LukePDX
New Member
Nortiz publishes pressure loss curves for their products. I'm trying to understand the practical implications of this. For example, http://support.noritz.com/download.php?file=Literature Page/Spec Sheet/NRCP SPEC.pdf&field=SpecSheet.
For the most part there appears to be a somewhat nonlinear drop in pressure across the unit relative to the flow rate. During low-flow operation (large delta T, or low flow operation like sinks) the pressure drop is quite low and seems like something I can just ignore. During higher flow operation (two showers, tub fillers, etc), the unit above claims that pressure will drop 15 to 30 psi across the unit.
Presumably I should se a bit of a pressure increase at the mixing valve for the shower/tub fillers because the cold water should still have roughly the original pressure for the system.
Does anyone have any rules of thumb about pressure loss in these units? I think we get about 65 PSI from the city, and I think we want something like 45 PSI at the tub filler mixing valve (not sure about the showers). If I lose the maximum (8GPM flow is 30 PSI drop) then the hot line would be at 35 PSI (ignoring other losses). Recombining with the 65 PSI cold line to mix 120 degrees hot line down to like 110 degrees should boost this a bit, right?
My main concern is low pressure showers and very slow tub fill rate (if, e.g., I have a 10GPM@44 PSI mixing valve, but I'm only getting low 30 PSI at the valve due to system-wide losses). Should I look for a unit with better pressure loss, or am I likely to be okay?
For the most part there appears to be a somewhat nonlinear drop in pressure across the unit relative to the flow rate. During low-flow operation (large delta T, or low flow operation like sinks) the pressure drop is quite low and seems like something I can just ignore. During higher flow operation (two showers, tub fillers, etc), the unit above claims that pressure will drop 15 to 30 psi across the unit.
Presumably I should se a bit of a pressure increase at the mixing valve for the shower/tub fillers because the cold water should still have roughly the original pressure for the system.
Does anyone have any rules of thumb about pressure loss in these units? I think we get about 65 PSI from the city, and I think we want something like 45 PSI at the tub filler mixing valve (not sure about the showers). If I lose the maximum (8GPM flow is 30 PSI drop) then the hot line would be at 35 PSI (ignoring other losses). Recombining with the 65 PSI cold line to mix 120 degrees hot line down to like 110 degrees should boost this a bit, right?
My main concern is low pressure showers and very slow tub fill rate (if, e.g., I have a 10GPM@44 PSI mixing valve, but I'm only getting low 30 PSI at the valve due to system-wide losses). Should I look for a unit with better pressure loss, or am I likely to be okay?
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