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ASME PTC 47.2 2019

$98.04

ASME PTC 47.2-2019, Gasification Block of an Integrated Gasification Combined Cycle Power Plant

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ASME 2019
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PDF Catalog

PDF Pages PDF Title
4 CONTENTS
7 NOTICE
8 FOREWORD
9 ASME PTC COMMITTEE ROSTER
10 CORRESPONDENCE WITH THE PTC COMMITTEE
12 INTRODUCTION
14 Section 1 Object and Scope
1-1 OBJECT
1-1.1 Accuracy
1-1.2 Performance Characteristics
1-2 SCOPE
15 1-3 UNCERTAINTY
1-4 REFERENCES
Tables
Table 1-3-1 Largest Expected Test Uncertainties of Performance Parameters
18 Section 2 Definitions and Descriptions of Terms
2-1 DEFINITIONS
26 Section 3 Guiding Principles
3-1 INTRODUCTION
3-2 TEST BOUNDARY AND REQUIRED MEASUREMENTS
3-2.1 Defining the Test Boundary
3-2.2 Identifying Streams Related to Test Result Calculations
27 3-2.3 Identifying Required Measurements and Measurement Accuracy
3-2.4 Primary and Secondary Measurements
Figures
Figure 3-2.2-1 Gasification Test Boundary
28 3-3 TEST PLAN
3-3.1 General
3-3.2 Object of Test
3-4 TEST PREPARATIONS
3-4.1 General Precaution
3-4.2 Agreements
3-4.3 Test Apparatus
29 3-4.4 Preliminary Testing
30 3-5 CONDUCT OF THE TEST
3-5.1 Valve Lineup/Cycle Isolation
3-5.2 Proximity to Design Conditions
3-5.3 Stabilization
31 Table 3-5.2-1 Guidance for Establishing Permissible Deviations From Design Conditions
32 3-5.4 Starting Criteria
3-5.5 Stopping Criteria
3-5.6 Duration of Test Runs
3-5.7 Number of Test Runs
3-5.8 Number of Readings
33 3-5.9 Evaluation of Test Runs
3-5.10 Constancy of Test Conditions
Figure 3-5.9-1 Uncertainty Intervals
34 3-6 CALCULATION AND REPORTING OF RESULTS
3-6.1 Data Records and the Test Log
3-6.2 Causes for Rejection of Test Runs
3-6.3 Uncertainty
3-6.4 Application of Correction Methods
35 Section 4 Instruments and Methods of Measurement
4-1 INTRODUCTION
4-2 GENERAL REQUIREMENTS
4-2.1 Introduction
4-2.2 Measurements
36 4-2.3 Instrumentation
37 4-2.4 Instrument Calibration
39 4-2.5 Instrument Verification
4-2.6 Instrumentation Systematic Uncertainty
4-3 PRESSURE MEASUREMENT
4-3.1 Introduction
40 Table 4-2.6-1 Potential Instrumentation Systematic Uncertainty
42 4-3.2 Required Uncertainty
4-3.3 Recommended Pressure Measurement Devices
44 4-3.4 Absolute Pressure Measurements
4-3.5 Gauge Pressure Measurements
45 4-3.6 Differential Pressure Measurements
46 4-4 TEMPERATURE MEASUREMENT
4-4.1 Introduction
4-4.2 Required Uncertainty
4-4.3 Recommended Temperature Measurement Devices
47 Figure 4-3.6.2-1 Five-Way Manifold
Figure 4-3.6.2-2 Water Leg Correction for Flow Measurement
50 Figure 4-4.3.2.1-1 Three- and Four-Wire RTDs
51 4-4.4 Calibration of Primary Parameter Temperature Measurement Devices
4-4.5 Temperature Scale
4-4.6 Typical Applications for Temperature Measurement
52 Figure 4-4.6.2-1 Flow-Through Well
53 4-5 SOLID FLOW MEASUREMENT
4-5.1 Solid-Fuel and Sorbent Flow Measurement
4-5.2 Solid-Fuel and Sorbent Sampling
54 Figure 4-4.6.3-1 Duct Measurement Points
55 4-5.3 Residue Flow Measurement and Splits
56 Table 4-5.2.1-1 Typical ASTM Test Uncertainties for Properties of Coal and Coke
57 4-5.4 Residue Sampling
Table 4-5.2.1-2 Typical Systematic Uncertainties for Limestone Properties Determined From ASTM C25, Test Method31
58 4-6 LIQUID FLOW MEASUREMENT
4-6.1 Water
4-6.2 Liquid Fuel and Hydrocarbon Products
59 4-7 STEAM FLOW MEASUREMENT
4-7.1 Steam Flow Characteristics
4-7.2 Secondary Steam Flow Measurements
4-7.3 Two-Phase Steam-Water Mixtures
4-8 GAS FLOW MEASUREMENT
Table 4-6.2-1 Typical ASTM Standard Test Systematic Uncertainty for Fuel Oil Properties
60 4-8.1 Digital Computation of Gas Flow Rate
4-8.2 Oxygen Purity Measurements
4-9 MATERIAL ANALYSIS
4-9.1 Sample Collection
61 4-9.2 Analytical Techniques
4-10 INPUT AND OUTPUT HEAT MEASUREMENT
4-10.1 Direct Measurement Method
62 4-10.2 Indirect Measurement Method
4-11 AUXILIARY ELECTRIC POWER MEASUREMENT
4-11.1 Introduction
63 4-11.2 Electrical Metering Equipment
64 4-11.3 Measurement of Step-Up and Step-Down Transformers
4-12 DATA COLLECTION AND HANDLING
4-12.1 Introduction
4-12.2 Data Management
65 4-12.3 Data Acquisition System Selection
66 Section 5 Calculations and Results
5-1 INTRODUCTION
5-2 DATA REDUCTION
5-3 FUNDAMENTAL EQUATIONS
5-3.1 Nomenclature
67 5-3.2 Corrected Product Syngas Energy
68 5-3.3 Corrected Gasification Effectiveness
69 5-3.4 Carbon Conversion Efficiency
5-3.5 Gasifier Energy Efficiency
70 5-4 CORRECTIONS
5-4.1 Gasification Block Model
71 5-4.2 Additive and Multiplicative Corrections
72 Table 5-4.2-1 Additive and Multiplicative Corrections
74 5-5 PARAMETERS USED IN THE FUNDAMENTAL EQUATIONS
75 5-5.1 Primary Fuel Input Calculations
Table 5-4.2.4.3-1 Typical Auxiliary Equipment and Corrections
76 5-5.2 Heating Value, LHV
5-5.3 Product Syngas Energy Flow, Qpg
77 Section 6 Report of Results
6-1 GENERAL REQUIREMENTS
78 6-2 EXECUTIVE SUMMARY
6-3 INTRODUCTION
6-4 CALCULATIONS AND RESULTS
6-5 INSTRUMENTATION
6-6 CONCLUSIONS
79 6-7 APPENDICES
80 Section 7 Uncertainty Analysis
7-1 INTRODUCTION
7-1.1 Pretest Uncertainty Analysis
7-1.2 Post-Test Uncertainty Analysis
7-2 OBJECTIVE OF UNCERTAINTY ANALYSIS
7-3 DETERMINATION OF OVERALL UNCERTAINTY
81 7-4 SOURCES OF ERROR
7-5 CALCULATION OF UNCERTAINTY
Table 7-5-1 Expected Uncertainty Limits
Table 7-5-2 Format of Uncertainty Calculations
82 Table 7-5-3 Measured Parameters Needed for Uncertainty Calculations
83 7-6 SENSITIVITY COEFFICIENTS
7-7 SYSTEMATIC UNCERTAINTY
84 7-8 RANDOM STANDARD UNCERTAINTY FOR SPATIALLY UNIFORM PARAMETERS
85 7-9 RANDOM STANDARD UNCERTAINTY FOR SPATIALLY NONUNIFORM PARAMETERS
7-10 CORRELATED SYSTEMATIC STANDARD UNCERTAINTY
86 NONMANDATORY APPENDIX A SAMPLE CALCULATION: IGCC GASIFICATION BLOCK
A-1 INTRODUCTION
A-2 CYCLE DESCRIPTION
A-3 BASIS FOR EXAMPLE CASE
A-4 TEST BOUNDARY
A-5 TEST CORRECTIONS
87 Figure A-2-1 A Simplified Sketch Separating the Gasification Block From an Integrated Gasification and Combined Cycle Plant
88 Figure A-2-2 A Simplified Block Diagram Illustrating the General Configuration of the Gasification Block
89 Table A-3-1 Reference Design Data for the Tampa Electric Polk Power Station
90 Table A-5-1 Additive and Multiplicative Corrections
92 Figure A-5.5-1 Syngas Energy Correction for Primary Fuel LHV, MS1
Figure A-5.6-1 Syngas Energy Correction for Slurry Concentration, MS5
93 Figure A-5.8-1 Primary Fuel Energy Correction for Primary Fuel LHV, MF1
Figure A-5.9-1 Primary Fuel Energy Correction for Slurry Concentration, MF5
94 A-6 REFERENCE AND MEASURED CONDITIONS
A-7 CORRECTED PERFORMANCE CALCULATIONS
95 Table A-6-1 Reference and Test Conditions
96 Table A-7.1.1-1 Sour and Product Syngas
97 Table A-7.3-1 Auxiliary Components
98 A-8 CONCLUSIONS
99 Table B-2-1 Calculated and Expected Uncertainty Limits
NONMANDATORY APPENDIX B SAMPLE UNCERTAINTY ANALYSIS
B-1 INTRODUCTION
B-2 CALCULATIONS
100 Table B-2-2 Uncertainty of Corrected Product Syngas Energy
101 Table B-2-3 Uncertainty of Corrected Primary Fuel Energy
Table B-2-4 Uncertainty of Corrected Auxiliary Power
102 Table B-2-5 Uncertainty of Corrected Gasification Effectiveness
103 NONMANDATORY APPENDIX C STREAMS AND TEST BOUNDARIES OF TYPICAL GASIFICATION BLOCKS
C-1 INTRODUCTION
C-2 MOVING (FIXED) BED GASIFIERS
C-3 FLUIDIZED-BED GASIFIERS
C-4 ENTRAINED-FLOW GASIFIERS
104 Figure C-2-1 Lurgi Fixed-Bed Dry Ash Gasifier
105 Figure C-2-2 BGL Fixed-Bed Slagging Gasifier
106 Figure C-3-1 High-Temperature Winkler Fluidized-Bed Dry Ash Gasifier
107 Figure C-3-2 TRIG Fluidized-Bed Agglomerating Gasifier
108 Figure C-4-1 Shell Entrained-Flow Gasifier With Dry-Fed Fuel
109 Figure C-4-2 GEE Entrained-Flow Gasifier With Fuel Slurry
110 Figure C-4-3 Conoco Entrained-Flow Gasifier With Fuel Slurry
111 Figure C-4-4 MHI Entrained-Flow Gasifier
112 Figure C-4-5 Siemens Entrained-Flow Gasifier With Secondary Fuel
ASME PTC 47.2 2019
$98.04