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The system has now been in operation for a couple of years and the customer said at a<br />

presentation in Norway that the company was a little bit sceptic in the beginning but<br />

now that it has proven to work he would not hesitate to take the journey again.<br />

Some facts about cascade vs. 2-stage ammonia<br />

The cascade system is designed for Te/Tc = -47,5/42˚C. Tc CO 2<br />

-7˚C and -12˚C for the high<br />

stage compressors<br />

difference of 5 K between the room temperature and the evaporating CO 2<br />

.<br />

The required swept volume is only about 10% of the comparable two-stage ammonia<br />

system on the low stage.<br />

The return lines are remarkably smaller. The liquid lines are bigger but it makes only a<br />

negligible difference.<br />

The customer Nordlaks AS are very happy with the performance of the system.<br />

We have simulated a two-stage ammonia system for the same conditions with an open<br />

intercooler with a temperature at -12˚C<br />

The results are as follows:<br />

• 11 times larger swept volume on the low stage ammonia system<br />

• 8% higher energy consumption<br />

If we then assume the -47˚C in the IQF freezers and 100 meter return line, 10 bends and<br />

a circulation ratio of 2 and a pressure loss of 0,5 K we get:<br />

• Two stage ammonia DN 300<br />

• Cascade system DN 150<br />

Since the heat capacity of ammonia is higher than CO 2<br />

we get following liquid lines:<br />

• Two stage ammonia DN 40<br />

• Cascade system DN 65<br />

65<br />

Another advantage of the cascade system is that the ammonia high stage now only<br />

operates at pressures well above the ambient pressure and therefore there is no need<br />

for air purger and no water enters the system.<br />

Results<br />

The experience with the plant shows that this concept is very reliable and high<br />

performing. When the IQF freezers are in operation there is only a temperature

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