Hi guys,
I'm trying to solve a problem with my injection setup. Before I go into all the details, I want to know this:
Suppose we have a circulator in a closed loop 20' elevation below a closed pressurized storage tank. The circulator only has to overcome the friction in the piping to move fluid in that loop, right? The ferris wheel thing. OK.
Now suppose the tank is open to atmospheric pressure. Same piping, same circ. Clearly the static pressure at the pump will be bit lower since pressure is atmospheric at the top of storage rather than say 15 psi. Other than that, is there any difference at all in the pump's operating dynamics? Does it have to overcome any more static head pressure than the closed/pressurized version? If the pump in the atmospheric version was being ramped down by a triac control like a tekmar injection controller, would it have any increased tendency to stall as it is being ramped down, as compared to the pressurized version?
Here's a drawing to make it clearer.
I'm trying to solve a problem with my injection setup. Before I go into all the details, I want to know this:
Suppose we have a circulator in a closed loop 20' elevation below a closed pressurized storage tank. The circulator only has to overcome the friction in the piping to move fluid in that loop, right? The ferris wheel thing. OK.
Now suppose the tank is open to atmospheric pressure. Same piping, same circ. Clearly the static pressure at the pump will be bit lower since pressure is atmospheric at the top of storage rather than say 15 psi. Other than that, is there any difference at all in the pump's operating dynamics? Does it have to overcome any more static head pressure than the closed/pressurized version? If the pump in the atmospheric version was being ramped down by a triac control like a tekmar injection controller, would it have any increased tendency to stall as it is being ramped down, as compared to the pressurized version?
Here's a drawing to make it clearer.