3) If the flow in the 2.0 in. diameter pipe was expected to be laminar (Ng < 1399), the velocity was to be within pressure line velocity specifications (20 f/sec), and the specific gravity of the oil was 0.93. (a) What would the viscosity of the oil need to be in cS (b) What would the viscosity need to be in SUS (c) What is the head loss (HL), in units of psi, due to friction for a 95 feet length of pipe given system parameters in the problem statement?
3) If the flow in the 2.0 in. diameter pipe was expected to be laminar (Ng < 1399), the velocity was to be within pressure line velocity specifications (20 f/sec), and the specific gravity of the oil was 0.93. (a) What would the viscosity of the oil need to be in cS (b) What would the viscosity need to be in SUS (c) What is the head loss (HL), in units of psi, due to friction for a 95 feet length of pipe given system parameters in the problem statement?
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Transcribed Image Text:3)
If the flow in the 2.0 in. diameter pipe was expected to be laminar (Ng < 1399), the velocity was to
be within pressure line velocity specifications (20 f/sec), and the specific gravity of the oil was
0.93.
(a) What would the viscosity of the oil need to be in eS
(b) What would the viscosity need to be in SUS
(c) What is the head loss (HL), in units of psi, due to friction for a 95 feet length of pipe given
system parameters in the problem statement?
Vls ad
(d) What is the head loss (pressure drop) found in (e) above in kilopascals (kPa) ?
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