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ASME MFC 3M 1989

$98.04

ASME MFC-3M – 1989 Measurement of Fluid Flow in Pipes Using Orifice, Nozzle and Venturi

Published By Publication Date Number of Pages
ASME 1989 75
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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
4 Foreword
5 Standards Committee Roster
6 CONTENTS
9 1 Scope and Field of Application
10 2 References
3 Symbols and Definitions
3.1 Symbols
3.2 Definitions
11 Tables
1 symbols
18 4 Principle of Measurement and the Method of Computation
4.1 Principle of Measurement
19 4.2 Method of Sizing the Bore of the Selected Primary Element
20 4.3 Computation of Flow Rate
4.4 Determination of Gas (Vapor) Density
21 5 General Measurement Requirements
5.1 Primary Device
5.2 Type of Fluid
5.3 Flow Conditions
22 6 Installation Requirements
6.1 General
23 2 Recommended Straight Lengths for Nozzles and Orifice Plates for 0.5% Additional Uncertainty
24 6.2 Specific Installation Requirements for Orifice Plates
25 6.3 Upstream Length
6.4 Upstream and Downstream Straight Lengths for Installation Between Various Fittings and the Primary Device
Figures
1 Eccentricity of Installed Orifice
26 6.5 Flow Conditioning Devices
27 2 Flow Conditioners
29 6.6 General Requirement for Flow Conditions at the Primary Device
7 Orifice Plates and Pressure Taps
7.1 Description
30 3 Standard Orifice Plate
32 3 Minimum Orifice Plate Thickness
33 7.2 Differential Pressure Taps
4 Recommended Maximum Diameters of Pressure Tap Holes for Flange and D and D/2 Taps
35 4 Location for Orifice Flange, and D and D/2 taps
36 5 Corner Taps
37 7.3 Coefficients and Corresponding Uncertainties for Orifice Plates
5 Upper Limits of Relative Roughness of the Up stream Pipe for Corner Tap Orifice Plates
40 7.4 Pressure Loss
8 ASME Flow Nozzles
8.1 Recommended Proportions for ASME Nozzles
41 6 ASME Flow Nozzles
42 8.2 Pressure Tap Requirements
8.3 Installation Requirements
43 8.4 ASME Flow Nozzle Coefficients
8.5 Uncertainties
44 8.6 Unrecovered Pressure Loss
9 ASME Venturi Tubes
9.1 Types of Venturi Tubes
6 Uncertainty of Discharge Coefficients
45 9.2 Geometric Profiles for ASME Venturi Tube
7 Profile of the ASME Venturi Tube
47 9.3 Materials and Manufacture of ASME Venturi Tubes
9.4 Pressure Taps
9.5 ASME Venturi Tube Discharge Coefficients
48 8 Discharge Coefficients of ASME Rough Cast Venturi Tubes as a Function of RD
49 9.6 Uncertainties
9.7 Pressure Loss of Venturi Tubes
50 9.8 Installation Requirements for ASME Venturi Tubes
9 Pressure Loss Across an ASME Venturi Tube
51 10 Uncertainties in the Measurement of Flow Rate
10.1 Definition of Uncertainty
7 Recommended Straight Lengths for ASME Venturi Tubes (for 0.5% Additional Uncertainty)
52 10.2 Practical Computation of the Uncertainty
55 A1
Appendices
A Typical Values of the Pipe Wall Roughness k
56 B1 Results of Sample Calculations for Discharge Coefficients at RD = 105
B2 Results of Sample Calculations for Expansion Factor [Y]
B Sample Calculations for Discharge Coefficients and Expansion Factors
57 C Classical Venturi Tubes Used Outside the Scope Covered by ASME MFC-3M
60 D Pressure Loss in a Classical Venturi Tube
61 D1 Pressure Loss Across an ASME Venturi Tube
62 E Thermal Expansion Factor
63 E1 Thermal Expansion Data [SI]
64 E2 Thermal Expansion Data [U.S.]
65 E3 Thermal Expansion of Various Materials
66 Index
ASME MFC 3M 1989
$98.04