| Abstract | 第4-5页 |
| 摘要 | 第6-11页 |
| Nomenclature | 第11-14页 |
| Chapter 1 Introduction | 第14-26页 |
| 1.1 Background of thesis research | 第15-21页 |
| 1.2 Objective | 第21-22页 |
| 1.3 Literature review and research progress | 第22-26页 |
| Chapter 2 System design Consideration | 第26-40页 |
| 2.1 Lithium Bromide | 第26-28页 |
| 2.1.1 Main description of lithium-Bromide | 第26页 |
| 2.1.2 Chemical and physical properties | 第26-27页 |
| 2.1.3 Featured thermochemical properties of lithium Bromide | 第27-28页 |
| 2.2 System construction alloys | 第28-36页 |
| 2.3 System working fluid | 第36-37页 |
| 2.4 New designed system structure and work principles | 第37-39页 |
| 2.5 Chapter summary | 第39-40页 |
| Chapter 3 System components and analysis | 第40-58页 |
| 3.1 System structure and work theory | 第40-42页 |
| 3.2 System thermodynamic analysis | 第42-45页 |
| 3.2.1 System solution properties and analysis | 第42-43页 |
| 3.2.2 The pressure of the vapour of lithium bromide-water solution | 第43-44页 |
| 3.2.3 The Enthalpy of mixture solution Water-Lithium bromide | 第44页 |
| 3.2.4 Enthalpy of pure water (superheated vapour) | 第44-45页 |
| 3.3 Steady flow analysis of New designed System | 第45-46页 |
| 3.4 Thermodynamic system components modelling | 第46-50页 |
| 3.4.1 Steam absorber | 第46-47页 |
| 3.4.2 Steam Generator (Boiler and Super-heater) | 第47-48页 |
| 3.4.3 Steam turbine | 第48-50页 |
| 3.5 System masses flow rate modeling | 第50-51页 |
| 3.6 System thermodynamics analysis by use endoreversible approach | 第51-57页 |
| 3.6.1 General considerations | 第51-52页 |
| 3.6.2 FFT modelling | 第52-55页 |
| 3.6.3 Endo-reversible approach and system efficiency at maximum power | 第55-57页 |
| 3.7 Chapter Summary | 第57-58页 |
| Chapter 4 System simulation results and performance analysis | 第58-100页 |
| 4.1 The main comprehensions | 第58-59页 |
| 4.2 Systems considerations and assumptions for the analysis | 第59-60页 |
| 4.2.1 Steam Rankine Cycle software design considerations | 第59页 |
| 4.2.2 New designed system working considerations for the simulation | 第59-60页 |
| 4.3 Simulation software review | 第60-62页 |
| 4.4 Performance analysis, comparison, and simulation result discussions whenSteam Rankine cycle work at virtually operating conditions | 第62-77页 |
| 4.4.1 By increasing the low side pressure gradually to specific limitation | 第62-65页 |
| 4.4.2 By keeping the low side pressure at constant level, then decrease the highside pressure gradually to specific terms | 第65-68页 |
| 4.4.3 by keep the system low side pressure and temperature constant anddecreasing the system temperature max gradually | 第68-71页 |
| 4.4.4 By keeping systems low pressures constant at specific level andcontinuing from decreasing the systems pressures and temperatures max | 第71-73页 |
| 4.4.5 By lower the system minimum pressure to minimum recommended level and keep decreasing the system temperature max gradually until the failure of the system | 第73-77页 |
| 4.5 Performance analysis, comparison, and simulation result when Steam Rankinecycle work at actually operating conditions | 第77-96页 |
| 4.5.1 By increasing the system low side pressure gradually until specificlimitation at real operating conditions | 第77-80页 |
| 4.5.2 By decreasing the systems high side pressure gradually and keep othersystems input parameters constant at real operating standardizations | 第80-84页 |
| 4.5.3 By decreasing the system high side temperature gradually at minimumcondenser pressure of Rankine cycle | 第84-87页 |
| 4.5.4 Systems performance test and comparison by decreasing the | 第87-90页 |
| 4.5.5 Improve the power output of the new designed system by lower the | 第90-92页 |
| 4.5.6 Applying minimum selected parameters on both systems and decreasingthe systems temperatures and pressures max gradually until system failure | 第92-96页 |
| 4.6 System thermodynamics analysis results by use Endo-reversible approach | 第96-100页 |
| Conclusion | 第100-102页 |
| Future studies | 第102-103页 |
| References | 第103-110页 |
| Acknowledgement | 第110-111页 |
| Resume | 第111-112页 |
| Appendixes | 第112-115页 |
