whereby product is concentrated further. When steam costs are high and/or the amount of water evaporation is high, preferably mechanical vapour recompression (MVR) is used. Major parameters to check are: availability, reliability and costs of electricity. A density controller in the concentrate flow is used to set the speed of the MVR fan. After the final pass product is pumped to the Tetra Magna TVR calandria, using steam as driving force. Final concentrate is pumped into the concentrate tank of the dryer.
Open the catalog to page 1Capacity of the evaporator system depends on milk composition and milk intake. For example if skim milk is concentrated from 9 to 50% total solids for a 44,000 kg/hr feed a typical system would be as follows: Based on a capacity of 44,000 kg/hr skim milk from 9.0 to 51 % and during normal production: Balance tank Feed pump Pre-heaters Calandrias Vapour separators Condensor Ducting Instrumentation Documentation and engineering Steam (incl. DSI) Electricity Cooling water Ring water Sealing water 995 kg/hr (medium heat) 420 kW (absorbed kW for MVR and pumps) 15 m³/hr with 30°C in and 48°C out 1.0...
Open the catalog to page 22 Pages
2 Pages
6 Pages
3 Pages
3 Pages
2 Pages
2 Pages
2 Pages
2 Pages
5 Pages
4 Pages
3 Pages
2 Pages
28 Pages
4 Pages
2 Pages
12 Pages
2 Pages
2 Pages
24 Pages
2 Pages
2 Pages
3 Pages
4 Pages
60 Pages
8 Pages
2 Pages
2 Pages
60 Pages