16 research outputs found
μμ°¨μ μΉ΄λ₯΄λ Έ μ¬μ΄ν΄μ μ΄μνμ νΉμ±κ³Ό μ΄νν μμ€ν μμμ μμ©μ κ΄ν μ°κ΅¬
νμλ
Όλ¬Έ (λ°μ¬)-- μμΈλνκ΅ λνμ : κΈ°κ³ν곡곡νλΆ, 2015. 8. κΉλ―Όμ.Since the fossil fuels, which meet most of the energy requirements in the world, are not environmental friendly and its present stocks are finite, various renewable energy sources have been introduced as a promising option to fill increasing demand of worldwide energy. Although some typical renewable energy sources, such as solar photovoltaic energy, wind energy, and hydrogen energy of fuel cells, are directly converted into electricity, a lot of renewable sources, such as solar thermal energy, industrial waste heat, geothermal energy, and ocean thermal energy, still exist in the form of heat. These thermal energy sources categorized as low grade heat source because they have low temperature and relatively small heat capacity, requires some thermodynamic cycles to generate useful power.
Generally, Carnot cycle, has been used in the evaluation of the thermal system as a standard. However, considering that the characteristics of renewable heat sources are different from those of conventional sources, it may not be the best choice to use just a single Carnot cycle for analyzing renewable thermal energy system as it deals with the heat source of infinite heat capacity. Therefore, the sequential Carnot cycle has been suggested, where a number of individual Carnot cycles are arranged in parallel. In contrast to the original Carnot cycle, the sequential cycle considers the temperature change in heat sources which occurs at the heat transfer process between the cycle and heat sources. Moreover, in case of a sequential Carnot cycle, the heat transfer rate between the cycle and heat sources is calculated by taking account of temperature difference between them.
In this study, the thermodynamic characteristics of sequential Carnot cycles, such as the efficiency and power output of the system in various conditions, are investigated. Using basic model for the sequential system, which is advanced from the initial one suggested earlier, the performance of sequential Carnot cycles is calculated in an analytical way. For the analysis, only fundamental relations of thermodynamics and heat transfer are utilized, instead of complex numerical techniques. The effect of major variables, which are the number of individual Carnot cycles in the system, the inventory of heat exchangers used and the final temperature of heat sources, on the system performance is researched and some optimization processes are also conducted based on those results. During the analysis, some symbolic expressions are obtained, which can be utilized effectively in actual situations.
Also, to bridge the gap between the practical thermal system and the sequential Carnot cycle, more detailed sequential system models are proposed. Different from the previous one, this model adopts the heat sink with finite heat capacity and has some internal irreversibilities in contrast with Carnot cycles. How these features influences the system performance is discovered by analytical equations which are derived from the process similar to that used in the basic model.
By the way, throughout the theoretical research, the interesting phenomenon is obeserved, which is that the efficiency of the sequential system increases along with the number of individual Carnot cycles in the system. Paying attention to the possibility that this result can also be applied to actual thermodynamic systems, the numerical simulation using thermodynamic properties of real working fluids is carried out targeting organic Rankine cycles (ORC) and heat pumps. As a result, it is found that the concept of sequential cycles has advantages in actual cases.
Finally, the experimental setup for a sequential heat pump, which has two refrigeration cycles in one system, is prepared to validate the result of numerical calculation. The experiment is conducted with not only a sequential heat pump, but also a simple conventional heat pump, which have the same heat capacity. After comparing coefficients of performance (COP) of both systems, it can be found that the sequential heat pump has higher efficiency than the simple heat pump. It can be expected that the result of this research, such as simple expressions from sequential Carnot cycles, is widely used in various situations related with renewable thermal energy sources or a lot of researches about sequential thermal cycles will be initiated by this study.Abstract i
Contents v
List of Figures viii
List of Tables xiii
Nomenclature xiv
Chapter 1. Introduction 1
1.1 Background of the study 1
1.2 Literature survey 6
1.3 Objectives and scopes 11
Chapter 2. Thermodynamic analysis of basic sequential Carnot cycles 14
2.1 Introduction 14
2.2 System description 16
2.3 Analytical modeling of the cycle 19
2.4 Parametric study for the performance of the cycle 22
2.5 Analytical modeling for exergy analysis 30
2.6 Result of exergy analysis 36
2.7 Summary 42
Chapter 3. Advanced analysis and optimization study on sequential Carnot cycles 44
3.1 Introduction 44
3.2 Sequential Carnot cycle with finite heat sink 46
3.2.1 Analytical modeling of the cycle 46
3.2.2 Performance of advanced sequential Carnot cycles 50
3.3 Sequential Carnot cycle with internal irreversibility 60
3.3.1 Analytical modeling of the cycle 60
3.3.2 Performance of sequential cycles with internal irreversibility 65
3.4 Optimization of sequential systems 72
3.4.1 The optimal distribution of heat exchanger inventory 72
3.4.2 The optimal TF in sequential systems 85
3.4.3 The optimal NTUH/NTUL in sequential systems 93
3.5 Summary 101
Chapter 4. Practical research for sequential heat pump. 103
4.1 Introduction 103
4.2 Numerical simulation of the sequential system 105
4.2.1 Simulation model of the system 105
4.2.2 The results numerical simulation 111
4.3 The experimental study on the sequential heat pump 121
4.3.1 Experimental methodology 121
4.3.2 Experimental result 129
4.4 Summary 142
Chapter 5. Concluding remarks 143
References 146
Abstract (in Korean) 152Docto
R134aμ R410Aλ₯Ό μ¬μ©ν μΊμ€μΌμ΄λ λλ μμ€ν μ μ΅μ μ€κ°μ¨λμ λν μ°κ΅¬
νμλ
Όλ¬Έ (μμ¬)-- μμΈλνκ΅ λνμ : κΈ°κ³ν곡곡νλΆ, 2012. 2. κΉλ―Όμ.The eco-friendly heat pump system which brings high efficiency has gained a lot of attention and becomes one of the major facilities in refrigeration and air-conditioning. In case of producing hot water, however, replacement of existing hot water supply systems which use fossil fuel as a heat source with heat pump water heaters has not been progressed effectively because providing hot water with heat pump systems has some disadvantages. Major weaknesses of heat pump water heaters are that their heat capacity is deteriorated in cold climate and their maximum water temperature has some limitations by refrigerants used and systems.
To overcome those drawbacks, a cascade cycle using R134a and R410A is adopted in a heat pump water heater system. A cascade cycle in a refrigeration system has two different refrigerants as working fluids in separated loops: a high-temperature cycle, and a low-temperature cycle. By operating two divided loops in one system, the problems mentioned earlier can be handled properly. While the cascade system can solve the problems of existing heat pump water heaters, it raises some control issues since the number of devices composing the cycle increases in a cascade system. One of the most important and unique control parameters in a cascade refrigeration cycle is the intermediate temperature which is an evaporating temperature of a high-temperature cycle. In this study, the optimal intermediate temperature for the maximum COP was investigated in an analytical and an experimental way.
In an analytical study, a new equation which can calculate the optimal intermediate temperature was suggested. This formula was derived by fundamental thermodynamic laws without additional numerical data. Some assumptions were employed to model a complex system, such as an isothermal heat transfer process. In addition, regression analysis was also applied in the equation to reflect the thermodynamic characteristic of refrigerants. Optimal values from this equation were compared with an existing correlation and its tendency according to other conditions was studied.
To prove the validity of an analytical result, experiments were carried out. Experiments were conducted under a steady-state condition with an intermediate temperature changed. Major operating conditions were also adjusted to identify their effects and experimental optimum value of intermediate temperature and corresponding COP were determined in each case. Finally, the experimental results were compared with an analytical result to secure the validity of an analytic solution.μΉνκ²½μ μ΄λ©° κ³ ν¨μ¨λ‘ μλνλ ννΈνν μμ€ν
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