| 摘要 | 第4-6页 |
| ABSTRACT | 第6-8页 |
| 创新点 | 第9-14页 |
| Chapter 1. Introduction | 第14-32页 |
| 1.1 Research background | 第14-16页 |
| 1.2 Organic Rankine Cycle (ORC) technology | 第16-24页 |
| 1.2.1 Organic Rankine cycle (ORC) operation principle | 第18-22页 |
| 1.2.2 Application of organic Rankine cycles (ORCs) | 第22-24页 |
| 1.2.3 ORC investigated in this dissertation | 第24页 |
| 1.3 Main research area concerning ORC | 第24-27页 |
| 1.3.1 Working fluid selection and new working fluids | 第24-25页 |
| 1.3.2 Process optimization and integration of ORC | 第25-26页 |
| 1.3.3 Techno-economic optimization of ORC | 第26-27页 |
| 1.4 Methods and tools | 第27-30页 |
| 1.5 Dissertation organization | 第30-32页 |
| Chapter 2. Working fluid selection considering waste heat source characteristics | 第32-84页 |
| 2.1 Motivation | 第32页 |
| 2.2 Approach overview | 第32-37页 |
| 2.2.1 Characteristics and requirement of organic working fluids | 第32-34页 |
| 2.2.2 Specific literature review | 第34-37页 |
| 2.3 Working fluid preselection and waste heat source classification | 第37-41页 |
| 2.4 Working fluid selection for sensible heat source | 第41-66页 |
| 2.4.1 Working fluid selection for sensible heat source without targettemperature constraints | 第41-60页 |
| 2.4.2 Working fluid selection for sensible heat source with targettemperature constraints | 第60-66页 |
| 2.5 Working fluid selection for combined waste heat source | 第66-81页 |
| 2.5.1 Effect of the ratio of latent to sensible heat on working fluidselection for combined heat sources | 第67-73页 |
| 2.5.2 Effect of inlet temperature of waste heat on working fluid selectionfor combined heat sources | 第73-78页 |
| 2.5.3 Effect of target temperature of waste heat on working fluid selectionfor combined heat sources | 第78-81页 |
| 2.5.4 Discussion on working fluid selection for combined waste heatsources | 第81页 |
| 2.6 Working fluid selection for latent heat source | 第81页 |
| 2.7 Summary | 第81-84页 |
| Chapter 3. Process integration and optimization of organic Rankine cycles fordirect waste heat recovery | 第84-112页 |
| 3.1 Motivation | 第84页 |
| 3.2 Approach overview | 第84-87页 |
| 3.3 Problem statement | 第87-90页 |
| 3.4 Model formulation | 第90-102页 |
| 3.4.1 Model to determine the ORC configuration and operatingconditions | 第90-101页 |
| 3.4.2 Model to determine the heat exchanger network structure | 第101-102页 |
| 3.5 Case study | 第102-110页 |
| 3.6 Summary | 第110-112页 |
| Chapter 4. Systematically customizing an organic Rankine cycle to a process forindirect waste heat recovery | 第112-142页 |
| 4.1 Motivation | 第112-113页 |
| 4.2 Approach review | 第113页 |
| 4.3 Problem statement | 第113-115页 |
| 4.4 Heat exchanger network synthesis considering waste heat utilization | 第115-117页 |
| 4.5 Hot water flow rate determination and waste heat recovery networksynthesis | 第117-120页 |
| 4.6 Simultaneous determination of working fluid and operating conditions ofthe ORC system | 第120-121页 |
| 4.7 Procedures of the proposed method | 第121-122页 |
| 4.8 Case study | 第122-140页 |
| 4.8.1 Scenario 1: Customizing ORC to the system without heat exchangernetwork modification | 第124-126页 |
| 4.8.2 Scenario 2: Customizing the ORC to the system consideringmodification of heat exchange violating pinch design principles | 第126-132页 |
| 4.8.3 Scenario 3: Customize ORC to the system considering waste heatupgrading on the basis of Scenario 2 | 第132-137页 |
| 4.8.4 Comparison of three Scenarios | 第137-140页 |
| 4.9 Summary | 第140-142页 |
| Chapter 5. Simultaneous heat integration and techno-economic optimization oforganic Rankine cycle (ORC) for indirect waste heat recovery | 第142-164页 |
| 5.1 Motivation | 第142页 |
| 5.2 Approach overview | 第142-143页 |
| 5.3 Problem statement | 第143-145页 |
| 5.4 Model description | 第145-155页 |
| 5.4.1 Duran-Grossmann model | 第145-146页 |
| 5.4.2 Thermodynamic model of ORC | 第146-151页 |
| 5.4.3 Cost correlations | 第151-152页 |
| 5.4.4 Objective function | 第152-153页 |
| 5.4.5 Determination of the optimal HRAT | 第153-155页 |
| 5.5 Case study | 第155-161页 |
| 5.5.1 Optimization with N-butane (R600) as working fluid | 第155-159页 |
| 5.5.2 Comparison of different working fluids | 第159-161页 |
| 5.6 Sensitivity analysis | 第161-162页 |
| 5.7 Summary | 第162-164页 |
| Chapter 6. Conclusion and future work | 第164-167页 |
| 6.1 Conclusion | 第164-165页 |
| 6.2 Future work | 第165-167页 |
| Nomenclatures | 第167-172页 |
| References | 第172-181页 |
| Appendix A: Peng-Robinson Equation | 第181-183页 |
| Appendix B: The initialization of cubic equations of state | 第183-188页 |
| Appendix C: Working fluids thermodynamic parameters in Chapter 5 | 第188-189页 |
| 致谢 | 第189-190页 |
| 个人简历、在学期间发表的学术论文及研究成果 | 第190-191页 |
| 学位论文数据集 | 第191页 |
