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Integrierte Vermeidung und Verminderung der Umweltverschmutzung

Integrierte Vermeidung und Verminderung der Umweltverschmutzung

Integrierte Vermeidung und Verminderung der Umweltverschmutzung

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2.1.6 Concentration by heat (F)<br />

2.1.6.1 Evaporation (liquid to liquid) (F.1)<br />

2.1.6.1.1 Objective<br />

Chapter 2<br />

Evaporation is the partial removal of water from liquid food by boiling. For instance, liquid<br />

products can be concentrated from 5 % dry solids to 72 %, or even higher, depending on the<br />

viscosity of the concentrates. Evaporation is used to pre-concentrate food, to increase the solid<br />

content of food, to change the colour of food and to reduce the water content of a liquid product<br />

almost completely, e.g. as in edible oil drying.<br />

2.1.6.1.2 Field of application<br />

Evaporation is used in many FDM sectors. For example, it is used to process milk, starch<br />

<strong>der</strong>ivatives, coffee, fruit juices, vegetable pastes and concentrates, seasonings, sauces, sugar and<br />

edible oil.<br />

2.1.6.1.3 Description of techniques, methods and equipment<br />

Steam, vapour, or exhaust gases from other drying operations, are usually used as the heating<br />

medium. The latent heat of condensation is transferred to the liquid food to raise its temperature<br />

to boiling point, to evaporate the water. The vapour is then removed from the surface of the<br />

boiling liquid. Since food products are heat sensitive, it is often necessary to work at low<br />

temperatures. This is achieved by boiling the liquid part <strong>und</strong>er vacuum. Evaporation normally<br />

occurs in the range of 50 to 100 °C, although it can be as high as 130 °C in the sugar industry.<br />

In its simplest form, evaporation is carried out by boiling off water to the air, using immersed<br />

electric heaters. However, in practice the most commonly used equipment is multistage shell<br />

and tube evaporators, or plate evaporators. Shell and tube evaporators may be natural or forced<br />

circulation, climbing or falling film types. Centritherm evaporators, wiped film evaporators<br />

(WFE), thin film evaporators and vacuum pans are specially designed for the evaporation of<br />

highly viscous products. Typical total solids concentrations for various types of evaporators are<br />

shown in Table 2.3. The level of total solids in the outlet depends on the composition of the<br />

product to be concentrated.<br />

Evaporator type Total solids inlet (%) Total solids outlet (%)<br />

Shell and tubes, multistage 5 – 25 40 – 75<br />

Plates, multistage 5 – 25 40 – 75<br />

Vacuum pans 60 – 70 80 – 85<br />

Centritherm, single-stage 5 – 25 40 – 60<br />

WFE, single-stage 40 – 50 70 – 90<br />

Table 2.3: Typical total solids concentrations for various types of evaporators<br />

[1, CIAA, 2002]<br />

Multiple-effect evaporators are used when evaporation requires significant energy, e.g. in sugar<br />

beet processing, starch production and the evaporation of milk and whey. These evaporators use<br />

fresh steam or exhaust gases from other operations, and so recover or re-use energy, to boil off<br />

water vapour from the liquid in the first effect. The evaporated water still has sufficient energy<br />

to be the heat source for the next effect, and so on. A vacuum is applied in a multiple-effect<br />

series to allow the water to boil off. The liquid being processed is passed from one evaporator<br />

body through the others so it is subjected to multiple stages of evaporation. In this way, one unit<br />

of steam injected in the first evaporator can remove three to six units of water from the liquid.<br />

RHC/EIPPCB/FDM_BREF_FINAL January 2006 41

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