Reader-Harris Orifice Plates and Venturi Tubes
1. Auflage 2015
ISBN: 978-3-319-16880-7
Verlag: Springer International Publishing
Format: PDF
Kopierschutz: 1 - PDF Watermark
E-Book, Englisch, 393 Seiten
Reihe: Experimental Fluid Mechanics
ISBN: 978-3-319-16880-7
Verlag: Springer International Publishing
Format: PDF
Kopierschutz: 1 - PDF Watermark
Zielgruppe
Professional/practitioner
Autoren/Hrsg.
Weitere Infos & Material
1;Preface;6
2;Contents;8
3;Notations;15
4;1 Introduction and History;19
4.1;Abstract;19
4.2;1.1 Introduction;19
4.3;1.2 Theory;20
4.3.1;1.2.1 Bernoulli's Theorem;20
4.3.2;1.2.2 Method of Operation;21
4.3.2.1;1.2.2.1 General;21
4.3.2.2;1.2.2.2 Incompressible Flow;21
4.3.2.3;1.2.2.3 Compressible Flow;22
4.3.2.4;1.2.2.4 Equation for Practical Use;24
4.4;1.3 Essential Requirements;25
4.4.1;1.3.1 General;25
4.4.2;1.3.2 With a Calibration in a Flowing Fluid;25
4.4.3;1.3.3 Without a Calibration in a Flowing Fluid;26
4.5;1.4 Introduction to Reynolds Number and Velocity Profile;26
4.6;1.5 Pipe Roughness;29
4.7;1.6 Accuracy;30
4.8;1.7 Pressure Loss;31
4.9;1.8 Standards;32
4.10;1.9 Advantages and Disadvantages;32
4.11;1.10 History;33
4.12;1.11 Conclusions;40
4.13;Appendix 1.A: Sextus Julius Frontinus;41
4.14;References;46
5;2 Orifice Design;50
5.1;Abstract;50
5.2;2.1 Introduction;50
5.3;2.2 Orifice Plate;51
5.3.1;2.2.1 General;51
5.3.2;2.2.2 Flatness;53
5.3.3;2.2.3 Surface Condition of the Upstream Face of the Plate;54
5.3.4;2.2.4 Edge Sharpness;56
5.3.5;2.2.5 Plate Thickness E and Orifice (Bore) Thickness e;58
5.3.5.1;2.2.5.1 General;58
5.3.5.2;2.2.5.2 Plate Thickness E;58
5.3.5.3;2.2.5.3 Orifice (Bore) Thickness e;59
5.3.5.4;2.2.5.4 Requirements;61
5.3.6;2.2.6 Circularity;62
5.4;2.3 The Pipe;62
5.4.1;2.3.1 General;62
5.4.2;2.3.2 Pressure Tappings;63
5.4.2.1;2.3.2.1 General;63
5.4.2.2;2.3.2.2 Flange and D and D/2 Tappings;63
5.4.2.2.1;General;63
5.4.2.2.2;Tapping Diameter;65
5.4.2.2.3;Tapping Location;65
5.4.2.3;2.3.2.3 Corner Tappings;67
5.4.2.4;2.3.2.4 Number of Tappings;67
5.4.3;2.3.3 Pipe Roughness;68
5.4.3.1;2.3.3.1 Uniform Roughness;68
5.4.3.2;2.3.3.2 Rough Pipes with a Smooth Portion Immediately Upstream of the Orifice;71
5.4.3.3;2.3.3.3 Non-uniform Roughness;72
5.4.4;2.3.4 Steps and Misalignment;74
5.4.5;2.3.5 Eccentricity;76
5.5;2.4 Dimensional Measurements;77
5.6;2.5 Orifice Fittings;78
5.7;2.6 Pressure Loss;79
5.8;2.7 Reversed Orifice Plates;82
5.9;2.8 Conclusions;84
5.10;Appendix 2.A: Orifice Plates of Small Orifice Diameter;85
5.10.1;2.A.1 Introduction and Test Work;85
5.10.2;2.A.2 Conclusions;89
5.11;References;90
6;3 Venturi Tube Design;94
6.1;Abstract;94
6.2;3.1 Introduction;94
6.3;3.2 Type;96
6.3.1;3.2.1 General;96
6.3.2;3.2.2 Machined Convergent (5.2.9, 5.5.3 and 5.7.2 of ISO 5167-4:2003);97
6.3.3;3.2.3 Rough-Welded Sheet-Iron Convergent (5.2.10, 5.5.4 and 5.7.3 of ISO 5167-4:2003);97
6.3.4;3.2.4 `As Cast' Convergent (5.2.8, 5.5.2 and 5.7.1 of ISO 5167-4:2003);97
6.3.5;3.2.5 Wider Range of Reynolds Number;98
6.4;3.3 Angles, Pressure Loss and Truncation;98
6.5;3.4 Dimensional Measurements;100
6.6;3.5 Steps and Straightness;101
6.7;3.6 Pressure Tappings;102
6.8;3.7 Effects of Roughness and Reynolds Number;104
6.9;3.8 High or Low Reynolds Number;104
6.10;3.9 Conclusions;107
6.11;Appendix 3.A:‚Effect of Roughness: Computational Fluid Dynamics;107
6.11.1;3.A.1 General;107
6.11.2;3.A.2 Venturi Tube Roughness;107
6.11.2.1;3.A.2.1 Effect of Venturi Tube Roughness Height;107
6.11.2.2;3.A.2.2 Effect of Reynolds Number;108
6.11.2.3;3.A.2.3 Effect of Venturi Tube Roughness Type;108
6.11.3;3.A.3 Pipe Roughness;109
6.11.4;3.A.4 Effect of Rounding the Corner Between the Convergent Section and the Throat;110
6.12;References;112
7;4 General Design;114
7.1;Abstract;114
7.2;4.1 Introduction;114
7.3;4.2 Impulse Lines;114
7.3.1;4.2.1 General;114
7.3.2;4.2.2 Tapping Locations and Slopes of Impulse Lines;116
7.3.3;4.2.3 Density of the Fluids in Two Impulse Lines to Measure the Differential Pressure;118
7.3.4;4.2.4 Length of Impulse Lines;121
7.3.5;4.2.5 Blockage;122
7.3.6;4.2.6 Damping of the Pressure Signal or Resonance;123
7.4;4.3 Differential Pressure;123
7.4.1;4.3.1 Differential-Pressure Transmitters;123
7.4.2;4.3.2 Piezometer Rings;126
7.5;4.4 Static Pressure;127
7.6;4.5 Drain and Vent Holes (Through the Pipe Wall);128
7.7;4.6 Temperature;128
7.7.1;4.6.1 General;128
7.7.2;4.6.2 Temperature Correction from Downstream of the Flowmeter to Upstream of It;129
7.7.3;4.6.3 Using a Densitometer;132
7.7.4;4.6.4 Correction of Dimensions for Temperature;133
7.8;4.7 Iteration;134
7.9;4.8 Uncertainty;134
7.10;4.9 Cavitation;135
7.11;4.10 Diagnostics;135
7.12;4.11 Mixtures;136
7.13;4.12 Conclusions;137
7.14;Appendix 4.A: Impulse Lines in Pulsating Flows;137
7.15;Appendix 4.B:‚Measuring Low Differential Pressure at High Static Pressure;140
7.15.1;4.B.1‚Introduction;140
7.15.2;4.B.2‚The Problem;140
7.15.3;4.B.3‚A Possible Solution;140
7.16;References;141
8;5 Orifice Discharge Coefficient;143
8.1;Abstract;143
8.2;5.1 Introduction;143
8.3;5.2 History;144
8.4;5.3 The EEC/API Database;147
8.5;5.4 The Equation;150
8.5.1;5.4.1 Introduction;150
8.5.2;5.4.2 The Tapping Terms;150
8.5.2.1;5.4.2.1 Introduction;150
8.5.2.2;5.4.2.2 High Reynolds Number Tapping Terms;152
8.5.2.2.1;Total Tapping Terms;152
8.5.2.2.2;Upstream Term;152
8.5.2.2.3;Downstream Term;154
8.5.2.3;5.4.2.3 Low Reynolds Number Tapping Terms;156
8.5.3;5.4.3 The C221E and Slope Terms;160
8.5.4;5.4.4 A Term for Small Orifice Meters;162
8.5.5;5.4.5 The Complete Equation;163
8.6;5.5 Quality of Fit;164
8.7;5.6 Equations and Comparison Between Them on the Basis of Deviations;171
8.7.1;5.6.1 The Reader-Harris/Gallagher (RG) Equation as in API 14.3.1:1990;171
8.7.2;5.6.2 The Stolz Equation in ISO 5167:1980;172
8.7.3;5.6.3 Comparisons;172
8.8;5.7 Uncertainty;175
8.9;5.8 Conclusions;179
8.10;Appendix 5.A: Better Options for Tapping Terms;179
8.11;Appendix 5.B: Small Orifice Diameters Within the EEC/API Database;183
8.12;Appendix 5.C: The PR14 Equation and an Equation in Terms of Friction Factor;186
8.12.1;5.C.1 The PR14 Equation;186
8.12.2;5.C.2 An Equation in Terms of Friction Factor;187
8.13;Appendix 5.D: The Effect on the Discharge-Coefficient Equation of Changing the Expansibility-Factor Equation;188
8.14;Appendix 5.E: Orifice Plates in Pipes of Small Diameter or with No Upstream or with No Downstream Pipeline or with No Upstream and No Downstream Pipeline;191
8.14.1;5.E.1 Introduction;191
8.14.2;5.E.2 Orifice Plates in Pipes of Small Diameter;191
8.14.3;5.E.3 Orifice Plates with No Upstream or Downstream Pipeline;192
8.14.4;5.E.4 Orifice Plates with No Upstream Pipeline;194
8.14.5;5.E.5 Orifice Plates with No Downstream Pipeline;195
8.15;Appendix 5.F: Lower Reynolds Number Limit for the Reader-Harris/Gallagher (1998) Equation;197
8.16;References;199
9;6 Orifice Expansibility Factor;203
9.1;Abstract;203
9.2;6.1 Introduction;203
9.3;6.2 History and Theory;204
9.4;6.3 The Database;205
9.5;6.4 Analysis;206
9.6;6.5 Theoretical Model;211
9.7;6.6 Subsequent Work;214
9.8;6.7 Conclusions;215
9.9;Appendix 6.A: Data Taken with a Flow Conditioner 7D or 10D from the Orifice Plate;215
9.10;References;216
10;7 Venturi Tube Discharge Coefficient in High-Pressure Gas;218
10.1;Abstract;218
10.2;7.1 Introduction;218
10.3;7.2 Experimental Work: Standard Shape;219
10.3.1;7.2.1 Description of the Venturi Tubes;219
10.3.2;7.2.2 Calibration in Water;220
10.3.3;7.2.3 Calibration in Gas;221
10.4;7.3 Interpretation and Analysis of Data;224
10.4.1;7.3.1 Static-Hole Error;224
10.4.2;7.3.2 Measurements of Static-Hole Error at High Tapping-Hole Reynolds Number;225
10.4.3;7.3.3 Measurements of Static-Hole Error at Low Tapping-Hole Reynolds Number;226
10.4.4;7.3.4 The Effect of Tapping Depth on Static-Hole Error;227
10.4.5;7.3.5 The Effect of Tapping Shape on Static-Hole Error;229
10.4.6;7.3.6 The Effect of a Burr or a Protruding Tapping on Static-Hole Error;229
10.4.7;7.3.7 Analysis of the Gas Data in Sect. 7.2.3;229
10.4.8;7.3.8 Conclusions to Sect. 7.3;230
10.5;7.4 Improved Shape;232
10.5.1;7.4.1 General;232
10.5.2;7.4.2 Venturi Tube with Convergent Angle 10.5?;232
10.5.3;7.4.3 The Discharge-Coefficient Equation for Venturi Tubes with Convergent Angle 10.5?;234
10.6;7.5 Conclusions;236
10.7;Appendix 7.A: Shape of Venturi Tubes: Tests at NEL;236
10.7.1;7.A.1 Design;236
10.7.2;7.A.2 Calibration in Water;239
10.7.3;7.A.3 Calibration in Gas;239
10.7.4;7.A.4 Analysis;239
10.7.5;7.A.5 Conclusions on Shape from the 42033 Venturi Tubes;247
10.7.6;7.A.6 Manufacture of Additional Venturi Tubes with 10.5? Convergent Angle and Sharp Corners;247
10.7.7;7.A.7 Calibration of Additional Venturi Tubes in Water and in Gas;248
10.8;Appendix 7.B: Depth of Tappings: Tests at NEL;252
10.9;Appendix 7.C: Refitting the Data With Convergent Angle 10.5?;254
10.10;References;257
11;8 Installation Effects;259
11.1;Abstract;259
11.2;8.1 Introduction;259
11.3;8.2 Upstream Straight Lengths;260
11.3.1;8.2.1 General;260
11.3.2;8.2.2 Definitions;262
11.3.3;8.2.3 Orifice Plates;262
11.3.3.1;8.2.3.1 History;262
11.3.3.2;8.2.3.2 The Pattern of the Data;262
11.3.3.3;8.2.3.3 The Straight Lengths in ISO 5167-2:2003;267
11.3.4;8.2.4 Venturi Tubes;269
11.3.4.1;8.2.4.1 Standard Venturi Tubes;269
11.3.4.1.1;General;269
11.3.4.1.2;Calibrations Downstream of a Contraction and an Expansion;270
11.3.4.1.3;Calibrations Downstream of Bends;270
11.3.4.1.4;Analysis;273
11.3.4.2;8.2.4.2 Venturi Tubes with Convergent Angle 10.5?;274
11.3.5;8.2.5 What to Do if a Case is not Covered in Table 3 of ISO 5167-2:2003/Table 1 of ISO 5167-4:2003;276
11.3.5.1;8.2.5.1 General;276
11.3.5.2;8.2.5.2 The Upstream Installation is a Combination of Fittings;276
11.3.5.3;8.2.5.3 A Flow Conditioner Is Used;277
11.3.5.3.1;General;277
11.3.5.3.2;With an Orifice Plate;278
11.3.5.3.3;With a Venturi Tube;282
11.3.5.3.4;Damage to Flow Conditioners;284
11.3.5.4;8.2.5.4 A Specific Test Is Done;284
11.3.5.5;8.2.5.5 CFD is Carried Out;285
11.3.5.6;8.2.5.6 Engineering Judgement is Employed;285
11.4;8.3 Downstream Straight Length;286
11.4.1;8.3.1 Orifice Plates;286
11.4.2;8.3.2 Venturi Tubes;286
11.5;8.4 Pulsations;287
11.5.1;8.4.1 General;287
11.5.2;8.4.2 Orifice Plates;288
11.5.3;8.4.3 Venturi Tubes;288
11.6;8.5 Conclusions;288
11.7;Appendix 8.A: Swirl Decay;289
11.8;References;289
12;9 Nozzle Discharge Coefficient;295
12.1;Abstract;295
12.2;9.1 Introduction;295
12.3;9.2 Manufacture;297
12.3.1;9.2.1 General;297
12.3.2;9.2.2 Pipework and Nozzles;298
12.3.3;9.2.3 Nozzle Tappings;298
12.3.4;9.2.4 Wall Tappings;300
12.4;9.3 Data;300
12.5;9.4 Wall-Tapping Data: Analysis;301
12.6;9.5 Throat-Tapping Data: Initial Analysis;305
12.7;9.6 Hot-Water (NMIJ Throat-Tapping) Data;309
12.8;9.7 Throat-Tapping Data: Further Analysis;310
12.8.1;9.7.1 General;310
12.8.2;9.7.2 Analysis of NMIJ Data;312
12.8.3;9.7.3 Application to NEL Data;313
12.8.4;9.7.4 Analysis of NEL Data;315
12.9;9.8 Conclusions;316
12.10;References;317
13;10 Orifice Plates with Drain Holes;319
13.1;Abstract;319
13.2;10.1 Introduction;319
13.3;10.2 Experimental Work: Initial Data;322
13.4;10.3 Experimental Work: Additional Data;327
13.5;10.4 Analysis;330
13.5.1;10.4.1 Bernoulli's Theorem;330
13.5.2;10.4.2 Pressure Tapping Location for Flow Measurement Without Error;332
13.5.3;10.4.3 An Equation for the Corrected Diameter;334
13.5.4;10.4.4 Practical Equations for the Corrected Diameter;338
13.6;10.5 Conclusions;339
13.7;References;339
14;11 Wet Gas;341
14.1;Abstract;341
14.2;11.1 Introduction;341
14.3;11.2 Fundamental Equations;343
14.3.1;11.2.1 General;343
14.3.2;11.2.2 Laboratory Test Work;344
14.3.3;11.2.3 Models for Field Use;344
14.3.3.1;11.2.3.1 General;344
14.3.3.2;11.2.3.2 Venturi Tube;345
14.3.3.2.1;General;345
14.3.3.2.2;de Leeuw Equation;345
14.3.3.2.3;ISO/TR 11583:2012 Correlation;345
14.3.3.3;11.2.3.3 Orifice Plate;346
14.3.4;11.2.4 Methods to Obtain the Lockhart-Martinelli Parameter, X (Eq. 11.2);347
14.3.4.1;11.2.4.1 General;347
14.3.4.2;11.2.4.2 Pressure Loss Ratio;348
14.3.4.2.1;Venturi Tube;348
14.3.4.2.2;Orifice Plate;349
14.4;11.3 Venturi Tubes;350
14.4.1;11.3.1 Over-Reading Equations;350
14.4.1.1;11.3.1.1 Derivation of the ISO/TR 11583:2012 Correlation;350
14.4.1.2;11.3.1.2 Comparison with the de Leeuw Equation;357
14.4.1.3;11.3.1.3 Possible Improvement of the ISO/TR 11583:2012 Correlation;357
14.4.2;11.3.2 Using Pressure-Loss Measurements;361
14.4.3;11.3.3 Mixtures of Liquids;365
14.5;11.4 Orifice Plates;367
14.5.1;11.4.1 General;367
14.5.2;11.4.2 Derivation of the Equations in ISO/TR 11583:2012;367
14.5.3;11.4.3 Subsequent Work;371
14.6;11.5 Conclusions;371
14.7;Appendix 11.A: A Brief History of ISO/TR 11583;372
14.8;Appendix 11.B: Dependence of the Wet-Gas Correlations for Venturi Tubes on Liquid Viscosity;375
14.8.1;11.B.1 General;375
14.8.2;11.B.2 Deviations from the ISO/TR 11583:2012 Correlation;375
14.8.3;11.B.3 Deviations from the de Leeuw Equation;378
14.8.4;11.B.4 Errors Using ISO/TR 11583:2012 with X Determined from the Pressure Loss Ratio;380
14.8.5;11.B.5 Analysis;380
14.8.6;11.B.6 Horizontal Tappings;388
14.9;References;388
15;12 Standards;390
15.1;Abstract;390
15.2;12.1 Introduction;390
15.3;12.2 ISO Standards;391
15.4;12.3 ISO/TC 30 Measurement of Fluid Flow in Closed Conduits;392
15.4.1;12.3.1 General;392
15.4.2;12.3.2 ISO/TC 30/SC 2 Pressure Differential Methods;392
15.4.2.1;12.3.2.1 General;392
15.4.2.2;12.3.2.2 Differential-Pressure Flow Measurement Standards: ISO 5167 Etc.;393
15.4.2.3;12.3.2.3 ISO/TR 9464 Guidelines for Using ISO 5167;395
15.4.2.4;12.3.2.4 ISO/TR 12767 Differential-Pressure Meters Departing from ISO 5167;395
15.4.2.5;12.3.2.5 ISO/TR 15377 Differential-Pressure Meters Beyond the Scope of ISO 5167;396
15.4.2.6;12.3.2.6 ISO/TR 3313 Pulsating Flow;396
15.4.2.7;12.3.2.7 ISO/TR 11583 Wet Gas;397
15.4.2.8;12.3.2.8 ISO 2186 Impulse Lines;397
15.4.2.9;12.3.2.9 Priorities for the Future as Seen in 2014;397
15.4.3;12.3.3 The TC Itself;398
15.4.3.1;12.3.3.1 General;398
15.4.3.2;12.3.3.2 Priorities for the Future as Seen in 2014;399
15.5;12.4 AGA/API Standards;399
15.6;12.5 Conclusions;400
15.7;Appendix 12.A: The Standards of ISO/TC 30/SC 2;400
15.8;References;401
16;Index;402




