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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
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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
ASME MFC 3M 2004 R2017
$98.04