Temperature and level controls in industrial
refrigeration
The
majority of control loops in industrial refrigeration plants are two positions
or on-off. In most storage spaces for frozen food, for example, when temperature
in the space rises to the set point, a solenoid valve opens allowing liquid
refrigerant into the coil. The additional refrigeration capacity thus provided
will drop the temperature. But this method of temperature control sometimes
creates instability of refrigeration plant and reduces its
efficiency.
Refrigeration load of holding freezers are usually
pretty steady. But the load on refrigeration plant is fluctuating very
significantly. Very often we can see continuous loading and unloading of
refrigeration compressors. Refrigeration plant is loosing efficiency when screw
compressors are operating at capacity lower than 100 %. To
improve efficiency and stability of refrigeration plant, we have to minimize the
fluctuation of the load on refrigeration plant. How can we do
that?
Example.
Holding freezer has 4 evaporator coils. Assume that these coils
are operating at optimum suction pressure (October, November 2005
newsletters). Winter refrigeration load is 40% of
summer (design) refrigeration load.
During the summer, all 4 coils are
running. Operating time of these coils are 90-100 %. We have a
stable operation of refrigeration plant.
During the winter, operating time of these coils will
decrease to 35-40 %. Refrigeration plant will have instable
operation. Sometimes 4 coils are running, sometimes just 1 coil
is running. To minimize this instability, total capacity of evaporator coils
should be slightly higher than refrigeration load. In our case, we can turn off
2 coils, for example 2, 4,
and run just coils 1, 3. Operating time of
coils 1, 3 will be 70-80% and
fluctuation of refrigeration load will be reduced. Every day we can switch the
pair of operating coils.
Another source of refrigeration plant instability is a
level control. To keep certain level in the vessel, we should supply liquid from
high pressure vessel. Liquid refrigerant at high pressure passes though a
solenoid and an expansion valve. After expansion valve we have mixture of liquid
and flash-gas vapor. This flash-gas vapor can significantly increase the load on
refrigeration compressors. Operating time of liquid supply solenoids is usually
less than 50 %. When solenoid is open, significant amount of
flash-gas vapor is going into the vessel and refrigeration load on the
compressors is jumping up. Modulating level controls will help you to keep a
precise level in the vessel and will prevent instability of the refrigeration
plant.