CDS - DELTA-P CALCULATIONS FOR SINGLE AND MULTI-PHASE FLOWS

Flow type: 1

Input Values for Single Phase Flow:0.00E+00 0

Relative Rougness of the pipe mm 0.00E+00Pipe inside diameter mm 0.00E+00

Density of the fluid kg/m3 0Viscosity of the fluid cP 0

Mass flow rate of the fluid kg/hr 0

CDS - DELTA-P CALCULATIONS FOR SINGLE AND MULTI-PHASE FLOWSSingle phaseSingle phaseMulti-phase

Relative Rougness of the pipePipe inside diameter

Density of the fluid0.00E+00 0

0.00E+00 Viscosity of the fluid0.00E+00 Mass flow rate of the fluid

0 0 0 0 0 Pipe inside diameter0 Viscosity of the liquid0 Mass flow rate of the vapour

Mass flow rate of the liquidDensity of the liquid

Density of the vapourSurface tension of liquid

Viscosity of the vapour

CDS - DELTA-P CALCULATIONS FOR SINGLE AND MULTI-PHASE FLOWS

E = 0 E = 0Velocity, U = #DIV/0! ft/sec (pro V)^.5 = 0

Reynold's No. , Nre = #DIV/0! N/A Bx = #DIV/0!A = #DIV/0! (pro V*pro L)^.5 = 0B = #DIV/0! By = #DIV/0!

Friction factor, f = #DIV/0! Avg. fluid density, D = #DIV/0! lb/ft3Pressure drop, P = #DIV/0! psi/100 ft. of pipe Total flow rate, Q = 0 lb/hr

Flow regime is #DIV/0!Velocity, U = #DIV/0! ft/sec

Prssure Drop = #DIV/0! psi/100 ft. of pipePhi SQ = #DIV/0!

Selection of regimeCond 1Cond 2

Dispersed/Annular/Slug/Bubble Cond 3D = 0 Now, Cond 4Q = 0 H = #DIV/0!E = 0 D = 0 Delta P =U = #DIV/0! Q = 0

Nre = #DIV/0! V = 0A = #DIV/0! U = #DIV/0!B = #DIV/0! Nre = #DIV/0! SlugW = #DIV/0! A = #DIV/0! M = #DIV/0!P = #DIV/0! B = #DIV/0! C = #DIV/0!

W = #DIV/0!P = #DIV/0!T = #DIV/0!

Dispersed Z = #DIV/0! AnnularZ=<.1 Z=<.5 Else I<=10

M = #DIV/0! M = #DIV/0! M = 9.445 M = #DIV/0!Since Z = #DIV/0! Thus, M = #DIV/0! For I = 0

C = #DIV/0! C =

CDS - DELTA-P CALCULATIONS FOR SINGLE AND MULTI-PHASE FLOWS

psi/100 ft. of pipe

#DIV/0!#DIV/0!#DIV/0!#DIV/0!

#DIV/0! psi

BubbleM = #DIV/0!C = #DIV/0!

AnnularElseM = #DIV/0!

Thus, M = #DIV/0!

#DIV/0!

CDS - DELTA-P CALCULATIONS FOR SINGLE AND MULTI-PHASE FLOWS

CDS - DELTA-P CALCULATIONS FOR SINGLE AND MULTI-PHASE FLOWS