View Single Post
Unread 09-16-2003, 07:26 AM   #8
RoboTech
Cooling Savant
 
RoboTech's Avatar
 
Join Date: Sep 2002
Location: Cincinnati, OH
Posts: 229
Default

Thanks Ben,

Yes, there are many possible piping arrangements, especially the order of components. I definately will not be placing the pump after the block. I'm a firm believer in only throttling a centrifugal pumps discharge - always try to minimize any restrictions on the suction side (I agree with pH). I guess I could place the block upstream in the flow path (pump > block > filter > flow meter > throttle valves > res) to minimize the affects of heat generated by restrictions. I will just have to try it different ways to see if there is any measurable difference.

The chiller I'm looking at has a digital controller and can be programmed with a temp offset, which may be useful it setting actual block inlet temp.

Yes, the recirculating pumps built-in to most chillers do not have the head or flow needed for the main test loop.

Manometer - to measure the Delta P across the block you would just connect each side of the manometer U-tube to the inlet and outlet press ports of the block.

I believe flow "sensor" is a generic term that includes all types of flow measuring and detection devices. A flow "meter" specifically measures flow rate while a flow "indicator" generally gives a yes/no (on/off) indication of flow.

The 10 D rule is applicable to certain types of invasive flow meters (turbines, paddle wheels, etc). Some units have flow straighteners built-in and some other types don't care.

50 micron was just an initial guesstimate - more of a strainer than a filter, fine enough to keep the chunks out (protect flow meter) but not so fine as to require frequent maintenace and create a substantial press drop.
RoboTech is offline   Reply With Quote