Saved calculations: 

LINE DETAILS
 
Line number
Source
Destination
 
 
FLOW TYPE
 
Type of flow
 
 
FLUID PROPERTIES
 
Fluid
Flowrate m
Inlet density ρ1
Viscosity μ
Inlet temperature T1
Inlet pressure P1
Ratio of specific heat capacities γ
 
 
PIPELINE
 
Pipe nominal diameter inch
Pipe schedule
Pipe internal diameter d
6.8
mm
Pipe length L
Absolute roughness e
 
 
FITTINGS
 
  Quantity
90° LR bends
90° Std elbows
45° LR bends
45° Std elbows
Straight tees (flow thro' run)
Straight tees (flow thro' branch)
Pipe entrances
Pipe exits
Pipe contractions
Pipe expansions
Gate valves
Globe valves
Swing check valves
Lift check valves
Tilting disc check valves
Stop check valves
Poppet foot valves (with strainers)
Hinged disc foot valves (with strainers)
Ball valves
Butterfly valves
Plug valves
 
Miscellaneous losses (no. of velocity heads)
 
Fittings factor
 
 
OUTPUTS
 
Relative roughness e:d 0.00676
Flow area A 0.00004
Reynolds No. Re 5201
Flow regime turbulent
Friction factor f 0.04514
Pipe velocity head loss Kpipe 0.000
Fittings total velocity head loss Kfittings 0.000
 
 
  Inlet Outlet
Mach number Mach 0.0014 0.0029
Temperature T 20.0 20.0
Density ρ 10.0000 5.0000
Volumetric flow rate Q 0.0000 0.0001
Velocity u 0.76 1.53
Pressure P 2000000.0 1000000.0
Critical velocity ucritical 529.15 529.15
Choked flow? NO NO
 
 
Outlet pressure P2 10.00
Pressure drop through pipe ΔP 10.00


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