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where!!
! hL!is!the!head!losses!due!to!friction![L]!
! f!is!an!empirical!friction!factor![Y]!
! L!is!the!length!of!the!tubing![L]!
! D!is!the!diameter!of!the!tubing![L]!
! V!is!the!average!fluid!velocity![L/t]!=!Q/A!
! Q!is!the!volumetric!flow!rate![L3/t]!
! A!is!the!crossYsectional!area!of!tubing![L2]!=!πD2/4!
! g!is!the!acceleration!due!to!gravity![L/t2]!
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Frictional!head!losses!are!proportional!to!fluid!velocity!and!tubing!length!and!inversely!
proportional!to!tubing!diameter.!!The!friction!factor,!f,!is!a!function!of!the!Reynolds!
number!and!can!be!calculated!using!the!Blasius!equation:!!
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! ! ! ! f = 0.316 Re-0.25! ! ! ! ! ! ! ! ! ! ! ! ! ! ! (2)!
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where!Re!is!the!Reynolds!number!
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Re =
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DV
υ !!
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(3)!
and!ν!is!the!kinematic!viscosity!of!the!fluid![L2/t!].!!
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The!head!lift!and!length!of!tubing!required!at!each!of!the!six!Dead!Run!stations!is!shown!
in!Table!3.!!We!calculated!the!frictional!head!losses!for!at!0˚C!and!30!˚C,!and!at!fullyY
charged!and!lowYvoltage!conditions!for!both!pumps!(Appendix!A).!!!
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Table!3.!!Head!lift!and!tubing!length!at!each!station.!
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* Station!!!!!!!!Head*lift**********Tubing*length*
* *******required* ********required*
* * * (ft)!! ! ! (ft)!
DRKR!! ! 9.0!! ! ! 21!
DR1! ! 9.8!! ! ! 18!
DR2!! ! 8.0!! ! ! 45!
DR3!! !! 7.3!! ! ! 19!
DR4! ! 7.4!! ! ! 36!
DR5! ! 9.2!! ! ! 26!
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