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ASME PTC 10 2022

$75.42

ASME PTC-10-2022 Axial and Centrifugal Compressors

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ASME 2022
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The object of this Code is to provide a test procedure to determine the thermodynamic performance of an axial or centrifugal compressor doing work on a gas of known or measurable properties under specified conditions. This Code is written to provide a test procedure, which will yield the highest level of accuracy consistent with the best engineering knowledge and practice currently available. Nonetheless, no single universal value of the uncertainty is, or should be, expected to apply to every test. The uncertainty associated with any individual ASME PTC 10 test will depend on practical choices made in terms of instrumentation and methodology. Rules are provided to estimate the uncertainty for individual tests.

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PDF Pages PDF Title
4 CONTENTS
8 NOTICE
9 FOREWORD
11 ASME PTC COMMITTEE ROSTER
12 CORRESPONDENCE WITH THE PTC COMMITTEE
14 Section 1 Object and Scope
1-1 OBJECT
1-2 SCOPE
1-2.1 General
1-2.2 Compressor Arrangements
15 1-2.3 Compressor Performance and Polytropic Assumption
1-3 EQUIPMENT NOT COVERED BY THIS CODE
1-4 TYPES OF TESTS
1-5 PERFORMANCE RELATION TO GUARANTEE
1-6 ALTERNATE PROCEDURES
1-7 INSTRUCTIONS
1-8 REFERENCES
16 Section 2 Definitions and Description of Terms
2-1 BASIC SYMBOLS AND UNITS
2-2 PRESSURE DEFINITIONS
2-3 TEMPERATURE DEFINITIONS
17 Tables
Table 2-1-1 Symbols and Units
19 Table 2-1-2 Subscripts
20 2-4 OTHER GAS (FLUID) PROPERTIES DEFINITIONS
21 2-5 OPERATING CHARACTERISTICS DEFINITIONS
22 2-6 WORK, POWER, AND EFFICIENCY DEFINITIONS
2-7 MISCELLANEOUS DEFINITIONS
23 2-8 INTERPRETATION OF SUBSCRIPTS
24 Section 3 Guiding Principles
3-1 PLANNING THE TEST
3-1.1 Specified Conditions
3-1.2 Test Objectives
3-1.3 Test Facility
3-1.4 Test Personnel
3-1.5 Responsible Individual
3-2 TYPES OF TESTS
3-2.1 Type 1 Tests
25 3-2.2 Type 2 Tests
3-2.3 Test Type Selection
Table 3-2.1-1 Permissible Deviation From Specified Operating Conditions for Type 1 Tests
Table 3-2.1-2 Permissible Deviation From Specified Operating Parameters for Type 1 and Type 2 Tests
26 3-2.4 Calculation Procedures
3-3 LIMITATIONS
3-3.1 Section Boundaries
3-3.2 Sidestreams
Figures
Figure 3-2.1-1 Allowable Test Machine Mach Numbers for Centrifugal Compressors
27 3-3.3 Leakage Ratio
Figure 3-2.1-2 Allowable Test Machine Mach Numbers for Axial Compressors
28 3-3.4 Mechanical Losses
3-3.5 Components Between Sections
3-3.6 Heat Losses
3-3.7 Inlet Gas Superheat Requirement
Figure 3-2.1-3 Allowable Test Machine Reynolds Numbers Departure for Centrifugal Compressors
29 3-4 TEST GAS AND SPEED
3-4.1 Test Gas Properties
3-4.2 Test Speed
Figure 3-3.1-1 Section Control Volume
30 3-5 INTERMEDIATE FLOW STREAMS
3-5.1 Section Treatment
3-5.2 Compressors With Sidestreams
Figure 3-5.2-1 Typical Sidestream Sections
31 3-5.3 Inward Sidestreams
3-5.4 Extraction Sidestreams
3-5.5 Multisection Compressors
32 3-6 SAFETY
3-6.1 Compliance
3-6.2 Test Gas Compliance
3-6.3 Closed-Loop Testing
3-6.4 System Protection
3-7 PIPING
3-7.1 Piping Arrangements
3-7.2 Straight Lengths of Piping
3-7.3 Intercooler Performance and Pressure Drop
3-8 INSTRUMENTATION
33 3-9 PRELIMINARY TEST
3-9.1 Pretest Inspection
3-10 TEST OPERATION
3-10.1 Stabilization Time
3-10.2 Test Readings
3-10.3 Test Point Duration
3-10.4 Two-Point Test
3-10.5 Multipoint Test
34 3-10.6 Determination of Surge
3-10.7 Maximum Capacity Determination
3-11 TEST STABILIZATION
3-11.1 Test Readings
3-11.2 Calculated Values
3-12 INCONSISTENCIES
3-12.1 Outliers
3-12.2 Fluctuation Tolerances
3-13 ERRORS AND UNCERTAINTIES
3-13.1 Uncertainty Analysis
3-13.2 Test Quality
35 3-14 TEST LOG SHEETS
Table 3-12.2-1 Permissible Fluctuations of Test Readings
36 Section 4 Instruments and Methods of Measurement
4-1 METHODS
4-2 INSTRUMENTATION
4-3 PIPING
4-3.1 Pressure- and Temperature-Measuring Stations
4-3.2 Inlet Piping
37 Figure 4-3.2-1 Inlet and Discharge Configuration
38 Figure 4-3.2-2 Open Inlet
Figure 4-3.2-3 Vortex-Producing Axial Inlet
39 4-3.3 Discharge Piping
Figure 4-3.3-1 Diffusing Volute Discharge With Nonsymmetric Flow
Figure 4-3.3-2 Open Discharge
40 4-3.4 Typical Piping Arrangement
Figure 4-3.4-1 Typical Closed Loop
41 Figure 4-3.4-2 Typical Closed Loop With Sidestream
42 4-4 PROTECTIVE SCREENS
4-5 FLOW CONDITIONERS
4-6 PRESSURE MEASUREMENTS
4-6.1 Pressure Instrumentation
4-6.2 Gauge Lines
4-6.3 Transducers
4-6.4 Operational Stability
4-6.5 Dynamic Pressure
4-6.6 Raw Data Observations
4-6.7 Inlet Pressure Measurement
4-6.8 Discharge Pressure Measurement
43 4-6.9 Total Pressure Measurement
4-6.10 Ambient Pressure and Temperature
4-6.11 Internal Pressure Measurements
4-7 TEMPERATURE MEASUREMENTS
4-7.1 Temperature Instrumentation
4-7.2 Thermocouples
44 4-7.3 Total Temperature Measurement
4-7.4 Inlet Temperature Measurement
4-7.5 Discharge Temperature Measurement
4-7.6 Internal Temperature Measurements
4-8 CAPACITY MEASUREMENTS
4-8.1 Flow Measurement Instrumentation
4-8.2 Flow-Measuring Device for Flow Sections
4-8.3 Open Inlet Flow Nozzle
45 4-8.4 Open Discharge Flow Nozzle
4-9 GAS COMPOSITION
4-9.1 Gas Composition Evaluation
4-9.2 Gas Composition Evaluation for Performance Curve
4-9.3 Gas Chromatographs
Figure 4-7.6-1 Typical Inward Sidestream Cross Section
46 4-9.4 Test Loop Design
4-9.5 Test Loop Condensation
4-10 SPEED MEASUREMENT
4-10.1 Continuous Speed Measurement
4-10.2 Speed Measurement Instrumentation
4-11 TIME MEASUREMENT
4-12 METHODS OF SHAFT POWER MEASUREMENT
4-12.1 Shaft Power Input
4-12.2 Power Measurement Methods
4-13 SHAFT POWER BY TORQUE MEASUREMENTS
47 4-14 SHAFT POWER BY ELECTRICAL MEASUREMENTS
4-14.1 Motor Shaft Power
4-14.2 Motor Efficiency Determination
4-14.3 Motor Power Input Measurement
4-14.4 Transformers
4-15 SHAFT POWER BY HEAT BALANCE MEASUREMENTS
4-15.1 Shaft Power Computation
4-15.2 Mechanical Losses
4-15.3 Precautions and Limitations
48 4-16 HEAT LOSS
4-16.1 Heat Loss Minimization
4-16.2 Cooling Fluid Measurements
4-17 MECHANICAL LOSSES
4-17.1 Heat Produced by Mechanical Losses
4-17.2 Gear Losses
4-18 INSTRUMENT CALIBRATION AND UNCERTAINTY
4-18.1 Calibration
49 4-18.2 Measurement Uncertainty
4-18.3 Temperature Instrumentation Calibration
4-18.4 Electrical Power Instrumentation Calibration
4-18.5 Torque Meter Calibration
4-19 HUMIDITY MEASUREMENT
4-20 TORQUE MEASUREMENT
Table 4-18.2-1 Typical End-to-End Measurement Uncertainty
50 4-21 DATA ACQUISITION SYSTEM
4-21.1 Collection
4-21.2 Processing
4-21.3 Calibration
51 Section 5 Computation of Results
5-1 CALCULATION PROCEDURE
5-2 COMPUTATIONAL METHODS: CHOICE OF METHODS
5-2.1 Method Selection
5-2.2 Sandbergā€“Colby Method
Table 5-2.2-1 Sandbergā€“Colby Method Polytropic Relations
52 5-2.3 Huntington Method
5-2.4 Sandbergā€“Colby Multistep Method
5-2.5 Tabulated Properties and Equations of State Methods
5-3 TYPE 2 TEST GAS AND TEST SPEED SELECTION
5-3.1 Test Gas Selection
5-3.2 Test Speed Selection
53 Table 5-2.3-1 Huntington Method Polytropic Relations
54 Figure 5-2.4-1 Sandbergā€“Colby Multistep Numerical Integration Method
58 5-3.3 Test Speed Validation
5-4 CALCULATIONS FOR TEST CONDITIONS
5-4.1 Test Data Acquisition
59 5-4.2 Raw Data Acceptability
5-4.3 Processing Raw Data
5-4.4 Test Pressure and Temperature
60 Figure 5-4.4.1-1 Rigorous Method to Calculate the Test Total Pressure and Temperature
62 Figure 5-4.4.2-1 Alternative Mach Number Method to Calculate the Test Total Pressure and Temperature
64 5-4.5 Test Density and Specific Volume
5-4.6 Test Flow Rate
5-4.7 Test Power
66 5-5 NONDIMENSIONAL PARAMETERS
5-5.1 Machine Mach Number
5-5.2 Machine Reynolds Number
5-5.3 Specific Volume Ratio
5-5.4 Volume Flow Ratio
67 5-5.5 Flow Coefficient
5-6 CALCULATIONS FOR SPECIFIED OPERATING CONDITIONS
5-6.1 Single-Section Compressor
68 Table 5-6.1.2-1 Real Gas Nondimensional Parameters
Table 5-6.1.2-2 Conversion of Nondimensional Parameters
70 5-6.2 The Multisection Compressor
Figure 5-6.1.2-1 Interpolation for the Specified Condition Flow Coefficient
71 5-6.3 Machine Reynolds Number Correction
72 5-6.4 Mechanical Losses
73 Figure 5-6.3.2-1 Machine Reynolds Number Correction for Centrifugal Compressors
75 Section 6 Report of Test
6-1 CONTENTS
6-2 TYPICAL REPORT INFORMATION
6-2.1 General Information
6-2.2 Description of Test Calculations
6-2.3 Description of Test Installation
76 6-2.4 Specified Conditions and Test Conditions
6-2.5 Performance at Specified Conditions
6-2.6 Setup of Instruments and Methods of Measurement
6-2.7 Test Points Data (See Subsection 2-7)
77 6-2.8 Computed Results for Each Test Point (See Paras. 3-10.4 and 3-10.5)
78 6-2.9 Computed Test Performance Parameters
79 6-2.10 Machine Reynolds Number Correction
6-2.11 Computed Results for Specified Operating Conditions
6-2.12 Uncertainty Analysis
6-2.13 Summary of Results
80 Section 7 Test Uncertainty
7-1 GENERAL
7-2 SCOPE OF UNCERTAINTY ANALYSIS
7-3 METHODS OF ASME PTC 19.1
7-4 TEST METHOD UNCERTAINTY
Table 7-4-1 Maximum Expected Uncertainty
81 NONMANDATORY APPENDICES
NONMANDATORY APPENDIX A USE OF TOTAL PRESSURE AND TOTAL TEMPERATURE TO DEFINE COMPRESSOR PERFORMANCE
A-1 GENERAL
A-2 ENERGY EQUATION
A-3 TOTAL CONDITIONS
82 Figure A-4-1 Compressor State Points, Static and Total
A-4 COMPRESSION PROCESS
A-5 SYSTEM BOUNDARIES
83 NONMANDATORY APPENDIX B TYPE 2 PERFORMANCE TESTING OF BACK-TO-BACK COMPRESSORS
B-1 OBJECTIVE
B-2 FUNCTIONAL OPERATION OF TYPE 2 PERFORMANCE TEST
84 Figure B-2.1-1 Typical Back-to-Back Compressor Type 2 Test Setup
86 Table B-2.4-1 Sample Post-Test Leakage Evaluation for Division Wall
Table B-2.4-2 Sample Post-Test Leakage Evaluation for Balance Seal
87 NONMANDATORY APPENDIX C SAMPLE CASE CALCULATIONS
C-1 INTRODUCTION
88 Table C-1.3.1-1 Historical Gas Models and Labels
C-2 PERFORMANCE ANALYSIS ELEMENTS
C-3 HIGH-PRESSURE NATURAL GAS COMPRESSOR SAMPLE CALCULATIONS
90 Figure C-3.2-1 Typical Straight-Through Centrifugal Compressor Section
91 Table C-3.2-1 Specified Design for High-Pressure Natural Gas Compressor
92 Figure C-3.2-2 Phase Diagram for Specified Gas Composition
94 Table C-3.3-1 Specified Performance Calculations for High-Pressure Natural Gas Compressor
95 Table C-3.3-2 Calculation of Total Conditions for Specified Performance: Inlet ā€” U.S. Customary Units
96 Table C-3.3-2M Calculation of Total Conditions for Specified Performance: Inlet ā€” SI Units
97 Table C-3.3-3 Calculation of Total Conditions for Specified Performance: Discharge ā€” U.S. Customary Units
98 Table C-3.3-3M Calculation of Total Conditions for Specified Performance: Discharge ā€” SI Units
100 Table C-3.4-1 Type 2 Preliminary Test Design
101 Table C-3.4-2 Screening Criteria Comparison for Potential Test Gas Compositions
102 Table C-3.5-1 Test Design for High-Pressure Natural Gas Compressor Using Carbon Dioxide
103 Figure C-3.5-1 Phase Diagram for Test Gas Composition
104 Table C-3.5-2 Test Design Performance Calculations for High-Pressure Natural Gas Compressor Using Carbon Dioxide
105 Table C-3.6.1-1 Necessary Information
Table C-3.6.1.1-1 Recorded Raw Data Observations for Compressor Inlet Static Pressure for a Test Point
106 Table C-3.6.1.1-2 Raw Data Observations Converted to Absolute Values
Table C-3.6.1.1-3 Test for and Remove Outliers on a per-Reading Basis
107 Table C-3.6.1.1-4 Raw Data Observations Excluding Outliers
Table C-3.6.1.1-5 Verification of Fluctuation Compliance
Table C-3.6.1.1-6 Determination of Test Point Value, pi, Excluding Outliers and Rejected Readings Due to Fluctuations
108 Table C-3.6.1.2-1 Recorded Raw Data Observations for Compressor Inlet Measured Temperature for a Test Point
Table C-3.6.1.2-2 Converted Raw Data Observations to Absolute Values
Table C-3.6.1.2-3 Test for and Remove Outliers on a per-Reading Basis
109 Table C-3.6.1.2-4 Raw Data Observations Excluding Outliers
Table C-3.6.1.2-5 Verification of Fluctuation Compliance
Table C-3.6.1.2-6 Determination of Test Point Value, Ti, Excluding Outliers and Rejected Readings Due to Fluctuations
110 Table C-3.6.2-1 Type 2 As-Tested Data Point
111 Table C-3.7-1 Comparison of Test Design and As-Tested Inlet and Discharge Conditions
112 Table C-3.7-2 Comparison of Test Design and As-Tested Performance
113 Table C-3.8-1 As-Tested Nondimensional Results
Table C-3.9-1 Specified and As-Tested Operating Parameters
114 Figure C-3.9-1 As-Tested Flow Coefficient and Volume Ratio
115 Figure C-3.9-2 As-Tested Machine Mach Number
116 Figure C-3.9-3 As-Tested Machine Reynolds Number
117 Table C-3.10.1-1 As-Tested Reynolds Number Corrections
118 Figure C-3.10.2-1 Reynolds Number Correction Trend ā€” Polytropic Efficiency ā€” Perfect Test
Figure C-3.10.2-2 Reynolds Number Correction Trend ā€” Polytropic Work Coefficient ā€” Perfect Test
119 Figure C-3.10.2-3 Reynolds Number Correction Trend ā€” Flow Coefficient ā€” Perfect Test
Figure C-3.10.2-4 Reynolds Number Correction Trend ā€” Work Input and Total Work Input Coefficients ā€” Perfect Test
121 Table C-3.11-1 As-Tested Performance at Specified Conditions
122 Table C-3.11-2 Comparison of Specified Performance and Converted Specified Performance
124 Table C-3.12.1-1 Specified and Type 2 Test Design Section Heat Transfer Losses
126 Figure C-3.12.2.1-1 Trends for Natural Convection Heat Transfer Coefficient
127 Figure C-3.12.2.2-1 Trends for Radiative Heat Transfer Rate
128 NONMANDATORY APPENDIX D REFERENCES AND BIBLIOGRAPHY
D-1 CODES AND STANDARDS
D-2 OTHER REFERENCES
129 D-3 BIBLIOGRAPHY
132 NONMANDATORY APPENDIX E RATIONALE FOR CALCULATION METHODS
E-1 PURPOSE
E-2 CALCULATION MODEL
134 E-3 CODE NONDIMENSIONAL PARAMETERS
138 Figure E-3.11-1 Compressor Section Model
139 E-4 SPEED SELECTION
E-5 INLET STATE FOR MIXED STREAMS
141 NONMANDATORY APPENDIX F REYNOLDS NUMBER CORRECTION FOR CENTRIFUGAL COMPRESSORS
F-1 GENERAL
142 NONMANDATORY APPENDIX G METHODS FOR CALCULATING TOTAL CONDITIONS
G-1 INTRODUCTION
143 G-2 RIGOROUS METHOD
G-3 ALTERNATIVE MACH NUMBER METHOD
144 NONMANDATORY APPENDIX H TEST UNCERTAINTY SAMPLE CALCULATION
H-1 INTRODUCTION
H-2 EXAMPLE
146 Table H-2-1 Sample Calculation of the Systematic Uncertainty for Polytropic Efficiency
147 Table H-2-2 Sample Calculation of the Systematic Uncertainty for Polytropic Work
ASME PTC 10 2022
$75.42