1,451 research outputs found

    A HYBRID AIR CONDITIONER DRIVEN BY A HYBRID SOLAR COLLECTOR

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    The objective of this thesis is to search for an efficient way of utilizing solar energy in air conditioning applications. The current solar Air Conditioners (A/C)s suffer from low Coefficient of Performance (COP) and performance degradation in hot and humid climates. By investigating the possible ways of utilizing solar energy in air conditioning applications, the bottlenecks in these approaches were identified. That resulted in proposing a novel system whose subsystem synergy led to a COP higher than unity. The proposed system was found to maintain indoor comfort at a higher COP compared to the most common solar A/Cs, especially under very hot and humid climate conditions. The novelty of the proposed A/C is to use a concentrating photovoltaic/thermal collector, which outputs thermal and electrical energy simultaneously, to drive a hybrid A/C. The performance of the hybrid A/C, which consists of a desiccant wheel, an enthalpy wheel, and a vapor compression cycle (VCC), was investigated experimentally. This work also explored the use of a new type of desiccant material, which can be regenerated with a low temperature heat source. The experimental results showed that the hybrid A/C is more effective than the standalone VCC in maintaining the indoor conditions within the comfort zone. Using the experimental data, the COP of the hybrid A/C driven by a hybrid solar collector was found to be at least double that of the current solar A/Cs. The innovative integration of its subsystems allows each subsystem to do what it can do best. That leads to lower energy consumption which helps reduce the peak electrical loads on electric utilities and reduces the consumer operating cost since less energy is purchased during the on peak periods and less solar collector area is needed. In order for the proposed A/C to become a real alternative to conventional systems, its performance and total cost were optimized using the experimentally validated model. The results showed that for an electricity price of 0.12 $/kW-hr, the hybrid solar A/C's cumulative total cost will be less than that of a standard VCC after 17.5 years of operation

    Experimental Study on a Finned-tube Internally Cooled Contactor for Liquid Desiccant air conditioning systems with Ionic Liquid

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    This paper presents an experimental study on the dehumidification performance of a finned-tube internally cooled contactor as compared to that of an adiabatic contactor in liquid desiccant air conditioning systems with ionic liquid. The contactor is the most significant component in liquid desiccant systems; it is the component responsible for the dehumidification and regeneration processes. When air and absorptive solution are in contact in the contactor, absorption/desorption of the solution occurs due to the difference in vapor pressure. This results to the transfer of heat and mass between the air and solution. Conventionally, adiabatic contactors, which only have air and solution interaction are being used for the dehumidification/regeneration process of liquid desiccant systems. On the contrary, internally cooled contactors are being suggested as these have the possibility of realizing a more efficient dehumidification process. This is possible as internally cooled contactors can maintain the dehumidification ability of the absorptive solution by utilizing cooling water as a third fluid in the contactor for removing the heat of absorption. In other words, internally cooled contactors have the possibility of reducing the circulating solution mass flux and, hence, the power consumption of the solution pumps. In this research, the dehumidification ability of a finned-tube internally cooled contactor is experimentally studied. In order to increase the heat transfer ability of the cooling water, aluminium, which has a high thermal conductivity, is used as the contactor material. Although Lithium Chloride solution is a conventional absorptive solution, it corrodes aluminum; therefore, ionic liquid is used as the absorptive solution in this experiment since it does not corrode aluminum. Research on this new combination of contactor and absorptive solution is not extensively done at present; this research provides new and valuable information for future research. Moreover, the results were compared with that of an adiabatic contactor in order to analyze the difference in dehumidification ability between the two of contactors. As a result, outlet air dew point temperatures lower than the cooling water temperature were achieved, which emphasize the advantage of liquid desiccant air conditioning system to conventional vapor compression air conditioning systems. Furthermore, the outlet air dew point temperatures of the internally cooled contactor were lower than that of adiabatic contactor for low mass fluxes, and converged at higher solution mass flux. This suggests the significant effect of the cooling water to the dehumidification ability of the absorptive solution. Experimental data of the dehumidification ability of this new combination of aluminum finned-tube contactor and ionic liquid solution are promising for further research about the structure of contactors. These results provide significant information for the improvement in the design of liquid desiccant air conditioning systems

    Mathematical Model and Performance Analysis of a Liquid Desiccant Dehumidification Tower

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    A finite difference model simulating a liquid desiccant dehumidification tower with lithium chloride as the desiccant solution has been developed. The model determines the packing height needed for a condensation rate. Comparisons with experimental data illustrates that the model produces valid results. Air and desiccant solution temperatures within the dehumidification tower show that a temperature increase is experienced for both the air and desiccant solution from their respective entrances and exits from the tower. Increasing the air mass velocity or the amount of moisture removed from the air supply causes an increase in packing height. Increasing the desiccant mass velocity decreases the packing height

    ์ œ์Šต์ œ ์ฝ”ํŒ… ์—ด๊ตํ™˜๊ธฐ๋ฅผ ์ ์šฉํ•œ ์ „๊ธฐ์ž๋™์ฐจ์šฉ ํžˆํŠธํŽŒํ”„ ์‹œ์Šคํ…œ ์„ฑ๋Šฅ ๋ถ„์„

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    ํ•™์œ„๋…ผ๋ฌธ(๋ฐ•์‚ฌ) -- ์„œ์šธ๋Œ€ํ•™๊ต๋Œ€ํ•™์› : ๊ณต๊ณผ๋Œ€ํ•™ ๊ธฐ๊ณ„ํ•ญ๊ณต๊ณตํ•™๋ถ€(๋ฉ€ํ‹ฐ์Šค์ผ€์ผ ๊ธฐ๊ณ„์„ค๊ณ„์ „๊ณต), 2021.8. ๊น€๋ฏผ์ˆ˜.In this study, a heat pump system of an electric vehicle (EV) with a novel dehumidifier is suggested and validated by modeling and experiment. The aim of the study is the determination of the energy consumption of the proposed system. The driving range of a conventional EV sharply drops when operating the MHP system for heating or defogging. Because the traditional MHP consumes a lot of energy since it used the condensing method to remove moisture. It means that the air temperature must be lower than dew points to occurs condensation on the metal fins of a heat exchanger, then the air should be reheated to supply into the cabin. In this study, to solve this irrational process for dehumidification, a solid desiccant coated heat exchanger (DCHE) is introduced which is able to heat and mass transfer simultaneously for removing water vapor in the cabin air and recovering waste heat from power electronics and electric machineries (PEEM). To attach the desiccant material onto the metal fin of a heat exchanger, a binder should be necessary. Thus, the proper pair of the desiccant and binder is selected. After analyzing the physical properties of the adsorbent, the optimum binder contents ratio is obtained. Then, the numerical model of the DCHE was developed base on the thermal resistance method to predict the adsorption performance of the DCHE. To validate the predicted results, the DCHE was fabricated and the test facility was also constructed. The simulation results show good agreement with the experimental data. To obtain the power consumption of the MHP, the numerical model of the MHP was developed. The compressor characteristics were determined by preliminary test since it is a crucial component of the MHP and it strongly affects the performance of the MHP system. Similar to the DCHE model, heat exchangers of the MHP also modeled using the thermal resistance method by discrete as small segments. To validate the developed MHP model, the experimental apparatus was constructed and conducted experiments. As a result, the simulation results reveal small differences as compared with the experimental data. Owing to determine the effect of the DCHE on the energy consumption of the MHP to satisfy the cabin target condition, the simulation was conducted by integrated the developed numerical model in the Simulink program. Simulation results reveal that the system with DCHE achieves a reduction in energy consumption as compared to the traditional system. Because the DCHE led to decreasing the operation time of the MHP by adsorption the water vapor in the cabin air, and by heating to approach the cabin air temperature to the setpoint. In conclusion, the novel configuration which is utilized the DCHE in the automobile heat pump system is suggested in this study. And the DCHE effects on the energy reduction of the automobile heat pump system were investigated. Conclusively, the DCHE helps to reduce energy consumption.์ฐจ๋Ÿ‰ ํƒ‘์Šน๊ฐ์˜ ์—ด์พŒ์ ์„ฑ๊ณผ ์šด์ „ ์•ˆ์ „์„ฑ ํ™•๋ณด๋ฅผ ์œ„ํ•˜์—ฌ, ๋ƒ‰๋‚œ๋ฐฉ ๊ณต์กฐ ์‹œ์Šคํ…œ์„ ๊ฐ€๋™ํ•˜์—ฌ ์ฐจ๋Ÿ‰์‹ค๋‚ด ๋ƒ‰๋‚œ๋ฐฉ ๋ฐ ๊น€์„œ๋ฆผ ์ œ๊ฑฐํ•œ๋‹ค. ์ด๋Ÿฌํ•œ ๊ณต์กฐ์‹œ์Šคํ…œ์„ ์šด์ „ํ•˜๊ธฐ ์œ„ํ•œ ์—๋„ˆ์ง€ ์†Œ๋น„๋Š” ๋ถˆ๊ฐ€ํ”ผํ•˜๋‹ค. ๊ธฐ์กด ๋‚ด์—ฐ๊ธฐ๊ด€ ์ฐจ๋Ÿ‰์˜ ๊ฒฝ์šฐ, ์ถฉ๋ถ„ํ•œ ์—ฐ์†Œ์—ด๋Ÿ‰์„ ํ™œ์šฉํ•˜์—ฌ ๋‚œ๋ฐฉ ๋ฐ ๊น€์„œ๋ฆผ ๋ฐฉ์ง€๋ฅผ ์œ„ํ•ด ์‚ฌ์šฉํ•  ์ˆ˜ ์žˆ์—ˆ๋‹ค. ํ•˜์ง€๋งŒ ์ „๊ธฐ์ž๋™์ฐจ์˜ ๊ฒฝ์šฐ, ๋‚ด์—ฐ๊ธฐ๊ด€ ์ฐจ๋Ÿ‰๊ณผ ๋‹ฌ๋ฆฌ ์ถฉ๋ถ„ํ•œ ์—ด์›์ด ์กด์žฌํ•˜์ง€ ์•Š์„๋ฟ๋”๋Ÿฌ ํƒ‘์žฌ๋œ ๋ฐฐํ„ฐ๋ฆฌ์— ์ €์žฅ๋œ ์—๋„ˆ์ง€๋Ÿ‰์— ๋”ฐ๋ผ ์ฃผํ–‰๊ฑฐ๋ฆฌ๊ฐ€ ์˜์กด์ ์ด๋ฏ€๋กœ, ๊ณต์กฐ์‹œ์Šคํ…œ์„ ์šด์ „ํ• ์ˆ˜๋ก ์ „๊ธฐ์ž๋™์ฐจ์˜ ์ฃผํ–‰๊ฑฐ๋ฆฌ๊ฐ€ ๊ธ‰๊ฐํ•˜๋Š” ๋ฌธ์ œ๊ฐ€ ์กด์žฌํ•œ๋‹ค. ์ด๋ฅผ ํ•ด๊ฒฐํ•˜๊ธฐ ์œ„ํ•ด์„œ๋Š” ๊ณต์กฐ์‹œ์Šคํ…œ์˜ ์—๋„ˆ์ง€ ์‚ฌ์šฉ๋Ÿ‰์„ ์ค„์ด๊ณ  ํšจ์œจ์„ ๋†’์—ฌ์•ผ ํ•œ๋‹ค. ๊ธฐ์กด ์ฐจ๋Ÿ‰์—์„œ๋Š” ๊น€์„œ๋ฆผ ์ œ๊ฑฐ๋ฅผ ์œ„ํ•˜์—ฌ, ์‹ค๋‚ด๊ณต๊ธฐ๋ฅผ ์ด์Šฌ์ ๋ณด๋‹ค ๋‚ฎ๊ฒŒ ๋งŒ๋“ค์–ด ๊ณต๊ธฐ๋‚ด ์ˆ˜๋ถ„์ด ์—ด๊ตํ™˜๊ธฐ์— ์‘์ถ•์‹œ์ผœ ์ œ์Šตํ•œ ํ›„ ์žฌ๊ฐ€์—ดํ•˜์—ฌ ์‹ค๋‚ด๋กœ ๊ณต๊ธ‰ํ•˜๋Š” ๋ฐฉ๋ฒ•์„ ๋ณดํŽธ์ ์œผ๋กœ ์‚ฌ์šฉํ•˜๊ณ  ์žˆ๋‹ค. ์ด๋Š” ๋ถˆํ•ฉ๋ฆฌ์ ์ธ ์—๋„ˆ์ง€ ์†Œ๋น„๋ฅผ ์•ผ๊ธฐํ•œ๋‹ค. ์ด๋Ÿฌํ•œ ๋ฌธ์ œ๋ฅผ ํ•ด๊ฒฐํ•˜๊ธฐ ์œ„ํ•ด, ๊ณ ์ฒด ์ œ์Šต์ œ๋ฅผ ํ™œ์šฉํ•˜์—ฌ ๊ณต๊ธฐ๋‚ด ์ˆ˜๋ถ„์„ ์ง์ ‘ ํก์ฐฉ์‹œ์ผœ ์ œ์Šตํ•˜๋Š” ๋ฐฉ์•ˆ์„ ๊ณ ์•ˆํ•˜์˜€๋‹ค. ๋˜ํ•œ, ๋ชจํ„ฐ ๋ฐ ์ธ๋ฒ„ํ„ฐ์™€ ๊ฐ™์€ ์ „์žฅํ’ˆ๋“ค์˜ ํ์—ด์„ ํšŒ์ˆ˜ํ•˜์—ฌ ๊ณต์กฐ์— ํ™œ์šฉํ•˜๊ธฐ ์œ„ํ•ด ์ถ”๊ฐ€ ์—ด๊ตํ™˜๊ธฐ๋ฅผ ๊ณ ๋ คํ•˜์˜€๋‹ค. ๋ณธ ์—ฐ๊ตฌ์—์„œ, ์ œ์Šต์ œ ์ฝ”ํŒ… ์—ด๊ตํ™˜๊ธฐ (DCHE, Desiccant coated heat exchanger)๋ฅผ ์ œ์•ˆํ•˜๊ณ , ํ•ด๋‹น ์—ด๊ตํ™˜๊ธฐ๋ฅผ ์ ์šฉํ•œ ์ „๊ธฐ์ž๋™์ฐจ์šฉ ํžˆํŠธํŽŒํ”„ ์‹œ์Šคํ…œ์˜ ์—๋„ˆ์ง€ ์‚ฌ์šฉ๋Ÿ‰์— ๋Œ€ํ•œ ๋ถ„์„์„ ์‹ค์‹œํ•˜์˜€๋‹ค. ์ด๋ฅผ ์œ„ํ•˜์—ฌ, ์ฐจ๋Ÿ‰์‹ค๋‚ด ์—ด์  ๋ชจ๋ธ, ์ œ์Šต์ œ ์ฝ”ํŒ… ์—ด๊ตํ™˜๊ธฐ ๋ชจ๋ธ, ๊ทธ๋ฆฌ๊ณ  ์ฐจ๋Ÿ‰์šฉ ํžˆํŠธํŽŒํ”„ ๋ชจ๋ธ์„ ๊ตฌ์ถ• ๋ฐ ๊ฒ€์ฆํ•˜์˜€๋‹ค. ํƒ‘์Šน์ž์˜ ํ˜ธํก ๋ฐ ํ”ผ๋ถ€์—์„œ ์ฆ๋ฐœํ•˜๋Š” ์ˆ˜๋ถ„๋Ÿ‰์„ ๊ณ„์‚ฐํ•˜์—ฌ ์ฐจ๋Ÿ‰์‹ค๋‚ด ์—ด์  ๋ชจ๋ธ์„ ๊ตฌ์ถ•ํ•˜๊ณ , ๋‹ค๋ฅธ ์—ฐ๊ตฌ์ง„์˜ ๋ชจ๋ธ๊ณผ ๋น„๊ต ๊ฒ€์ฆํ•˜์˜€๋‹ค. ์ œ์Šต์ œ ์ฝ”ํŒ… ์—ด๊ตํ™˜๊ธฐ์˜ ํ•ด์„ ๋ชจ๋ธ์„ ์—ด ๋ฐ ๋ฌผ์งˆ ์ €ํ•ญ ๋ชจ๋ธ์„ ํ™œ์šฉํ•˜์—ฌ ์ฐจ๋ถ„ํ™”ํ•˜์—ฌ ๊ตฌ์ถ•ํ•˜์˜€๋‹ค. ์ด ํ•ด์„ ๋ชจ๋ธ์„ ๊ฒ€์ฆํ•˜๊ธฐ ์œ„ํ•˜์—ฌ, ๋‹ค์–‘ํ•œ ์กฐ๊ฑด์—์„œ DCHE์˜ ํก์ฐฉ ์„ฑ๋Šฅ์ธก์ •์„ ์‹คํ—˜ํ•˜์—ฌ ๊ทธ ๊ฒฐ๊ณผ๋ฅผ ์˜ˆ์ธก ์„ฑ๋Šฅ๊ณผ ๋น„๊ตํ•˜์˜€๋‹ค. ์ œ์Šต์ œ ์ฝ”ํŒ… ์—ด๊ตํ™˜๊ธฐ๋Š” ํก์ฐฉ์ œ์™€ ์ ‘์ฐฉ์ œ์˜ ๋น„์œจ์— ๋”ฐ๋ฅธ ํก์ฐฉ์„ฑ๋Šฅ์„ ๋ถ„์„ํ•œ ๊ฒฐ๊ณผ๋ฅผ ๋ฐ”ํƒ•์œผ๋กœ ์ œ์ž‘ํ•˜์˜€๋‹ค. ์ฐจ๋Ÿ‰์šฉ ํžˆํŠธํŽŒํ”„ ์‹คํ—˜์žฅ๋น„๋ฅผ ๊ตฌ์ถ•ํ•˜๊ณ  ๋‹ค์–‘ํ•œ ์กฐ๊ฑด์—์„œ ์‹คํ—˜ํ•˜์˜€์œผ๋ฉฐ, ๊ทธ ๊ฒฐ๊ณผ๋ฅผ ์ฐจ๋Ÿ‰์šฉ ํžˆํŠธํŽŒํ”„ ํ•ด์„ ๋ชจ๋ธ์˜ ์˜ˆ์ธก ์„ฑ๋Šฅ๊ฐ’๊ณผ ๋น„๊ตํ•˜์—ฌ ๊ฒ€์ฆํ•˜์˜€๋‹ค. ๋”ฐ๋ผ์„œ, ๊ฐœ๋ฐœ ๋ฐ ๊ฒ€์ฆ๋œ ๋ชจ๋ธ์„ Simulink์— ํ™œ์šฉํ•˜์—ฌ ๋‹ค์–‘ํ•œ ์šด์ „์กฐ๊ฑด์— ๋Œ€ํ•œ ์‹œ์Šคํ…œ์˜ ์†Œ๋น„๋™๋ ฅ์— ๋ฏธ์น˜๋Š” ์˜ํ–ฅ์„ ๋ถ„์„ํ•˜์˜€๋‹ค. ๊ทธ ๊ฒฐ๊ณผ, ๊ธฐ์กด ์ „๊ธฐ์ž๋™์ฐจ์— ๋น„ํ•˜์—ฌ ์ œ์Šต์ œ ์ฝ”ํŒ… ์—ด๊ตํ™˜๊ธฐ๋ฅผ ์ ์šฉํ•  ๊ฒฝ์šฐ, ์ฐจ๋Ÿ‰์šฉ ํžˆํŠธํŽŒํ”„์˜ ๋ƒ‰๋งค์••์ถ•๊ธฐ ์†Œ๋น„๋™๋ ฅ์ด ์ค„์–ด๋“ ๋‹ค๋Š” ๊ฒฐ๋ก ์„ ์–ป์—ˆ๋‹ค. ๋ณธ ์—ฐ๊ตฌ์—์„œ ์ œ์‹œํ•œ ์ œ์Šต์ œ ์ฝ”ํŒ… ์—ด๊ตํ™˜๊ธฐ๋ฅผ ์ „๊ธฐ์ž๋™์ฐจ์— ์ ์šฉํ•œ๋‹ค๋ฉด, ์ „๊ธฐ์ž๋™์ฐจ์šฉ ๊ณต์กฐ์‹œ์Šคํ…œ์ด ์‚ฌ์šฉํ•˜๋Š” ์—๋„ˆ์ง€๋ฅผ ์ค„์ž„์œผ๋กœ์จ, ๊ฒจ์šธ์ฒ  ์ฐจ๋Ÿ‰์˜ ์ฃผํ–‰๊ฑฐ๋ฆฌ๋ฅผ ํ™•๋ณดํ•  ์ˆ˜ ์žˆ์„ ๋ฟ๋งŒ ์•„๋‹ˆ๋ผ ๋ฏธ๋ž˜ ์ „๊ธฐ์ž๋™์ฐจ์˜ ๋ณด๊ธ‰ ๋ฐ ํ™•์‚ฐ์—๋„ ๊ธฐ์—ฌํ•  ์ˆ˜ ์žˆ์„ ๊ฒƒ์œผ๋กœ ๊ธฐ๋Œ€ํ•œ๋‹ค.Chapter 1. Introduction 1 1.1. The motivation of the study 1 1.2. Literature survey 11 1.2.1. Desiccant coated heat exchanger 11 1.3. Objectives and scopes 16 Chapter 2. Electric vehicle thermal loads analysis 19 2.1. Introduction of the cabin model 19 2.2. Numerical model of the cabin thermal load 20 2.3. Numerical model of the wet air 27 2.4. Validation of the cabin model 32 2.5. Sensitivity analysis of the cabin model 36 2.5.1. Ambient temperature and the number of passengers 38 2.5.2. Vehicle velocity profile 40 2.6. Summary 44 Chapter 3. Design and performance analysis of the desiccant coated heat exchanger 45 3.1. Introduction of the DCHE 45 3.1.1. Principle of the adsorption 46 3.1.2. Selection of the solid desiccant and the binder 49 3.2. Physical properties of the adsorbent 55 3.2.1. The surface area of the adsorbent 55 3.2.2. The image analysis using the scanning electron microscope 64 3.2.3. The vapor sorption capacity of the adsorbent 71 3.3. Numerical analysis of the DCHE 78 3.4. Experimental of the DCHE 87 3.4.1. Experiment set-up of the desiccant coated heat exchanger 87 3.4.3. Experimental validation of the DCHE model 96 3.5. Alternate control methods for DCHE 98 3.5.1. Absolute humidity gap method 98 3.5.2. Absolute humidity slope method 99 3.5.3. Water contents ratio method 101 3.5.4. Integrated area ratio method 103 3.6. Summary 105 Chapter 4. Design and performance analysis of the heat pump 107 4.1. Introduction of the automobile heat pump 107 4.1.1. Selection of the refrigerant 107 4.1.2. Selection of the lubricant 115 4.2. Numerical analysis of the automobile heat pump 117 4.2.1. Calculation method and assumption 117 4.2.2. Compressor 119 4.2.3. Heat exchangers 120 4.2.4. Expansion device 126 4.3. Experiment of the automobile heat pump 126 4.3.1. Experimental apparatus 127 4.3.2. Data reduction and uncertainty analysis 136 4.3.3. The optimum charge amounts 139 4.3.4. Performance of the heat pump system 143 4.3.5. Validation of the heat pump model 148 4.4. Summary 153 Chapter 5. Integrated System Simulation 155 5.1. Introduction 155 5.2. Simulation conditions 163 5.3. Simulation results 164 5.3.1. Effect of the additional heat exchanger 164 5.3.2. Effect of the DCHE frontal area 168 5.3.3. Effect of the fresh-recirculation air ratio 171 5.3.4. Effect of the ambient temperature 175 5.3.5. Effect of the DCHE inlet coolant temperature 180 5.3.6. Effect of the number of the passenger 184 5.3.7. Effect of the refrigerant type 187 5.3.8. Effect of the number of the DCHE 192 5.4. Summary 196 Chapter 6. Conclusions 199 References 203 ๊ตญ ๋ฌธ ์ดˆ ๋ก 222๋ฐ•

    Solar Cooling Technologies

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    This chapter describes different available technologies to provide the cooling effect by utilizing solar energy for both thermal and photovoltaic ways. Moreover, this chapter highlights the following points: (i) the main attributes for different solar cooling technologies to recognize the main advantages, challenges, disadvantages, and feasibility analysis; (ii) the need for further research to reduce solar cooling chiller manufacture costs and improve its performance; (iii) it provides useful information for decision-makers to select the proper solar cooling technology for specific application. Furthermore, some references, which include investigation results, will be included. A conclusion about the main gained investigation results will summarize the investigation results and the perspectives of such technologies

    Experimental Investigation on the Operation Performance of a Liquid Desiccant Air-conditioning System

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    A large share of energy consumption is taken by an air-conditioning system. It worsens the electricity load of the power network. Therefore, more and more scholars are paying attention to research on new types of air-conditioning systems that are energy- saving and environment-friendly. A liquid desiccant air conditioning system is among them, as it has a tremendous ability for power storage and low requirements for heat resources. Heat with low temperatures, such as excess heat, waste heat, and solar power, is suitable for the liquid desiccant air-conditioning system. The feasibility and economical efficiency of the system are studied in this experimental research. The result shows that when the temperature of the regeneration is about 80?, the thermodynamic coefficient of the system is about 0.6, and the supply air temperature of the air-conditioning system remains stable at 21?, the air-conditioning system can meet human comfort levels

    Study on Desiccant and Evaporative Cooling Systems for Livestock Thermal Comfort: Theory and Experiments

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    The present study considers evaporative cooling and desiccant unit-based air-conditioning (AC) options for livestock AC application. In this regard, proposed systems are investigated by means of experiments and thermodynamic investigations. Air-conditioning requirements for animals are theoretically investigated and temperature-humidity index (THI) is estimated. A lab-scale heat mass exchanger based on the Maisotsenko-cycle evaporative cooling conception (MEC) is set up and its performance is evaluated at different ambient air conditions. In addition, a desiccant-based air-conditioning (DAC) unit is thermodynamically evaluated using a steady-state model available in the literature. The study focuses on the ambient conditions of Multan which is the 5th largest city of Pakistan and is assumed to be a typical hot city of southern Punjab. The study proposed three kinds of AC combination i.e., (i) stand-alone MEC, (ii) stand-alone desiccant AC, and (iii) M-cycle based desiccant AC systems. Wet bulb effectiveness of the stand-alone MEC unit resulted in being from 64% to 78% whereas the coefficient of performance for stand-alone desiccant AC and M-cycle based desiccant AC system was found to be 0.51 and 0.62, respectively. Results showed that the stand-alone MEC and M-cycle based desiccant AC systems can achieve the animalsโ€™ thermal comfort for the months of March to June and March to September, respectively, whereas, stand-alone desiccant AC is not found to be feasible in any month. In addition, the ambient situations of winter months (October to February) are already within the range of animal thermal comfort

    Assessment of a desiccant cooling system in a traditional and innovative nanofluid HVAC system

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    The topic of energy saving is a constant in everyday life, and it is widespread all over the world. Space heating using solar panels is the most used renewable source of energy, but the application of solar energy for cooling the fluids used for refrigeration is growing very fast. Among the techniques used for refrigeration, this work focused on Desiccant Cooling. In particular, with the use of dynamic simulation software, it was possible to study the heat supplied and the energy consumption of a Heating Ventilation Air Conditioning (HVAC) system of a university building and to compare consumption with those of a Desiccant Cooling system applied to the same building. Four different cases were simulated: two related to the HVAC system, one of which operates with water and glycol and the other one with nanofluid, and the other ones to the Desiccant Cooling system with both types of fluids mentioned above. Keeping the same energy demand of the building in all the simulations, it was found that in summer the Desiccant Cooling system had higher performance than the traditional HVAC system and that the use of the nanofluid in both types of conditioning systems further increased the performance of 21%. Simulations were carried out using TRNSYS software
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