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Posted by nicksanspam on November 23, 2007, 4:25 pm
 


The thermal part might happen without a heat exchanger.


What's a thermovar? You might run the pump with a 3-way heatmotor zone valve
for mixing.


You might use a cast iron pump with a 1/2% solution of ACI-100 corrosion
inhibitor from D. W. Davies.


An STSS tank.


The EPDM tank liner only works to 170, long-term.

Nick


Posted by Loren Amelang on November 20, 2007, 3:05 pm
 
On Mon, 19 Nov 2007 17:35:28 -0800 (PST), Randy


Google "heat exchanger ntu technique"...  That's the estimation method
I've found to be simple enough to use and still decently predictive. I
don't know how to add the effect of the fins you mentioned, but I've
had good luck with smooth pipe.

Loren

Posted by John Barry on November 24, 2007, 3:36 pm
 Randy,
Another factoid of note (TM):
Counter-flow heat-exchanger will be much more efficient than "normal"
parallel-flow, in that, if properly sized for flows & temps, the
discharge temp of each loop will closely approximate the input temp of
the other loop. (This is common with air-air exchangers I've looked at.)
Downside: need (2 ea) loops w/pumps, to run the coldest of the cold
reservoir into the exchanger, with the discharge of that loop to the top
of the cistern.
HTH,
John

Randy wrote:


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