Methods and UHT plant for producing a drinkable mixture from a carrier liquid and at least one cereal under aseptic conditions
A technology for mixtures, grains, applications, dairy products, milk formulations, etc.
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[0051] The device constructed as a UHT device as a whole is in figure 1 The sub-area 100 shown in , starting from the first pipeline section 8.1, includes a partially shown preheating zone VWZ, a preheating zone VZ, a high-temperature heating zone HZ, a holding zone HHZ and a potable mixture P to be produced. In the partly shown cooling zone KZ, the carrier fluid TF, for example drinking milk M, flows into the first line section in the flow direction shown, for example at a temperature of about 5° C. In the shown partial area of the preheating zone VWZ, the rearmost or at least only heat exchanger 1 of the preheating zone is shown, which is configured as a so-called tube-bundle heat exchanger, in which heat exchanger The VW is preheated in the heat exchanger to a temperature of, for example, about 70° C., and the heat exchanger is usually operated regeneratively. The tube-bundle heat exchanger is preferably of the type described in DE-U-94 03 913 (Prinzip Tuchenhagen Dairy ...
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