Fluid_Flow_Rules_of_Thumb_for_Chemical
18
Rules of Thumb for Chemical Engineers
Example sketch
Mw = Gas molecular weight P1,P2 = Inlet and outlet line pressures, psia Pc r i t - Critical pressure for sonic velocity to occur, psia T = Absolute temperature, ~ W = Gas flow rate, lb/hr Z - Gas compressibi l i ty factor
psv set @ 110 psig x 1.1 accumulation = 121 psig = 136 psia
/ .
/ .
15 psia
l
NC ~[
]
60 ~ 1O0 psig
Sources
lin
0
1. Mak, Henry Y., "New Method Speeds Pressure-Rel ief Manifold Design," Oil and Gas Journal, Nov. 20, 1978, p. 166. 2. API Recommended Practice 520, "Sizing, Selection, and Installation of Pressure Rel ieving Devices I Refineries," 1993. 3. "Flow of Fluids through Valves, Fittings, and Pipe," Crane Co. Technical paper 410, 1981. 4. Crocker, Sabin, Piping Handbook, McGraw-Hi l l , Inc., 1945. 5. Standing, M.B. and D. L. Katz, Trans. AIME, 146, 159 (1942).
200 equiv, ft
C1
300 psig = 315 psia 60 ~
Nomenclature
D = Pipe diameter, ft d - Pipe diameter, in f = Moody friction factor L = Line equivalent length, ft M1,M2 = Mach number at the line inlet, outlet
CompressibleFlow--Long Pipelines
Equations CommonlyUsed for Calculating Hydraulic Data for Gas Pipe Lines
Weymouth.
0.5 Q- 433.5x (Yb/Pb)XI p12GLTz-p22 I X D2"667 x E
Panhandle A.
Qb 435.87 x (TB/PB)1"0778 D2.6182 - x x E x
Pavg -- 2/3[P~ + P2 - (P1 x P2)/1:'1 + P2]
pl 2 _ p2 2 _ 0.0375 x G x (h2 - hi) M Pavg2 0.5394 Tavg X Zavg 6 0.8539 • L x Tavg x Zavg
Pavg is used to calculate gas compressibi l i ty factor Z
Nomenclature for Panhandle Equations
Qb = f l ow r a t e , SCFD P b - base pressure, psia Tb " - b a s e temperature, ~ Tavg = average gas temperature, ~
Panhandle B.
P1 = inlet pressure, psia P2 - outlet pressure, psia G = gas specific gravity (air = 1.0) L = line length, miles Z = average gas compressibi l i ty D = pipe inside diameter, in. h2 - elevation at terminus of line, ft
Qb 737 X (Tb/Pb)L~176 - X D 2s3 • E
_ 0.0375 x G x (h2 - hi) x Pavg2 0.51
pl 2 _ p22
Tavg X Zavg 6 0"961X L x Tavgx Zavg
x
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