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نویسندگان: Junfu Lyu. Shuiqing Li
سری: Environmental Science and Engineering
ISBN (شابک) : 9811616566, 9789811616563
ناشر: Springer
سال نشر: 2021
تعداد صفحات: 1091
زبان: English
فرمت فایل : PDF (درصورت درخواست کاربر به PDF، EPUB یا AZW3 تبدیل می شود)
حجم فایل: 31 مگابایت
در صورت تبدیل فایل کتاب Clean Coal and Sustainable Energy: Proceedings of the 9th International Symposium on Coal Combustion به فرمت های PDF، EPUB، AZW3، MOBI و یا DJVU می توانید به پشتیبان اطلاع دهید تا فایل مورد نظر را تبدیل نمایند.
توجه داشته باشید کتاب زغال سنگ پاک و انرژی پایدار: مجموعه مقالات نهمین سمپوزیوم بین المللی احتراق زغال سنگ نسخه زبان اصلی می باشد و کتاب ترجمه شده به فارسی نمی باشد. وبسایت اینترنشنال لایبرری ارائه دهنده کتاب های زبان اصلی می باشد و هیچ گونه کتاب ترجمه شده یا نوشته شده به فارسی را ارائه نمی دهد.
Preface Contents About the Editors Part I Invited Talks 1 Advances in Two-Fluid LES of Two-Phase Combustion 1.1 Introduction 1.2 Previous Studies on Two-Fluid LES of Two-Phase Combustion 1.3 Suggested Models for Two-Fluid LES of Two-Phase Combustion 1.4 The Two-Phase SGS Energy Equation Model 1.5 The SGS Mass Flux and Heat Flux Models 1.6 The SOM-SGS Gas Combustion Model 1.7 Assessment of the Two-Phase SGS Energy Equation Model 1.8 Assessment of the SOM Combustion Model 1.9 Assessment of the Two-Fluid RANS Modeling of Coal Combustion 1.10 Conclusions References 2 Flexible Operation of High Efficiency Coal Power Plants to Ensure Grid Stability When Intermittent Renewables Are Included 2.1 Introduction 2.2 Instrumentation and Control 2.3 Flexibility Options 2.4 Pollution Control Systems 2.5 Flexibility Impact Management 2.6 Conclusions References 3 Advances in Modeling Coal Pyrolysis, Char Combustion, and Soot Formation from Coal and Biomass Tar 3.1 Elemental Composition of Tar and Char 3.2 Soot Formation from Coal 3.3 Char Oxidation References 4 The Change in Bed Materials Size Distribution and Its Effect on CFB Boiler Operation 4.1 Introduction 4.2 The Initial Operation of the Once-Thought CFB Boiler of 330 MWe Unit #9 of Novocherkassk TPP 4.3 Model for Estimation of Changes in the PSD of the Bed Material 4.4 Results and Discussion 4.5 Conclusions References 5 Insights of MILD Combustion from High-Fidelity Simulations 5.1 Introduction 5.2 Theoretical Formulation 5.2.1 Governing Equations for Coal Combustion Simulation 5.2.2 Mixture Fraction Based Models 5.2.3 Well-Stirred Reactor Models 5.3 Computational Configuration 5.4 Results and Discussion 5.4.1 Comparison of Mixture Fraction-Based Models 5.4.2 Analysis of MILD Combustion Using Well-Stirred Reactor and Steady Flamelet Models 5.5 Conclusions References Part II Basic Coal Quality and Combustion 6 Study on Alkali Metal Migration Characteristics in the Pyrolysis of Naomaohu Coal in CO Atmosphere 6.1 Experimental Part 6.1.1 Experimental Sample 6.1.2 Experimental Setup and Steps 6.1.3 Determination of the Form and Content of Alkali Metals 6.2 Results and Discussion 6.2.1 Analysis of the Occurrence of Alkali Metals in Raw Coal 6.2.2 Migration Characteristics of Alkali Metals at Different Temperatures 6.3 Conclusion References 7 Precipitation Characteristics of Alkali/Alkaline Earth Metal in High Alkali Coal 7.1 Introduction 7.2 Experimental Approaches 7.2.1 Preparation of Coal Samples and Sample Properties 7.2.2 Experimental Equipment and Facilities 7.2.3 Experimental Approaches 7.3 Experimental Results and Discussion 7.3.1 Influence of AT on Ash Content 7.3.2 Alkali and Chlorine Contents in Coal Ash at Different AT 7.3.3 Alkaline Earth Metal Content in Coal Ash at Different AT 7.3.4 Comparation of XRF and ICP-OES Results 7.4 Conclusion References 8 Experimental Study on Removal of Low Concentration Coal Tar in Syngas by Mg-Ca Composite Catalyst 8.1 Introduction 8.2 Experimental 8.2.1 Experimental Apparatus 8.2.2 Experimental Materials 8.3 Results and Discussion 8.3.1 Effect of Temperature on Tar Conversion Rate and Gas Products 8.3.2 Effect of Catalyst Particle Size on Tar Conversion Rate and Gas Products 8.3.3 Effect of Reaction Time on Tar Conversion Rate and Gas Products 8.4 Conclusions References 9 Experimental Investigation on Sodium Migration and Mineral Transformation in Ash Deposit During Gasification of Zhundong Coal Using a Drop Tube Furnace 9.1 Introduction 9.2 Experimental 9.3 Results and Discussion 9.3.1 Effects of Sodium Salts, Kaolin and Diatomite on Sodium Migration 9.3.2 Effect of Ash Deposition Time on Sodium Migration and Mineral Transformation 9.4 Conclusions References 10 Study on Characteristics and Influencing Factors of Coal-Water Slurry Pyrolysis 10.1 Introduction 10.2 Experiment 10.3 Experimental Results and Analysis 10.3.1 Effect of Temperature on Weight Loss Rate and Pyrolysis Gas Yield 10.3.2 Effect of Temperature on Combined Gas Volume Concentration 10.3.3 Effect of Temperature on Gas Yield and Volume Concentration 10.3.4 Effect of Heating Rate and Residence Time on Weight Loss Rate 10.4 Conclusion References 11 Soot Formation in High-Temperature Pyrolysis of Various Coals 11.1 Introduction 11.2 Experimental Section 11.2.1 Experimental Setups 11.2.2 Fuel Property 11.3 Results and Discussion 11.3.1 Soot Yield and Number Size Distribution 11.3.2 Gas Compositions 11.3.3 Soot Oxidization 11.4 Conclusions References 12 Effect of Microstructures on Char Combustion Reactivity 12.1 Introduction 12.2 Experimental 12.2.1 Coal Samples and Preparation of Char 12.2.2 Char Characterization 12.2.3 X-Ray Diffraction Analysis 12.2.4 Char Combustion Reactivity Measurement 12.3 Results and Discussion 12.3.1 X-Ray Diffraction Carbon Crystallite Analyses 12.3.2 Char Combustion Reactivity 12.3.3 Correlations Between Char Combustion Reactivity and X-Ray Diffraction 12.4 Conclusions References 13 Effect of K2CO3 Addition on CO2 Gasification Characteristics and Ash Sintering Behaviour of a Chinese Lignite at Different Temperatures and Pressures as Examined Using a High-Pressure Thermogravimetric Analyser 13.1 Introduction 13.2 Experimental 13.2.1 Materials 13.2.2 Experimental Setup 13.2.3 Data Processing and Analysis 13.2.4 SEM–EDS analysis 13.3 Results and Discussion 13.3.1 Gasification Characteristics 13.3.2 Ash Morphology 13.4 Conclusions References 14 Ash Deposition and Slagging Behavior of Xinjiang High-Alkali Coal in a 20MWth Cyclone Combustion Test Facility 14.1 Introduction 14.2 Experimental 14.2.1 Coal Properties 14.2.2 20MWth Pilot Plant Test Facility 14.3 Results and Discussion 14.3.1 Slagging Behavior of Ash During Cyclone Combustion Process 14.3.2 Ash Deposition Behavior in the Convective Zone of Furnace 14.3.3 Ash Slagging/Deposition Mechanism of Zhundong Coal Ash at Cyclone-Fired Condition 14.4 Conclusions References 15 Release Characteristics of Alkali Metals in Oxygen-Enriched Combustion of a Single Char Particle with Random Pore Model 15.1 Introduction 15.2 Physical Model 15.2.1 Random Pore Sub-model 15.2.2 Chemical Reaction Sub-model 15.2.3 Diffusion Sub-model 15.2.4 Energy Sub-model 15.3 Model Validation 15.4 Alkali Metal Release in O2/N2 and O2/CO2 Atmospheres 15.5 Effects of Particle Size and Ambient Temperature 15.6 Effects of O2 Mole Fraction in O2/N2 and O2/CO2 Atmospheres 15.7 Conclusion References 16 Experimental Study on the Influence of Slagging and Fouling for Wall Temperature Distribution 16.1 Introduction 16.2 Experimental Setups and Methods 16.2.1 Experimental System and Setups 16.2.2 Clean Tube Wall Temperature 16.2.3 Stained Tube Wall Temperature 16.2.4 Influence Factors of Stained Tube Temperature Distribution 16.3 Results and Discussions 16.3.1 Circumferential Temperature Distribution of Clean Tube 16.3.2 Circumferential Temperature Distribution of Stained Tube 16.3.3 Influence Factors of Temperature Distribution of Stained Tube 16.4 Conclusion References 17 Numerical Investigation of Fly Ash Deposition onto Tube Bundles Inside Coal-Fired Boilers 17.1 Introduction 17.2 Methodology 17.3 Results and Discussion 17.4 Conclusions References 18 Effect of Refractory Lining Thickness on Slag Layer Behavior in Cyclone Barrel 18.1 Introduction 18.2 The Modeled Cyclone Barrel 18.3 Numerical Models 18.4 Simulation Conditons 18.5 Results and Discussion 18.5.1 Temperature and Heat Flux 18.5.2 Thickness and Velocity 18.5.3 Outlet Temperature 18.6 Conclusions References 19 Characteristics of Alkali Metal Migration and Transformation During Pyrolysis of Naomaohu Coal 19.1 Introduction 19.2 Experimental System 19.3 Measurement of Alkali Metals (Na, K) 19.4 Results and Discussion 19.4.1 Effect Of Temperature And Atmosphere On Semi-Coke And Tar Yield 19.4.2 Effect of Temperature on the Occurrence Form and Residual Amount of Alkali Metal in Coal Char 19.4.3 Effect of Temperature on Distribution Characteristics of Alkali Metals 19.5 Conclusion References Part III Pulverized Coal Combustion 20 Numerical Investigation on Combustion Characteristics and NOx Emission of Double-Reheat Tower Boiler at Different Loads 20.1 Introduction 20.2 Boiler Decription 20.3 Modeling Methodology 20.3.1 Grid Independence 20.3.2 Numerical Models 20.4 Results and Disscusion 20.4.1 Validation of the CFD simulation 20.4.2 Effects of Different Unit Loads on the Combustion Characteristics and NOx Emission 20.4.3 Effects of Different Excess Air Ratios on the Combustion Characteristics and NOx Emission 20.5 Conclusions References 21 Numerical Study on Influence of Platen Super-Heaters on Heat Deviation in a 600 MW Tangentially Fired Pulverized-Coal Boiler 21.1 Introduction 21.2 Description of Boiler 21.3 Numerical Simulation 21.3.1 Geometric Models 21.3.2 Meshes 21.3.3 Mathematical Models 21.4 Results and Discussion 21.4.1 Calculation Validation 21.4.2 Temperature and Velocity Contours 21.4.3 Non-uniformity Analysis 21.5 Conclusions References 22 Industrial Experimental and Numerical Simulation Study on the Combustion and NOx Formation Characteristics in a 600MWe Utility Boiler with a Novel Swirl Burner Burning Bituminous Coal 22.1 Introduction 22.2 Research Object 22.3 Research Methods 22.3.1 Experimental Research Methods 22.3.2 Numerical Simulation 22.4 Analysis of Results 22.4.1 Numerical Calculation and Experimental Comparison of Cold Aerodynamic Field 22.4.2 Full-scale Experimental and Numerical Simulation Results 22.5 Conclusion References 23 Distribution of Temperature and Characteristics of Soot Volume Fraction in MILD-OCC Flame 23.1 Introduction 23.2 Experimental 23.2.1 Experimental System 23.2.2 Measurement Method and Devices 23.2.3 Thermocouple Particle Densitometry 23.2.4 The Filter Membrane Weighing Method 23.3 Results and Discussion 23.3.1 Measurement of Temperature Distribution in MILD-OCC Flame 23.3.2 Volume Fraction Distribution Characteristics of Soot in Combustion Flame 23.3.3 Soot Mass Concentration Distribution in Combustion Flame 23.4 Conclusion References 24 Experimental Investigation of Methane Assisted Pulverized Coal Flames Using an Optical Accessible Combustion Chamber 24.1 Introduction 24.2 Experimental Setup 24.2.1 Burner Design 24.2.2 Combustion Chamber 24.2.3 Gas and Particle Supply 24.2.4 Laser Doppler Velocimetry System 24.3 Operation Parameters and Conditions 24.3.1 Coal Case Measurements 24.3.2 Alu-Cold Case Measurements 24.4 Results and Discussion 24.4.1 Axial Mean Velocity 24.4.2 Tangential Mean Velocity 24.4.3 Root Mean Square (RMS) Intensities 24.5 Conclusion References 25 Ignition Characteristics of Coal/Air Jets from Rectangular Nozzles 25.1 Introduction 25.2 Experimental Approach 25.2.1 Experimental System 25.2.2 Coal Properties 25.2.3 Measurement Conditions 25.3 Numerical Approach 25.4 Results and Discussion 25.4.1 Ignition and Combustion Characteristics of Pulverized Coal-AIR Free Jets 25.4.2 Effect of Vpri on the Flame Length of Coal-Air Free Jets from a Slot Nozzle 25.4.3 Flame Lengths of the Coal-Air Free Jets from the Slot and Round Nozzles 25.4.4 Effect of Coal Concentration on the Flame Length and Ignition Delay Time 25.4.5 Mie Scattering Images of Pulverized Coal Particles 25.4.6 Simulation Results on Nozzle Effect 25.5 Conclusions References 26 Numerical Simulation on Pulverized Coal Combustion Chamber with Air Cooling 26.1 Introduction 26.2 Model and Parameters 26.2.1 The Structure of Air-Cooled Combustor 26.2.2 Research Object and Operating Condition 26.2.3 Mathematical Model 26.3 Results and Disscussion 26.3.1 The Combustion Effect and the Chamber Wall Temperature 26.3.2 Flame Shape in the Furnace 26.4 Conclusion References 27 Effect of Inner/Outer Secondary Air Mass Flow Rate on the Airflow Characteristics of the 14-MW Double Cone Burner 27.1 Introduction 27.2 Experiment Section 27.2.1 14-MW Double Cone Burner 27.2.2 Cold Air Experiments of the DC Burner Model 27.3 Results and Discussion 27.3.1 The Reynolds Numbers Experiments 27.3.2 Dimensionless Axial Velocity Distribution 27.4 Conclusions References 28 Theoretical Analyses on Isolated Particle Ignition of Coal and Biomass 28.1 Introduction 28.2 Methods 28.3 Results and Discussions 28.3.1 Ignition Time of Coal and Biomass Particles 28.3.2 Ignition Temperatures of Coal and Biomass Particles 28.3.3 Spatial Temperature and Species Distribution 28.4 Conclusion References 29 Numerical Simulation on Combustion Characteristics of Co-Firing Biomass Syngas and Coal in a 660 MW Utility Tower Boiler 29.1 Introduction 29.2 Methodology 29.2.1 Furnace and Burner Configuration 29.2.2 Fuel Properties and Cases Conditions 29.2.3 Computational Modeling 29.3 Results and Disscusion 29.3.1 Validation of the CFD Model 29.3.2 Effect of the Biomass Syngas Quality 29.3.3 Effect of Oxy-Fuel Working Condition 29.4 Conclusions References 30 Deactivation of V2O5–WO3–TiO2 SCR Catalyst by HF During Co-Firing Electrolytic Aluminum Waste with Coal 30.1 Introduction 30.2 Experiment 30.2.1 Catalyst Preparation and Deactivation of Catalyst Sample 30.2.2 Catalytic Activity Tests 30.2.3 Characterizations 30.3 Resuits and Discussion 30.3.1 SCR Catalytic Activity 30.3.2 NH3-TPD Analysis 30.3.3 BET and XRD Analysis 30.3.4 XPS Analysis 30.4 Conclusions References 31 Numerical Study on Combustion and NOx Emission Characteristics of Co-Firing Semi-Coke and Coal in a Tangentially-Fired Utility Boiler 31.1 Introduction 31.2 Boiler Description and Mesh Generation 31.3 Numerical Models and Operating Conditions 31.4 Results and Discussion 31.4.1 Influence of Semi-Coke Blending Ratio 31.4.2 Influence of Blending Mode 31.4.3 Influence of Semi-Coke Injection Position 31.5 Conclusion References 32 Investigation on NOx Formation Characteristics During Semi-coke Air-Staged Combustion 32.1 Introduction 32.2 Experimental Methods and Equipment 32.3 Results and Disscusion 32.3.1 Characteristics of NOx Formation at Non-staged Combustion Condition 32.3.2 Characteristics of NOx Formation at Air-Staged Combustion Condition 32.3.3 Microscopic Pore Structure and Morphology of Air-Graded Combustion Ash 32.4 Conclusions References 33 Numerical Investigation on Combustion Stability of Coal Slurry in the Double Cone Burner 33.1 Introduction 33.2 Experimental Set up 33.3 Numerical Modelling 33.3.1 Multiphase Flows 33.3.2 Discrete Phase Model 33.3.3 Combustion Model 33.4 Results 33.4.1 Experimental Results 33.4.2 Comparison Between Simulation and Experiment 33.4.3 Simulation Results 33.4.4 Design of Burner 33.5 Conclusion References 34 Experimental Study of NOx Emission and Char Characteristics 34.1 Introduction 34.2 Experimental Equipment 34.3 Experimental Results and Analysis 34.3.1 NOx Distribution 34.3.2 The Surface Oxygenic Functional Groups Distribution 34.3.3 The Surface Characteristics of Coal Char 34.4 Conclusions References Part IV Fluidized Bed Combustion 35 Study on Penetrability of Central Secondary Air Jet in CFB and Its Influences on Fluidization Characteristics 35.1 Introduction 35.2 Experiment 35.3 Results and Analysis 35.3.1 Influences of Total Air Volume 35.3.2 Influences of SAR 35.3.3 Influential Factors of SA Penetration Dept 35.4 Conclusions References 36 The Fundamental Studies on Combustion of Sintering Flue Gas in Circulating Fluidized Bed 36.1 Introduction 36.2 Methodology 36.2.1 Materials 36.2.2 Experimental 36.3 Results and Discussion 36.3.1 Comparison of Combustion Behavior of Coal Under Different Oxygen Contents 36.3.2 Comparison of Combustion Behavior of Coal Under Different Temperatures 36.3.3 Effect of CO on Coal Combustion 36.4 Conclusion References 37 Emission Characteristic of NOx in CFB Boiler at Low Load 37.1 Introduction 37.2 Experimental Work 37.2.1 NOx Emission Characteristic in a Bubbling Fluidized Bed 37.3 Results and Discussion 37.3.1 Experimental Stability Test 37.3.2 Comparison of NOx Emission in Different Bed Temperature 37.3.3 Comparison of NOx Emission in Different Excess Air Ratio 37.3.4 Effects of Coal Particle Size on the NOx Emission 37.4 Conclusions References 38 A Method to Measure the Solid Circulation Rate in CFB Boilers 38.1 Introduction 38.2 Methods 38.2.1 Experimental Setup 38.2.2 Numerical Simulation 38.3 Result and Discussion 38.3.1 Experimental Results 38.4 Conclusion References 39 Reliability Analysis of 100 MW and Above Circulating Fluidized Bed Boiler Units in China in 2017 39.1 Introduction 39.2 Statistics of Basic Reliability Indexes 39.3 Analysis of Unplanned Outages 39.4 Conclusion References 40 Development of Advanced Ultra Super Critical Circulating Fluidized Bed Technology by DongFang Boiler 40.1 Introduction 40.2 660 MW Advanced Ultra Supercritical CFB Boiler Scheme and Key Technical Problem Analysis 40.2.1 Boiler Scheme 40.2.2 Key Technical Problem Analysis During Boiler Development 40.3 Deviation Characteristics and Its Solution 40.3.1 Gas Solid Flow and Deviation Characteristics in EHE 40.3.2 Solution on Thermal Deviation 40.4 Environmental Protection Schemes for CFB Boilers 40.5 Summary References 41 Cold-Experimental Study About Pressure Resistance of CFB Wind Caps 41.1 Introduction 41.2 Experimental Methods 41.3 Results and Analysis 41.4 Conclusion References 42 Progress and Main Technical Characteristics of Ultra-supercritical Circulating Fluidized Bed Boiler 42.1 Research and Development of Ultra-supercritical CFB Technology 42.1.1 Tsinghua University 42.1.2 Clean Energy Technology Research Institute of Huaneng Group 42.1.3 American Foster Wheeler Company 42.1.4 ALSTOM Company of French 42.1.5 Three Major Boiler Manufacturers in China 42.2 Research and Development of Key Technologies for Ultra-supercritical CFB Boilers 42.2.1 Safety of High Temperature Heating Surface 42.2.2 Hydrodynamic Safety of Water Wall 42.2.3 Low Load Reheating Steam Temperature 42.2.4 Low Cost Ultra-low Emission Technology 42.3 Conclusion References 43 Experimental Study on Peaking Performance of 145 MW Circulating Fluidized Bed Boiler Unit with Retrofitting for Low-Vacuum Heat Supply 43.1 Introduction 43.2 Experimental Apparatus and Procedure 43.2.1 Experimental Apparatus 43.2.2 Experimental Procedure 43.3 Results and Discussion 43.3.1 Depth of Peak Regulation 43.3.2 Rate of Peak Regulation 43.3.3 Tube Wall Temperature of Superheater and Reheater 43.3.4 Bed Temperature and Furnace Negative Pressure 43.4 Conclusions References 44 The Technology and Application of a New Type of Coal Water Slurry-Fired CFB with High Efficiency and Clean Combustion 44.1 Introduction 44.2 Core Technology of Boiler Design 44.2.1 FSS Design Principle 44.2.2 Flow Pattern Reconstruction 44.3 Furnace Structure and Design Key Points 44.3.1 Determine Reasonable Furnace Structure According to CWS 44.3.2 Application of High Efficiency Adiabatic Separator 44.3.3 Application of High Flow Rate and Low Energy Consumption Self-balance Loop Seal 44.3.4 Application of Changeable Jacketed Bell-Type Air Nozzle 44.3.5 Application of Front Air Chamber with Special Structure 44.3.6 Application of Reasonable Air Distribution Device 44.3.7 Application of Low Resistance, Large Momentum with Powerful Penetrating Power Bellows Structure 44.4 Application of Reasonable Combustion Cycle and Gas/Air System 44.5 Environmental Performance 44.5.1 Basic Reaction Principle and Correlation of Desulfurization in Furnace and NOx 44.5.2 High Desulfurization Efficiency in the Furnace 44.5.3 Low NOx Initial Emission 44.5.4 Inhibition of PM2.5 Emission 44.6 Advantages of the Boiler 44.7 Applications 44.7.1 Awards 44.7.2 References 44.8 Development Prospects References 45 Study on Pollutants Control of Circulating Fluidized Bed Boiler Burning Low Calorific Value Coal 45.1 Introduction 45.2 Effect of Burning Low Calorific Value Coal on Pollutant Emission of CFB Boilers 45.3 Bed Pressure and Emission Fluctuation of Boilers Burning Low-Calorific-Value Coal 45.3.1 Adjusting the Function Relationship Between Air and Coal Volume 45.3.2 Modification of Primary Air Volume by Bed Pressure Function 45.3.3 Circulating Ash Flow Blockage in a Loop Seal 45.4 Optimization of Pollutant Control Parameters for Burning Low-Calorific-Value Coal 45.4.1 Experiments on the Coupling Relationship of Pollutant Emission 45.4.2 Control Strategy Optimization of Limestone Feeding System 45.5 Conclusion References Part V Low Carbon Energy 46 CO2 Adsorption Performance of Na/K-Impregnated MgO 46.1 Introduction 46.2 Experimental Section 46.3 Results and Discussion 46.4 Conclusion References 47 Comprehensive Analyses on Activation Agents of Amines and Nanoparticles for TETA-Based CO2 Capture Absorbents 47.1 Introduction 47.2 Materials and Methods 47.2.1 Materials 47.2.2 Experimental Process 47.2.3 Data Processing 47.3 AHP Analysis 47.3.1 Dividing Levels 47.3.2 Establishment of Judgment Matrix 47.3.3 Consistency Test 47.3.4 Signal Index Weight 47.4 Results and Discussion 47.4.1 Weight Calculation 47.4.2 Comprehensive Performance 47.5 Conclusion References 48 Experimental Study on Carbon Capture Performance of Polyimide Hollow Fiber Membrane in Post-combustion Process 48.1 Introduction 48.2 Experiment 48.2.1 Material 48.2.2 Basic Principle of Membrane Separation 48.2.3 Operating Conditions 48.3 Results and Discussion 48.3.1 Experimental Results of Single-Stage Membrane 48.3.2 Experimental Results of Two-Stage Membrane 48.4 Conclusions References 49 Simulation Study on Separation of CO2 from Flue Gas in Coal-Fired Power Plant by Membrane Method 49.1 Introduction 49.2 Simulation and Experiment 49.2.1 Model 49.2.2 Procedure 49.2.3 Experiment 49.3 Results and Discussion 49.4 Conclusion References 50 Experimental Study on Slagging and Fouling Behaviors During Oxy-Fuel Combustion of Zhundong Coal Using a Drop Tube Furnace 50.1 Introduction 50.2 Experimental 50.3 Results and Discussion 50.3.1 Slagging Characteristics in Air and Oxy-Fuel Atmospheres 50.3.2 Slagging Behaviors at Different Gas Temperatures 50.3.3 Slagging Characteristics at Different Oxygen Concentrations 50.4 Conclusions References 51 Thermodynamic Study on the Utility Oxy-Fuel Boiler with Different Oxygen Volume Fractions 51.1 Introduction 51.2 Calculation Models 51.2.1 Models of Start-up Schemes 51.2.2 Models of Furnace Heat Transfer 51.2.3 Models of Oxidant Gas 51.2.4 Models of Flue Gas Recycle (FGR) 51.3 Results and Discussions 51.3.1 Stability Analyses of the Start-up Period 51.3.2 Characteristics of Flue Gases in the Start-up Period 51.3.3 Effects of Oxygen Volume Fraction 51.4 Conclusions References Part VI Emissions Control 52 Formation of SO3 in Flue Gas Under SNCR Conditions 52.1 Experimental and Numerical Approaches 52.1.1 Experiment Approach 52.1.2 Numerical Approach 52.2 Results and Discussion 52.2.1 The SO3 Formation Under Typical SNCR Condition 52.2.2 The Influence of Inlet SO2 Mole Fraction on SO3 Formation 52.2.3 The Influence of Inlet O2 Mole Fraction on SO3 Formation 52.2.4 The Influence of Reaction Temperature on SO3 Formation 52.2.5 The Influence of Inlet CO Mole Fraction on SO3 Formation 52.2.6 The Influence of Inlet H2O Mole Fraction on SO3 Formation 52.3 Conclusions References 53 The Effect of Oxygen-Coal Equivalent Ratio on the Rapid Preparation of Powdered Activated Coke in Low Oxygen Atmosphere 53.1 Introduction 53.2 Experiment and Characterization 53.2.1 Preparation of Experimental Materials 53.2.2 Preparation of PAC 53.2.3 SO2 Adsorption Capacity 53.2.4 Characterization 53.3 Results and Discussion 53.3.1 SO2 Adsorption Capacity 53.3.2 Burn-Off Rate 53.3.3 Gas Products Analysis 53.3.4 Pore Structure and Surface Morphology 53.4 Conclusions References 54 Experimental Study on Synergistic Dust Removal of Desulfurization Tower of Coal-Fired Thermal Power Unit 54.1 Introduction 54.2 Particular Matter Concentration Measurement Method 54.3 Measurement Object 54.4 Result and Discussion 54.4.1 Comparison of the Two Measurement Methods 54.4.2 Effect of Demister on Synergistic Dust Removal of Desulfurization Tower 54.4.3 Effect of Tower Internals of Desulfurization Tower on Cooperative Dust Removal 54.4.4 Effect of Load on Synergistic Dust Removal of Desulfurization Tower 54.5 Conclusion References 55 Analysis of Desulphurization Process in Circulating Fluidized Bed Boiler by Calcium and Sulfur Conservation 55.1 Introduction 55.2 Simplified Calcium/Sulfur Conservation Methed 55.2.1 Sulfur Conservation 55.2.2 Calcium Conservation 55.3 Application Example 55.4 Conclusion References 56 Simulation Investigation on NOx Emission Characteristics and Mechanisms During Co-combustion of Fossil Fuels with Different Fuel-Nitrogen Distributions via CHEMKIN 56.1 Introduction 56.2 Models 56.3 Results and Discussion 56.3.1 The Influence of Combustion Temperature 56.3.2 The Influence of Main Combustion Zone Α 56.3.3 Influence of Blending Ratio 56.4 Conclusions References 57 Experimental Study on Combustion of Pulverized Char Preheated by a Circulating Fluidized Bed 57.1 Introduction 57.2 Experimental Section 57.2.1 Apparatus and Method 57.2.2 Fuel Characteristic 57.2.3 Experimental Conditions 57.3 Results and Discussion 57.3.1 Preheating Characteristics in CFB 57.3.2 Combustion Characteristics in DFC 57.4 Conclusion References 58 Experimental Study on Optimal Adjustment of SCR Ammonia Injection for 1000 MW Coal-Fired Unit Based on Multi-field Cooperative Diagnosis 58.1 Object of Study 58.1.1 Overview of Units 58.1.2 Test Methods 58.2 Test Results and Analysis 58.2.1 Basic Test 58.2.2 Test Results After Optimization 58.2.3 Verification Test 58.3 Conclusion References 59 Effects of High Temperature on NH3/NO Reactions in the Absence of Oxygen 59.1 Introduction 59.2 Methods 59.2.1 Experimental Set-up 59.2.2 Kinetic Modeling 59.3 Results and Discussion 59.3.1 The Influence of Residence Time 59.3.2 The Influence of NSR 59.3.3 The Influence of Temperature 59.3.4 Validation of Kinetic Model 59.3.5 Analysis of Reaction Mechanism 59.4 Conclusion References 60 Study on Kinetic Model of NOx Reduction Overall Reaction of Fluidized-Bed Flue Gas 60.1 Introduction 60.2 Model Description 60.3 Results and Discussion 60.3.1 Denitrification 60.3.2 Ammonia Slip 60.4 Conclusion References 61 The Mechanisms and Applications of NOx Reduction by Low-NOx Burner Coupling Deep Air-Staging Technology in Pulverized Coal 61.1 Introduction 61.2 Low-NOx Burner Simulation and Experiments 61.2.1 Structure of Double Cone Burner 61.2.2 Numerical Simulation of Double Cone Burner 61.2.3 Pilot Scale Experiments for Burner and the Combustion System 61.3 Industrial Experiments 61.4 Conclusions References 62 Experimental Research on NOx Emission Characteristics Based on Combined Removal Technology of Multi-pollutant with Ash Calcium Recycling 62.1 Introduction 62.2 Combined Removal Technology of Multi-pollutant with Circulating Calcium-Based Ash 62.3 Experiment 62.4 Results and Discussion 62.4.1 The Fixed Bed 62.4.2 The Bubble Bed 62.4.3 Industrial Test 62.5 Conclusion References 63 Selective Catalytic Reduction of NOx with NH3 Using Coal Ash Catalyst 63.1 Introduction 63.2 Experimental Section 63.2.1 Catalyst Preparation 63.2.2 Catalyst Characterization 63.2.3 Catalysts Activity Measurement 63.3 Results and Discussions 63.3.1 Catalyst Activity Test 63.3.2 Effect of Calcination Temperature 63.3.3 Effect of [NH3]/[NO] Molar Ratio on SCR Activity 63.3.4 Effect of Oxygen Concentration on SCR Activity 63.3.5 Catalyst Characterization 63.4 Conclusions References 64 Effects of Different Precipitants on the De–NO Efficiency of the Fe2O3 Catalyst Synthesized by Co-precipitation Method 64.1 Introduction 64.2 Catalyst Preparation 64.3 Characterization 64.4 Experimental Setup 64.5 Results and Discussion 64.5.1 NH3-SCR Activity 64.5.2 Crystalline Phase Analysis (XRD) 64.5.3 Microstructure Analysis (BET) 64.5.4 Energy Dispersive X-Ray Spectroscopy (EDS) 64.5.5 SO2 Tolerance 64.5.6 FT-IT Analysis of Fresh and Deactivated Catalyst 64.6 Conclusion References 65 In Situ Visual Monitoring of Rotary Air Preheater Blockage: Setup and Image Analysis 65.1 Introduction 65.2 Methodology 65.2.1 Setup of the Visual Monitoring System 65.2.2 3D-Printed Model Simulating the Blockage Morphology 65.2.3 Image Segmentation Algorithms 65.2.4 Influence of Noise 65.2.5 Convolutional Neural Network 65.3 Results and Discussion 65.3.1 Image Segmentation Results 65.3.2 Noise Influence 65.3.3 CNN Performance 65.4 Conclusions References 66 Effect of Chemical Composition on Adsorption and Agglomeration Characteristics of Ash Particles After Sulfuric Acid Adsorption 66.1 Introduction 66.2 Experimental Section 66.3 Results and Discussion 66.3.1 Effect of Chemical Constitution on Adsorption 66.3.2 Effect of Chemical Constitution on Particles Agglomeration 66.4 Conclusions References 67 Characteristics of Hg0 Re-emission Caused by Sulfite in a Wet Flue Gas Desulfurization System 67.1 Introduction 67.2 Experimental 67.2.1 Experimental Apparatus and Method 67.2.2 Experimental Materials 67.2.3 Calculation 67.3 Results and Discussion 67.3.1 Effect of Sulfite 67.3.2 Effect of Temperature 67.3.3 Effect of pH 67.3.4 Effect of O2 Concentration 67.3.5 Effect of Metal Ions 67.4 Conclusion References 68 Study of the Concentration of Mercury in Coal Used in Combustion, in an Area of Boyacá, Colombia, South America 68.1 Methodology 68.2 Results References 69 An Experimental Study on Ash Deposition Problem of Low-Low Temperature Flue Gas System 69.1 Introduction 69.2 Experimental Section 69.2.1 Ash Samples and Experimental Condition 69.2.2 Fixed Bed Adsorption Experimental System 69.2.3 The Entrained Flow Adsorption Experimental System 69.2.4 Calibration Tests of the Entrained Flow Adsorption Experimental System 69.3 Result and Discussion 69.3.1 The Agglomeration Effect of Ash Particles 69.3.2 The Influence of Adsorption Temperature on Agglomeration Effect 69.3.3 The Influence of Particle Size on Agglomeration Effect 69.3.4 The Flowability of Ash Particles 69.3.5 The Influence of Flue Gas Temperature on Ash Particle Flowability 69.4 Conclusions References 70 Condensation Characteristic of Sulfuric Acid Vapor on Low-Temperature Surface of Tube Heat Exchanger 70.1 Introduction 70.2 Physical and Numerical Models 70.2.1 Physical Models 70.2.2 Governing Equation 70.2.3 Vapor–Liquid Equilibrium and Interface Boundary Conditions 70.3 Physical and Numerical Models 70.3.1 Vapor–Liquid Equilibrium and Interface Boundary Conditions 70.3.2 Effect of Flue Gas Temperature and Velocity 70.3.3 Effect of Sulfuric Vapor Content in Flue Gas 70.3.4 Effect of Water Vapor Content in Flue Gas 70.3.5 Effect of Wall Temperature 70.3.6 Effect of Heat Exchanger Size 70.3.7 Effect of Heat Exchanger Arrangement 70.4 Conclusions References 71 Partitioning Behavior of Arsenic in an Ultra-Supercritical Coal-Fired Power Plant Equipped with APCDs for Ultra-Low Emission 71.1 Introduction 71.2 Materials and methods 71.2.1 Boiler Description 71.2.2 Sampling Procedure 71.2.3 Analysis Methods 71.3 Results and Discussion 71.3.1 Samples Analysis Results 71.3.2 Mass Balance Rate and Distribution of As Across the Power Plant 71.3.3 Concentration, Forms, and Removal Efficiency of As in Flue Gas Across APCDs 71.3.4 Relative Enrichment Index and Emission Factor of As 71.4 Conclusions References 72 A New Scheme for Synergetic Removal of NH3 and SO3 and Particulate Matter in the Flue Gas of Coal-Fired Boiler 72.1 Introduction 72.2 The New System 72.3 Experimental System and Procedure 72.4 Result and Discussion 72.4.1 Particle Dispersity and Size 72.4.2 Agglomeration Characteristics 72.5 Conclusion References 73 A Population Balance Model for Fine Particle Removal Inside the Electrostatic Precipitator 73.1 Introduction 73.2 Theoretical 73.3 Experimental 73.4 Results and Discussion 73.5 Conclusion References 74 Effect of Calcination Atmosphere on High Temperature H2S Removal of MnxOy/Al2O3 Sorbent in Synthesis Gas 74.1 Introduction 74.2 Experiment 74.2.1 Sorbents 74.2.2 Characterization of Sorbents 74.2.3 Desulfurization and Regeneration Tests for the Sorbents 74.3 Result and Discussion 74.3.1 H2S Absorption Capacity Over MnxOy/Al2O3 Sorbent 74.3.2 Characterization of the Sorbent Samples 74.3.3 Mechanism Analysis 74.3.4 Conclusions References Part VII Design and Operating Experiences 75 A Dataset Analysis of Particular Matter Removal Techniques in China’s Coal-Fired Power Plant 75.1 Introduction 75.2 ESP Database 75.3 Results and Discussion 75.4 Conclusions References 76 Dynamic Characteristics of a Boiler with Low-NOX Combustion 76.1 Introduction 76.2 The Tangentially Fired Boiler 76.3 Method 76.4 Results 76.5 Conclusions References 77 Study on Modeling and Control Strategy for Combustion Optimization of Pulverized Coal Boiler 77.1 Introduction 77.2 Formation Mechanism of NOX in Pulverized Coal Combustion Process 77.3 NOX Generation in Transient Process of Coal-fired Units 77.3.1 Long Short-Term Memory 77.3.2 NOX Production Prediction Model for Unit Transient Process 77.4 Optimal Control of Burner 77.4.1 Load Function Fitting 77.4.2 Optimal Scheme of Burner Switching in Variable Load Process 77.5 Summary References 78 Characteristics of RB Control Loop of Large Lignite Power Plant Boiler and Analysis and Comparison 78.1 Systematic Introduction 78.2 RB Main Circuit 78.3 RB Test Process and Problems Encountered 78.3.1 Condition 1 78.3.2 Condition 2 78.3.3 Condition 3 78.3.4 Result Analysis References 79 Power Plant Boiler Operation Optimization System Based on CO Control 79.1 Power Plant Boiler CO Monitoring Technology 79.1.1 Technical Principle 79.1.2 Flue Gas Treatment Mode 79.1.3 System Stability and Economy 79.1.4 System Installation Location 79.2 Power Plant Boiler Operation Optimization Method and System Based on CO Control 79.3 Optimized Operation of Power Plant Boiler Based on CO Control 79.4 Conclusion References 80 Technical Measures in Design and Operation of the 1000 MW Supercritical Boiler Burning High-Slagging-Propensity Coal 80.1 Introduction 80.2 Coal Properties 80.3 Technical Measures 80.4 Conclusions References 81 The Synergistic Performance of Heat and Electricity Studied from the Heating Demand Side and the Supply Side 81.1 Background 81.2 Peak Shaving Potential Analysis of Cogeneration Units 81.3 Analysis of Social Energy Conservation Caused by Deep Peak-Shaving of Heating Units 81.4 Improve the Peak-Shaving and Frequency-Regulating Ability of Cogeneration Units by Cooperative Operation 81.5 Conclusion References 82 Effect of Recirculated Flue Gas on 660 MW Double Reheated Boiler 82.1 Introduction 82.2 Geometry Model and Meshing 82.3 Numerical Model 82.4 Boundary Conditions 82.5 Effect of Load Reduction on Double Reheated Boiler 82.6 Effect of RFG 82.7 Conclusion References 83 Furnace Outlet Temperature Prediction Model of a 350 MW Ultra-Supercritical Boiler 83.1 Introduction 83.2 Model and Governing Equations 83.3 Calculation Condition, Validation and Result Analysis 83.4 Conclusion References 84 Study on the Stability of High Pressure Pneumatic Transport of the Mixture of Pulverized Coal and Extraction Residue of Direct Coal Liquefaction Residue 84.1 Introduction 84.2 Experimental Section 84.2.1 Experimental Facility and Procedure 84.2.2 Material 84.3 Results and Discussion 84.3.1 Pressure Fluctuation 84.3.2 Pressure Drop Fluctuation 84.3.3 Pulverized Coal Flow Rate, Velocity and Concentration Fluctuation 84.3.4 Conveying Stability 84.4 Conclusion References 85 Experimental Study of the Flat-Flame Pulverized Coal Gasification Technology 85.1 Introduction 85.2 Pilot Scale Test Facilities 85.3 Experimental Sample and Conditions 85.4 Results and Discussion 85.4.1 Running Conditions 85.4.2 Gasification Results 85.4.3 Gasification Temperature 85.4.4 Flow Field Analysis 85.5 Conclusion References 86 Research on Evaluation of Pulverized Coal Flow Stability in Dilute Phase Pneumatic Conveying Based on Pressure Fluctuation of Resistance Components 86.1 Introduction 86.2 Results and Discussion 86.2.1 Pressure Drop Characteristic 86.2.2 Flow Pattern Characteristic 86.2.3 Statistical Analysis of Pressure Drop Signal 86.3 Application of the Utilization of Pressure Drop Signal to Evaluate the Flow Stability 86.4 Conclusion References 87 Research on Dense Phase Pneumatic Conveying of the Mixture of Pulverized Coal and Extract Residue of Coal Liquefaction Residue at High Pressure 87.1 Introduction 87.2 Experimental Part 87.3 Results and Discussion 87.3.1 Effect of Superficial Gas Velocity on Particle Velocity 87.3.2 Effect of Fluidizing Gas on Conveying Characteristics 87.3.3 Effect of Supplemental Gas on Conveying Characteristics 87.3.4 Effect of Pressure Drop on Conveying Characteristics 87.4 Summary References 88 The Process of Self-heating Sludge Incineration Based on Granular Heat Carrier 88.1 Introduction 88.2 The Process of Sludge Incineration 88.2.1 Mixed Burning with Other Fuel 88.2.2 Incineration After Drying 88.2.3 Sludge Drying and Incineration Integration 88.3 The Process of Self-heating Sludge Incineration Based on Granular Heat Carrier 88.3.1 Process Introduction 88.3.2 Power Plant Based on the Process and Measurement Data 88.3.3 Advantages and Disadvantages 88.4 Conclusion References