newzeadan
Mechanical
- Jan 23, 2017
- 2
Hello,
I am working on a direct contact condenser design, and have a differing opinion with a colleague. They want the pressure coming out of the water spray nozzle to be equal to condenser pressure (.6psia). Since this is on a fresh water line they are putting in a pressure reducing valve upstream of our water control valve in order to obtain the correct pressure to achieve this.
Now that may be correct, but I am wondering, will it have any effect on the condenser vacuum or anything else, to come out of the nozzle with a bit of extra pressure? I would think extra pressure would be needed to get a good spray pattern out of our nozzle?
So, say we have 50 psig on the water line, and a 5 psig drop through spray nozzle. We are .6psia on the condenser, so he wants pressure upstream of nozzle to be like 6 psia. would it matter if we were say 10psig upstream of nozzle? Even if you take the vacuum out of the equation and just look at simple pipe of 4 in dia, expanding into a 36in dia (condenser), your pressure is going to decrease dramatically, so I would think the extra pressure would be negligible to the vacuum?
Any help is appreciated!
Thanks,
Dan
I am working on a direct contact condenser design, and have a differing opinion with a colleague. They want the pressure coming out of the water spray nozzle to be equal to condenser pressure (.6psia). Since this is on a fresh water line they are putting in a pressure reducing valve upstream of our water control valve in order to obtain the correct pressure to achieve this.
Now that may be correct, but I am wondering, will it have any effect on the condenser vacuum or anything else, to come out of the nozzle with a bit of extra pressure? I would think extra pressure would be needed to get a good spray pattern out of our nozzle?
So, say we have 50 psig on the water line, and a 5 psig drop through spray nozzle. We are .6psia on the condenser, so he wants pressure upstream of nozzle to be like 6 psia. would it matter if we were say 10psig upstream of nozzle? Even if you take the vacuum out of the equation and just look at simple pipe of 4 in dia, expanding into a 36in dia (condenser), your pressure is going to decrease dramatically, so I would think the extra pressure would be negligible to the vacuum?
Any help is appreciated!
Thanks,
Dan