ASME MFC 3M 2004 R2017
$98.04
ASME MFC-3M-2004-R2017 Measurement of Fluid Flow in Pipes Using Orifice, Nozzle, and Venturi
Published By | Publication Date | Number of Pages |
ASME | 2004 | 96 |
This Standard specifies the geometry and method of use (installation and flowing conditions) for orifice plates, nozzles, and Venturi tubes when they are inserted in a conduit running full, to determine the rate of the fluid flowing. It also gives necessary information for calculating flow rate and its associated uncertainty. It applies only to pressure difference devices in which the flow remains turbulent and subsonic throughout the measuring section is steady or varies only slowly with time and the fluid is considered single-phased. In addition, the uncertainties are given in the appropriate sections of this Standard for each of these devices, within the pipe size and Reynolds number limits which are specified. It deals with devices for which sufficient calibrations have been made to enable the specification of coherent systems of application and to enable calculations to be made with certain predictable limits of uncertainty. The devices introduced into the pipe are called primary devices. The term primary device also includes the pressure taps and the associated upstream and downstream piping. All other instruments or devices required for the measurement or transmission of the differential pressures are known as secondary elements, and in combination are referred to as the secondary devices. This Standard covers the primary devices; secondary devices will be mentioned only occasionally. The following primary devices are covered in this Standard: (a) orifice plates, which can be used with the following arrangements of pressure taps: (1) flange pressure taps, (2) D and D/2 pressure taps, (3) corner pressure taps. (b) nozzles: (1) ASME long radius nozzles. (c) Venturi tubes: (1) classical Venturi tubes. This Standard does not pipe or conduit sizes under 50 mm {2 in.} nominal. This Standard does not apply to ASME Performance Test Code measurements. The Standard is applicable to measurement of flow of any fluid, (liquid, vapor, or gas).
PDF Catalog
PDF Pages | PDF Title |
---|---|
5 | CONTENTS Part 1 Nonmandatory Appendices Part 2 Figures Part 2 Tables |
6 | Part 3 Figures Part 3 Tables Part 4 Figures Part 4 Nonmandatory Appendices |
7 | FOREWORD |
8 | COMMITTEE ROSTER |
9 | CORRESPONDENCE WITH THE MFC COMMITTEE |
11 | Part 1 General 1-1 SCOPE AND APPLICATION 1-2 REFERENCES AND RELATED DOCUMENTS |
12 | 1-3 SYMBOLS AND DEFINITIONS |
13 | Part 1 Table 1-1 Symbols |
15 | 1-4 PRINCIPLES OF THE METHOD OF MEASUREMENT AND COMPUTATION |
16 | 1-5 GENERAL REQUIREMENTS FOR MEASUREMENT Part 1 Figure 1-1 “Triple-T” Arrangement |
17 | 1-6 INSTALLATION REQUIREMENTS |
19 | 1-7 UNCERTAINTIES IN THE MEASUREMENT OF FLOW RATE |
21 | 1A ITERATIVE COMPUTATIONS |
22 | 1B EXAMPLES OF VALUES OF PIPE WALL UNIFORM EQUIVALENT ROUGHNESS, k |
23 | 1C FLOW CONDITIONERS AND FLOW STRAIGHTENERS |
28 | Part 2 Orifice Plates 2-1 SCOPE AND FIELD OF APPLICATION 2-2 REFERENCES AND RELATED DOCUMENTS |
29 | 2-3 PRINCIPLES OF THE METHOD OF MEASUREMENT AND COMPUTATION 2-4 ORIFICE PLATES 2-1 Standard Orifice Plate |
30 | 2-2 Orifice Plate Flatness Measurement |
32 | 2-3 Spacing of Pressure Taps for Orifice Plates With D and D/2 Pressure Taps or Flange Taps |
33 | 2-4 Corner Taps |
34 | 2-1 Maximum Value of 104 Ra/D 2-2 Minimum Value of 104 Ra/D (When Required) |
36 | 2-5 INSTALLATION REQUIREMENTS |
37 | 2-3 Spacing of Pressure Taps for Orifice Plates with D and D/2 Pressure Taps or Flange Taps |
38 | 2-5 Layout Including a Full Bore Valve for � � 0.6 |
40 | 2-6 Examples of Acceptable Installations |
41 | 2-7 19-Tube Bundle Flow Straightener |
42 | 2-4 Permitted Range of Straight Lengths Between Orifice Plate and 19-Tube Bundle Flow Straightener (1998) Downstream of Fittings Located at Distance, Lf, From the Orifice Plate |
43 | 2-8 Examples of Installations With a 19-Tube Bundle Flow Straightener Downstream of a Single Bend |
44 | 2-9 Zanker Flow Conditioner Plate |
47 | Part 2 Nonmandatory Appendix 2A TABLES OF DISCHARGE COEFFICIENTS AND EXPANSIBILITY FACTORS |
59 | Part 3 Nozzles and Venturi Nozzles 3-1 SCOPE AND FIELD OF APPLICATION 3-2 REFERENCES AND RELATED DOCUMENTS 3-3 PRINCIPLES OF THE METHOD OF MEASUREMENT AND COMPUTATION |
60 | 3-4 NOZZLES AND VENTURI NOZZLES 3-1 ISA 1932 Nozzle |
62 | 3-1 Upper Limits of Relative Roughness of the Upstream Pipe for ISA 1932 Nozzles |
64 | 3-2 Long Radius Nozzles |
66 | 3-3 Venturi Nozzle |
68 | 3-4 Venturi Nozzle, Pressure Taps 3-2 Upper Limits of Relative Roughness of the Upstream Pipe for Venturi Nozzles |
69 | 3-5 INSTALLATION REQUIREMENTS 3-5 Pressure Loss Across a Venturi Nozzle |
70 | 3-3 Required Straight Lengths for Nozzles and Venturi Nozzles |
72 | 3-6 Layout Including a Full Bore Valve for � � 0.6 |
73 | 3-7 Examples of Acceptable Installations |
75 | Part 3 Nonmandatory Appendix 3A TABLES OF DISCHARGE COEFFICIENTS AND EXPANSIBILITY FACTORS |
78 | Part 4 Venturi Meters 4-1 SCOPE AND FIELD OF APPLICATION 4-2 REFERENCES AND RELATED DOCUMENTS 4-3 PRINCIPLES OF THE METHOD OF MEASUREMENT AND COMPUTATION |
79 | 4-4 ASME VENTURI TUBES |
80 | 4-1 Geometric Profile of the ASME Venturi Tube |
84 | 4-5 INSTALLATION REQUIREMENTS 4-2 Pressure Loss Across an ASME Venturi Tube |
85 | Part 4 Table 4-1 Required Straight Lengths for Classical Venturi Tubes |
86 | 4-3 Layout Including a Full Bore Valve for � � 0.6 |
87 | 4-4 Examples of Acceptable Installations |
89 | 4A TABLE OF EXPANSIBILITY FACTORS |
90 | 4B ASME VENTURI METERS USED OUTSIDE THE SCOPE OF MFC-3M-2004 |
92 | 4C PRESSURE LOSS IN ASME VENTURI METERS |