In a venturi nozzle flow, the inlet conditions are p1 = 08 x 103 kPa gauge and d1 = 100 mm and the outlet conditions are p2 = 0 kPa gauge and d2 = 50 mm. Find the flow rate of water. Assume CD = 0.98 for the venturi coefficient. a)  Neglect viscous effects (friction loss). b)  Consider viscous effects.

Structural Analysis
6th Edition
ISBN:9781337630931
Author:KASSIMALI, Aslam.
Publisher:KASSIMALI, Aslam.
Chapter2: Loads On Structures
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In a venturi nozzle flow, the inlet conditions are p1 = 08 x 103 kPa gauge and d1 = 100 mm and the outlet conditions are p2 = 0 kPa gauge and d2 = 50 mm. Find the flow rate of water. Assume CD = 0.98 for the venturi coefficient.

  1. a)  Neglect viscous effects (friction loss).
  2. b)  Consider viscous effects.

 

.10
.09
.08
Laminar
Kritik
Gecis
Bilgesi
Alam
Bülge
Tam türbülans, Pūrūzlü boru
.07
.05
.04
.06
.03
.05
.02
Luminar
Akım
.015
-64/Re
.04
.01
.008 e
.006
.03
004
.003
.002
.0015
.02
.001
.0008
.0006
.0004
.015
Düz Borular
.0003
.0002
.00015
.0001
.00006
.00004
.00003
.01
.009
,00002
.000015
.00001
3 4 56 B 10
.008
103
2 3 4 56 B 10
2 3 4 5 6 8 105
2 3 45 6
R 106
2 3 4 56 8 107
2
Reynolds Suyısı, Re- v.D/v
Relutif Plirtizsüzlük, s/D
Transcribed Image Text:.10 .09 .08 Laminar Kritik Gecis Bilgesi Alam Bülge Tam türbülans, Pūrūzlü boru .07 .05 .04 .06 .03 .05 .02 Luminar Akım .015 -64/Re .04 .01 .008 e .006 .03 004 .003 .002 .0015 .02 .001 .0008 .0006 .0004 .015 Düz Borular .0003 .0002 .00015 .0001 .00006 .00004 .00003 .01 .009 ,00002 .000015 .00001 3 4 56 B 10 .008 103 2 3 4 56 B 10 2 3 4 5 6 8 105 2 3 45 6 R 106 2 3 4 56 8 107 2 Reynolds Suyısı, Re- v.D/v Relutif Plirtizsüzlük, s/D
1
(2)
V2
Flow through the nozzle
Transcribed Image Text:1 (2) V2 Flow through the nozzle
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