The drying air can be heated either by Indirect heating (steam, oil
and gas or hot oil) or Direct heating (gas or electricity).
INDIRECT HEATING
A steam heater is a simple radiator. The steam pressure determines the
temperature obtained in ths radiator. Under normal conditions it is possible to
reach air temperatures 10șC lower than the corresponding saturation enthalpy of
the steam.
Modern steam heaters are divided in sections, so that the
cold air first meets the condensate section, then a section with low steam
pressure (which is usually the biggest one in order to utilize as much
low-pressure steam as possible), and then the air finally enters the
high-pressure steam section. The air heater consists of rows of finned tubes
housed in an insulated metal case. The heat load is calculated from the
quantity and specific heat of the air. The heater size depends upon the heat
transfer properties of the tubes and fins and is usually about 50 Kcal/șC x h x
m3 for an air velocity of 5 m/sec. Steam-heated air heaters will
usually have an efficiency of 98-99%. As the steam boiler is usually placed at
some distance from the air heater, 2-3 bar g extra pressure on the boiler
should be anticipated due to pressure loss in the steam pipe and over the
regulating valve. To avoid corrosion of the tubes in the air heater it is
recommended to use stainless steel.
In indirect oil and gas heaters
drying air and combustion gases have separate flow passage. The combustion
gases pass through galvanized tubes that act as heat transfer surface for the
drying air. The combustion chamber is made of heat-resistant steel. The end
cover of the heater should be removable for cleaning of the tubes. Heaters of
this type will in the range of 175-250șC have an efficiency of about 85%. See
Fig. 41.

Hot oil liquid phase air heaters are used either alone, or when high inlet
drying air temperatures are required, and the steam pressure is not high
enough. The heater system consists of a heater, which can be gas- or oil-fired,
and an air heat exchanger. Between these two components a special food-grade
oil or heat transfer fluid, which does not crack at high temperatures, is
circulated at high speed. The main advantage of hot oil liquid phase is the
open pressure-less system.
DIRECT HEATING
Direct gas heaters are only used when the combustion gas can be
allowed to come into contact with the product. They are therefore not common in
the food and dairy industries. The direct gas heater is cheap, it has a high
efficiency, and the obtainable temperature can be as high as 2000șC. When a
plant is designed with an air heater with direct combustion, it is necessary to
calculate the amount of vapour resulting from the combustion (44 mg/kg dry
air/șC), as this will increase the humidity in the drying air. The outlet
temperature has therefore to be increased in order to compensate for this
increase in the humidity and to maintain the relative humidity.
Combustion of natural gas (methane) takes place according to the
following stoichiometric reaction formula:
CH4 + 2 O2 => 2 H2O +
CO2 + Heat
The oxygen for the combustion originates from the atmospheric air
with 21% O2 and 79% N2.
All combustion yields
small quantities of oxides of nitrogen as a result of the reaction of nitrogen
and oxygen at elevated temperatures. Subsequent nitrogen oxide NO and nitrogen
dioxide NO2 formation occurs and is referred to as the sum (NOx) of
the two.
It should be noted that high combustion temperatures, high
heat transfer rates, high excess air, and low residence time in the combustion
chamber are all factors increasing the formation of NOx.
For comparison
the following approximate NOx concentration prevails:
| Normal water supply: |
4000 ppm |
| Cigarette smoke: |
2000 ppm |
| Exhaust gas from a car: |
900 ppm |
| Heavy traffic intersection: |
75 ppm |
| Natural gas boiler stack: |
45 ppm |
| WHO food limit for infants: |
2-5 ppm |
| Spray drying chamber: |
<1 ppm |
| Normal fresh milk: |
0.1 ppm |
The level of NOx in the process air after the direct fired natural gas
air heater will depend on many variable factors, however, with a well adjusted
air heater it should be limited to the above. Only about 2% of the NOx formed
will be absorbed in the milk powder.
The level of NOx in milk powder
depends not only on the method used for heating the process air, but also on
the type of food used for the cows, as well as on the type of fertilizer and
soil used for producing the food.
The NOx level in milk powder is:
Indirect heating: Traces - 2 ppm
Direct heating: 1 - 3.5 ppm
and the level of nitrates (NO3) is in the order of 5-10
times the level of nitrites (NO2).
Electric air
heaters are common on laboratory and pilot plant spray dryers. The
heater has low investment costs, but is expensive in operation and therefore
not used in industrial size plants.