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#31
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![]() Ooooooh but that was my point!!! If it's 1200 psi out of a 1/8" nozzle, it ain't gonna be 1200 psi out of a 4" tube.
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#32
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![]() Illustration and graph,
http://home.earthlink.net/~mmc1919/venturi.html If it's on the internet, it must be true. |
#33
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![]() Myka, think your need to separate pressure and flow as they are not the same thing. As for your vac truck could have a 4" line with a 1/8" nozzle and it still would probably take your toes off with the orginal pump. Reason you wouldn't have a 4" line is having to drag around the weight of the water in the hose.
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#34
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![]() OH. LOL I had to many beers last night
__________________
Dan Pesonen Umm, a tank or 5 |
#35
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![]() Quote:
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#36
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![]() But back to the basic question. Does head pressure change at the pump, when using larger diameter pipes for tank return.
NO, it remains the same. The pressure the pump see's is equivalent to the weight of water equaling the volume of a pipe the same diameter as the pump outlet, times the head height. Now as far as friction losses, they are regardless of head height. Friction losses will happen on horizontal runs as well as vertical. If said pump was loosing flow (GPH) due to frictional losses, then yes, upping pipe size can gain back some lost GPH. Heres a chart comparing firehose sizes and friction losses per 100' of hose. Distance and flow determine friction losses, not head height Losses in PSI of firehose per GPM flow @ 100 PSI pump pressure 1.5" diameter GPM/ PSI Loss 50 6.3 100 25 150 56.3 2" diameter 50 1.7 100 6.6 150 14.8 200 26.3 250 41.1 300 59.2 2.5" diameter 150 4.9 200 8.7 250 13.5 300 19.5 And for elevation, add 0.5 PSI for each foot
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Dan Pesonen Umm, a tank or 5 |
#37
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![]() Here I thought the original question was well answered already, and that we were delving off further into the topic...???
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#38
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![]() lol, I'll shut up now
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Dan Pesonen Umm, a tank or 5 |
#39
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![]() BTW there is no head loss in a closed loop
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#40
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![]() Quote:
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