Produktbild: Hydroprocessing for Clean Energy

Hydroprocessing for Clean Energy Design, Operation, and Optimization

186,99 €

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Beschreibung

Produktdetails

Einband

Gebundene Ausgabe

Erscheinungsdatum

04.01.2017

Verlag

John Wiley & Sons Inc

Seitenzahl

576

Maße (L/B/H)

23,6/16/3,3 cm

Gewicht

930 g

Auflage

1. Auflage

Sprache

Englisch

ISBN

978-1-118-92135-7

Beschreibung

Produktdetails

Einband

Gebundene Ausgabe

Erscheinungsdatum

04.01.2017

Verlag

John Wiley & Sons Inc

Seitenzahl

576

Maße (L/B/H)

23,6/16/3,3 cm

Gewicht

930 g

Auflage

1. Auflage

Sprache

Englisch

ISBN

978-1-118-92135-7

Herstelleradresse

Libri GmbH
Europaallee 1
36244 Bad Hersfeld
DE

Email: [email protected]

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  • Produktbild: Hydroprocessing for Clean Energy
  • Preface xiii

    Part 1 Fundamentals 1

    1 Overview of This Book 3

    1.1 Energy Sustainability 3

    1.2 ULSD - Important Part of the Energy Mix 4

    1.3 Technical Challenges for Making ULSD 7

    1.4 What is the Book Written for 8

    References 8

    2 Refinery Feeds Products and Processes 9

    2.1 Introduction 9

    2.2 ASTM Standard for Crude Characterization 10

    2.3 Important Terminologies in Crude Characterization 12

    2.4 Refining Processes 13

    2.5 Products and Properties 15

    2.6 Biofuel 20

    3 Diesel Hydrotreating Process 23

    3.1 Why Diesel Hydrotreating? 23

    3.2 Basic Process Flowsheeting 25

    3.3 Feeds 28

    3.4 Products 30

    3.5 Reaction Mechanisms 36

    3.6 Hydrotreating Catalysts 40

    3.7 Key Process Conditions 44

    3.8 Different Types of Process Designs 47

    References 48

    4 Description of Hydrocracking Process 51

    4.1 Why Hydrocracking 51

    4.2 Basic Processing Blocks 53

    4.3 Feeds 58

    4.4 Products 59

    4.5 Reaction Mechanism and Catalysts 61

    4.6 Catalysts 67

    4.7 Key Process Conditions 70

    4.8 Typical Process Designs 75

    References 78

    Part 2 Hydroprocessing Design 79

    5 Process Design Considerations 81

    5.1 Introduction 81

    5.2 Reactor Design 81

    5.3 Recycle Gas Purity 98

    5.4 Wash Water 102

    5.5 Separator Design 107

    5.6 Makeup Gas Compression 115

    References 121

    6 Distillate Hydrotreating Unit Design 123

    6.1 Introduction 123

    6.2 Number of Separators 123

    6.3 Stripper Design 127

    6.4 Debutanizer Design 135

    6.5 Integrated Design 136

    References 147

    7 Hydrocracking Unit Design 149

    7.1 Introduction 149

    7.2 Single-stage Hydrocracking Reactor Section 150

    7.3 Two-stage Hydrocracking Reactor Section 155

    7.4 Use of a Hot Separator in Hydrocracking Unit Design 158

    7.5 Use of Flash Drums 160

    7.6 Hydrocracking Unit Fractionation Section Design 161

    7.7 Fractionator First Flow Scheme 161

    7.8 Debutanizer First Flow Scheme 163

    7.9 Stripper First Fractionation Flow Scheme 166

    7.10 Dual Zone Stripper Fractionation Flow Scheme 168

    7.11 Dual Zone Stripper - Dual Fractionator Flow Scheme 170

    7.12 Hot Separator Operating Temperature 171

    7.13 Hydrogen Recovery 174

    7.14 LPG Recovery 175

    7.15 HPNA Rejection 177

    7.16 Hydrocracking Unit Integrated Design 181

    References 187

    Part 3 Energy and Process Integration 189

    8 Heat Integration for Better Energy Efficiency 191

    8.1 Introduction 191

    8.2 Energy Targeting 191

    8.3 Grassroots Heat Exchanger Network (Hen) Design 202

    8.4 Network Pinch for Energy Retrofit 206

    Nomenclature 213

    References 213

    9 Process Integration for Low-Cost Design 215

    9.1 Introduction 215

    9.2 Definition of Process Integration 216

    9.3 Grand Composite Curves (GCC) 218

    9.4 Appropriate Placement Principle for Process Changes 219

    9.5 Dividing Wall Distillation Column 225

    9.6 Systematic Approach for Process Integration 228

    9.7 Applications of the Process Integration Methodology 230

    9.8 Summary of Potential Energy Efficiency Improvements 246

    References 247

    10 Distillation Column Operating Window 249

    10.1 Introduction 249

    10.2 What is Distillation? 249

    10.3 Why Distillation is the Most Widely Used? 251

    10.4 Distillation Efficiency 253

    10.5 Definition of Feasible Operating Window 255

    10.6 Understanding Operating Window 256

    10.7 Typical Capacity Limits 275

    10.8 Effects of Design Parameters 275

    10.9 Design Checklist 278

    10.10 Example Calculations for Developing Operating Window 281

    10.11 Concluding Remarks 296

    Nomenclature 297

    References 299

    Part 4 Process Equipment Assessment 301

    11 Fired Heater Assessment 303

    11.1 Introduction 303

    11.2 Fired Heater Design for High Reliability 304

    11.3 Fired Heater Operation for High Reliability 310

    11.4 Efficient Fired Heater Operation 315

    11.5 Fired Heater Revamp 321

    Nomenclature 322

    References 322

    12 Pump Assessment 323

    12.1 Introduction 323

    12.2 Understanding Pump Head 324

    12.3 Define Pump Head - Bernoulli Equation 325

    12.4 Calculate Pump Head 329

    12.5 Total Head Calculation Examples 330

    12.6 Pump System Characteristics - System Curve 332

    12.7 Pump Characteristics - Pump Curve 333

    12.8 Best Efficiency Point (BEP) 338

    12.9 Pump Curves for Different Pump Arrangement 338

    12.10 Npsh 340

    12.11 Spillback 345

    12.12 Reliability Operating Envelope (ROE) 346

    12.13 Pump Control 347

    12.14 Pump Selection and Sizing 347

    Nomenclature 351

    References 351

    13 Compressor Assessment 353

    13.1 Introduction 353

    13.2 Types of Compressors 354

    13.3 Impeller Configurations 357

    13.4 Type of Blades 358

    13.5 How a Compressor Works 358

    13.6 Fundamentals of Centrifugal Compressors 360

    13.7 Performance Curves 362

    13.8 Partial Load Control 364

    13.9 Inlet Throttle Valve 366

    13.10 Process Context for a Centrifugal Compressor 367

    13.11 Compressor Selection 368

    Nomenclature 369

    References 369

    14 Heat Exchanger Assessment 371

    14.1 Introduction 371

    14.2 Basic Concepts and Calculations 371

    14.3 Understand Performance Criterion - U Values 374

    14.4 Understand Fouling 380

    14.5 Understand Pressure Drop 382

    14.6 Effects of Velocity on Heat Transfer Pressure Drop and Fouling 384

    14.7 Heat Exchanger Rating Assessment 385

    14.8 Improving Heat Exchanger Performance 396

    Nomenclature 399

    References 400

    15 Distillation Column Assessment 401

    15.1 Introduction 401

    15.2 Define a Base Case 401

    15.3 Calculations for Missing and Incomplete Data 403

    15.4 Building Process Simulation 406

    15.5 Heat and Material Balance Assessment 408

    15.6 Tower Efficiency Assessment 411

    15.7 Operating Profile Assessment 414

    15.8 Tower Rating Assessment 417

    15.9 Guidelines 419

    Nomenclature 420

    References 420

    Part 5 Process System Evaluation 423

    16 Energy Benchmarking 425

    16.1 Introduction 425

    16.2 Definition of Energy Intensity for a Process 426

    16.3 The Concept of Fuel Equivalent for Steam and Power (FE) 427

    16.4 Data Extraction 429

    16.5 Convert All Energy Usage to Fuel Equivalent 432

    16.6 Energy Balance 432

    16.7 Fuel Equivalent for Steam and Power 435

    16.8 Energy Performance Index (EPI) Method for Energy Benchmarking 441

    16.9 Concluding Remarks 444

    16.10 Nomenclature 445

    References 446

    17 Key Indicators and Targets 447

    17.1 Introduction 447

    17.2 Key Indicators Represent Operation Opportunities 448

    17.3 Define Key Indicators 451

    17.4 Set Up Targets for Key Indicators 456

    17.5 Economic Evaluation for Key Indicators 460

    17.6 Application 1: Implementing Key Indicators into an "Energy Dashboard" 463

    17.7 Application 2: Implementing Key Indicators to Controllers 465

    17.8 It is Worth the Effort 466

    Nomenclature 467

    References 467

    18 Distillation System Optimization 469

    18.1 Introduction 469

    18.2 Tower Optimization Basics 470

    18.3 Energy Optimization for Distillation System 475

    18.4 Overall Process Optimization 481

    18.5 Concluding Remarks 489

    References 490

    Part 6 Operational Guidelines and Troubleshooting 491

    19 Common Operating Issues 493

    19.1 Introduction 493

    19.2 Catalyst Activation Problems 494

    19.3 Feedstock Variations and Contaminants 495

    19.4 Operation Upsets 496

    19.5 Treating/Cracking Catalyst Deactivation Imbalance 497

    19.6 Flow Maldistribution 500

    19.7 Temperature Excursion 501

    19.8 Reactor Pressure Drop 504

    19.9 Corrosion 506

    19.10 Hpna 509

    19.11 Conclusion 511

    20 Troubleshooting Case Analysis 513

    20.1 Introduction 513

    20.2 Case Study I - Product Selectivity Changes 514

    20.3 Case Study II - Feedstock Changes 516

    20.4 Case Study III - Catalyst Deactivation Balance 523

    20.5 Case Study IV - Catalyst Migration 526

    20.6 Conclusion 536

    Index 537