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 |
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 |