PERFORMANCE OF RADIAL FLOW VANELESS DIFFUSERS:
WITH DIVERGING WALLS
by
RATAN LAL GUPTA
Thesis submitted to the Indian Institute of Tecbnology,Delhi for the award of the Degree of
DOCTOR OF PHILOSOPHY
Department of Mechanical Engineering Indian Institute of chnology,Delhi
December, 1974
(1)
CERTIFICATE
This is to certify that the thesis entitled
"Performance of Radial Flow Vaneless Diffusers with Diverging Walls" being submitted by Mr. R.D. Gupta
to the Indian Institute of Technology, Delhi, for the award of the Degree of Doctor of Philosophy in Mechanical Engineering, is a record of bonafide research work carried out by him. He has worked under my guidance and has fulfilled the requirements for the submission of this thesis, which has reached
the requisite standard. 1)
The results contained in this thesis have not been submitted in part or in full, to any other University or Institute for the award of any degree or diploma.
( S.M. AHYA )
Mechanical Engineering Deptt.
Indian Institute of Technology New Delhi-110029.
ACKNOWLEDGEMENTS
It is with great pleasure that the author records his deep sense of gratitude to Dr. S.M. Yahya who sug- gested the research problem and ' supervised the work
reported in this thesis. Dr. Yahya's unceasing enthusiasm, fruitful discussions and constant encouragement inspired the author at all stages of this work.
Thanks are due to the staff of carpentary section, I.D.D.C. and Mechanical Workshop, in particular to
Mr: Karam Singh, for their efforts in fabricating a number of components for the experimental rig. Thanks are also due to the staff of Steam and Turbomac hinery Laboratory for their co-operation and help during the experimental work.
The support rendered by the Ministry of Education, Govt. of India, for the financial help under the scheme
of Quality Improvement Programme is gratefully acknow- ledged.
The author thanks all his friends who have helped in one way or the other.
Finally the thanks are due to Mr. V.P. Sharma who typed the manuscript.
N 0 TA TI ONS
A Area of cross-section at any section of the flow.
AR Area ratio = . A - 2 b Width of diffuser.
C Fluid velocity.
Cr,C9,Cx Velocity components in r-, 8-, and x directions.
CP = (p3-p2)/
ip 2 , pressure recovery coefficient.
AC Gain of pressure recovery over non-swirl. flow.
D Diameter of the pipe.
d Diffuser diameter.
f Friction coefficient.
g Acceleration due to gravity.
L Length of flow path of air.
N Speed of wire gauze rotor.
p Static pressure.
po S tagna ti on pressure.
R Gas constant.
R _ CX2.b2
e — , Reynolds number based on hydraulic mean diameter (2b).
r Radial distance.
T Static temperature.
To Stagnation temperature.
Axial distance measured across the width.
R kinematic viscosity.
P
Angle of divergence of the diffuser walls.
Angle between absolute velocity and tangen- tial component.
Density of air.
~po2- po3y PC22 , loss coefficient.
/1 - 1 , loss coefficient.
A2 R
Diffuser efficiency based on stagnation pressure loss.
Diffuser efficiency based on the static pressure rise.
SUBSCRIPTS
1. Entry to the test rig.
2. Entry to the diffuser.
3. Exit of the diffuser.
w At the diffuser wall.
SUPERSCRIPTS
- Average value.
Ideal value.
x
V
A a
1
d1T'd2
(v)
CONTENTS
CERTIFICATE ACKNOWLEDGEMENT NOTATIONS
CONTENTS
CHAPTER I IWJRODUCTION
1 .1 Definition and types 1 .2 Applications
1 .3 Flow process in a diffuser 1 .4 Brief history
1 .5 'The radial diffuser
1.6 Losses, pressure recovery and coefficients
1.7 Dimensional analysis CHAPTER II LITERATUREE SURVEY
2.1 Diffusers for hydraulic systems 2.2 Gas diffusers
2.2.1 'Pressure recovery coefficient 2.2.1.1 Effect of Reynolds number on
pressure recovery
2.2.1.2 Effect of boundary-layer on pressure recovery
2.2.1.3 Effect of swirl on pressure recovery
2.3 Incompressible flow analysis
1 1 3 3 4 8 9 11 13 . 13 14 22 22 23
23
24
3.4.4 Method of calculating friction
coefficient
59
CHAPTER IV EXPERIMENTAL RIG AND INSTRUMENTATION 61
4.1 Experimental rig 61
4.1 .1 Design and manufacture of the
diffusers .62
4.1 .2 Suction rings 67
4.1.3
Swirl generator68
4.2
Instrumentation 69
CHAPTER V EXPERIMENTS 71
5.1
Non-swirl tests72
5.1 .1
Diffuser A(Q= 2° ) 72
5.1 .2 Diffuser B(A = 30
)74
5.1 .3
Diffuser C (95°) 75
5.1 .4
Diffuser C4(0= 5
0)75
5.1 .5
Diffuser C-T(950
)75
5.2
Diffuser A-S(Q = 2°)75
5.3 Presentation
of'results 76
CHAPTER VI DISCUSSIONS 82
6.1 Non-swirl
tests 826.1 .1 Diffuser A(
=
2°) 826.1 .1 .1 Velocity profile 82
6.1 .1 .2 Pressure recovery 82
6.1.1.3 Efficiency 83
6.1.1.4
Loss coefficient84
6.1 ,1 .5
Comparison of loss coefficientsand efficiencies
85
6.1 .1 .6 Conclusions 86
6.1 .2 Diffuser B(8 = 30
) 87
6.1.2.1 Velocity profile 87
6.1.2.2 Pressure recovery
87
6.1.2.3 Efficiency 88
6.1.2.4 Loss coefficient
88
6.1 .2.5
Comparison of loss coefficientsand efficiencies 89
6.1.2.6 Conclusions 90
6.1 .3 Diffuser C (A = 50) 91
6.1 .3. Velocity profile 91
6.1.3.2
Pressure recovery 926.1.3.3 Efficiency 93
6.1.3.4 Loss coefficient 93.
6.1.3.5 Comparison of loss coefficients
and efficiencies 94
6.1.3.6 Conclusions
95
6.2 Swirl tests on diffuser A(ø = 2°) 96
6.2.1 Range of swirl angles .96
6.2.2 Velocity and swirl profiles at
diffuser entry 97
6.2.3 Pressure recovery C,, -98
6.2.4 Loss coefficient A 101
6.2.5 Efficiency i 103
6.2.6 Comparisons at Re =0.5,1.2 and
1.8X.105 105
6.2.7 Conclusions 106
6.3 Comparative performance of diffusers 108 6.3.1 Pressure and velocity profiles 108
6.3.2 Pressure recovery
C PR
1086.3.3 Loss coefficient & 112
6.3.4 Loss coefficient A 115
6.3.5
Efficiency 11d1 1176.3.6
Efficiency qd2 1176.3.7 Diffuser size 121
6.3.8 Friction coefficient 121
6.3.9
Comparison with other diffusers 123 CHAPTER VII CONCLUSIONS AND SUGGESTIONS FORFUTURE WORK 128
7.1 Main conclusions 128
7.2 Suggestions for future work 130
REFERENCES 131
APPENDIX 137