MinnesotaSlinger
Mechanical
- Feb 13, 2008
- 23
I am looking to run a small fraction of a flow (say, 10% of 200 gpm) through a heat exchanger. The HX would be selected with calculated venturi D/P in mind. The HX would be for cooling condensate from a steam-to-water HX, which will operate at about 50 psig and therefore have condensate coming out well above the boiling point when going to a tank at atmospheric pressure. Ahead of the steam-to-water HX, I was thinking of creating a sidestream that could be powered by a circulator pump, but it would seem almost simpler to just drive flow using the venturi that connects the inlet to 3" piping and the outlet to a 2" section downstream, which should give me about 2 psid to drive flow through the HX tubes. (Doing this would also keep flow proportional through both HXs.) If actual flow through the HX varies somewhat from calculated, I don't think it would be a problem given the lack of need for precision. The only thing I'd be concerned about is erosion in the narrow section, ensuring D/P is strong enough to drive require flow to cool condensate as desired (i.e., below 212 F), and ensuring D/P is not so strong as to drive too much flow through the condensate cooling HX as to cause tube erosion. Is this a bad idea? Should I just go with a circulator pump for the sidestream?