Performance of hybrid vaccine freezer that combined thermoelectric coolers with vapor compression refrigeration: Experimental assessment

In the medical field, refrigeration systems are used to store and transport vaccines, blood, and other medical supplies that require specific temperature ranges to remain effective. As technology continues to advance, the demand for more efficient and sustainable refrigeration systems is also increasing. The freezer compartment is typically designed to maintain a temperature of −18°C to −23°C for storing frozen items. Consequently, this work aims to develop a hybrid refrigeration system that combines a thermoelectric cooler system (TEC) and a vapor compression refrigeration cycle (VCC) system to achieve lower temperatures than conventional refrigerators. Also, the performance of the proposed hybrid refrigeration system is experimentally assessed with various operating conditions, including varying the voltage delivered to the system. The experimental results exhibited that the temperature inside the freezer room reached −33°C, while the cold side temperature is −47°C. Also, the maximum coefficient of performance of the VCC system, TEC, and hybrid system is 2.07, 1.06, and 0.37, respectively, at a DC voltage applied of 6 V. Moreover, the results revealed that the hybrid system combining a TEC and a VCC system can be a valuable technology for specific applications with low temperatures and limited capacity requirements.     

Analysis of mechanical vapour compression desalination process

Characteristics of the single‐effect mechanical vapour‐compression (MVC) are analysed as a function of the system design and operating parameters. The analysis focuses on prediction of the specific power consumption for the vapour compressor and the specific heat transfer areas for the evaporator/condenser unit and the plate‐type feed preheaters. The mathematical model includes material and energy balance equations as well as a set of correlations for evaluation of the thermophysical properties and the heat transfer coefficients. The correlations are dependent on the transport properties of the flowing streams, i.e. temperature, concentration, and velocity. In addition, the model considers the effects of the boiling point elevation and the pressure losses in the demister. Results show decrease in the specific power consumption and the specific heat transfer area of the evaporator/condenser at higher top brine temperatures. On the other hand, the specific power consumption decreases at low‐temperature differences between the boiling brine and steam condensate, while the specific heat transfer area increases. Model predictions are found consistent with the available industrial data. Finally, comparison of the performance of the MVC system and the single‐effect thermal vapour compression (TVC) is made as a function of design and operating parameters. Although, the results show comparable performance, choice between the two systems should take into consideration other operational parameters. Copyright © 1999 John Wiley & Sons, Ltd.     

Comparative performance of HFC134a- and HCFC22-based vapour absorption refrigeration systems

A comparative thermodynamic study of the vapour absorption refrigeration systems (VARS) working with HFC134a and HCFC22 is presented. Due to its superior performance in HCFC22-based VARS, dimethyl acetamide is chosen as the solvent for both the refrigerants. It is observed that the HCFC22-based system yields significantly better COP than the HFC134a system. However, since the latter operates at lower pressures, the possibility exists to improve its COP by resorting to two-stage operation. © 1998 John Wiley & Sons, Ltd.     

Optimization of multistage vapour compression systems using genetic algorithms. Part 1: Vapour compression system model

The vapour compression cycle is the most common type of refrigeration cycle in use today. Most vapour compression systems are simple, having only four major components: a compressor, a condenser, an expansion device and an evaporator. Multistage vapour compression systems are more complex with, for example, extra compressors, aftercoolers, intercoolers, flash tanks and liquid‐to‐suction heat exchangers. The study performed here considers 121 different configurations operating at condensing and evaporating temperatures that range from ?50 to 50°C. The refrigerants used are ammonia, R‐22, R‐134a, R‐152a and R‐123. The basis of comparison for the systems is multistage effectiveness. Multistage effectiveness is a novel term defined as the ratio of the coefficient of performance of a multistage system to the collective coefficient of performance of an equivalent group of basic single‐stage systems operating at the same cooling capacities and evaporating and condensing temperatures. Equivalency here is defined on the basis of achieving the same cooling capacity at their respective temperatures as dictated by the multistage systems. The vapour compression system model presented here was put through genetic optimization with interesting results. Copyright © 2001 John Wiley & Sons, Ltd.     

Life cycle cost analysis of energy efficiency design options for refrigerators in Brazil

The purpose of this paper was to present the results of a life cycle cost analysis concerning the purchase and operation of a more efficient popular refrigerator model compared with a baseline design in Brazil. The summarized results may be useful for organizations working to promote sustainable energy development. This paper specifically focuses on refrigerators, since their energy consumption is predicted to constitute over 30% of the total average domestic electricity bill in Brazilian households. If all new Brazilian refrigerators had an energy efficiency at the level consistent with the least life cycle cost of ownership, it would result in an annual savings of 2.8 billion dollars (US$) in electricity bills, 45 TWh of electricity demand, and 18 Mt of CO₂ emissions, with a respective payback period of 7 years which is less than half the average estimated lifetime of a refrigerator. The analysis was conducted following the guidelines of similar analyses available from the US Department of Energy and the Collaborative Labeling and Appliance Standards Program.

Optimization of multistage vapour compression systems using genetic algorithms. Part 2: Application of genetic algorithm and results

Genetic algorithms involve the coding of a solution into a binary string in the same manner that DNA is a biological coding. A population of binary strings are randomly created, evaluated, allowed to mate and are mutated to form a new generation of strings. There is a mating preference given to those strings which rate the highest to simulate the survival‐of‐the‐fittest theory that exists in nature. This process of evaluation, mating and mutation is repeated until some termination criteria are met. A computer code was written in Visual C++ to simulate the vapour compression systems and perpetuate the genetic algorithm. The genetic algorithm functioned adequately enough to provide general trends but it did not find a universal optimum. After numerous runs, the code produced data that suggest that systems which employ intercooler/flash tanks and operate at lower evaporating temperatures have a higher multistage effectiveness. Copyright © 2001 John Wiley & Sons, Ltd.     

Thermodynamic analysis of R422 series refrigerants as alternative refrigerants to HCFC22 in a vapour compression refrigeration system

In the present study, the first and second law analysis of R422 series refrigerants (R422A, R422B, R422C and R422D) is presented as an alternative to HCFC22. A computational model, developed in engineering equation solver software, is employed for comparing the performance of these refrigerants in vapour compression refrigeration cycle. The thermodynamic properties of the R422 series refrigerants are computed using Refprop version 7.0. The parameters computed are volumetric cooling capacity (VCC), compressor discharge temperature, coefficient of performance (COP), exergetic efficiency and efficiency defects in system components. The results indicate that VCC, COP and exergetic efficiency for HCFC22 are higher in comparison with R422A, R422B, R422C and R422D. The efficiency defects in the condenser are largest followed by throttle valve, compressor and evaporator. Thus, the design improvement of condenser is of utmost importance to reduce the overall irreversibility and improve the system performance. Copyright © 2009 John Wiley & Sons, Ltd.     

Performance analysis of a solar vapour thermal compression chiller

The influence of the design conditions on the coefficient of performance (COP) of a solar vapour thermal compression chiller was investigated from an operational point of view. Based on a well known model, a number of COP evaluation runs were conducted and the results are presented in graph form as a function of the main design parameters. Through these graphs the influence of the main operating parameters on the performance is quantitatively shown. Finally, the calculated COP is compared to that of a solar absorption system operating under similar conditions.     

Energy balance of solar absorption and vapour compression cooling systems

Solar absorption cooling systems are viewed as potential alternatives to fossil-fuel-based conventional cooling systems. This view is investigated in this paper from the point of view of the energy balance of solar absorption and conventional systems. The paper investigates the primary energy needs of three cooling systems; dry and wet cooled vapour compression systems and wet cooled solar absorption. The sources of energy demand in the three systems are identified and their primary energy needs determined. The paper, then, investigates the conditions under which the energy inputs to the solar system breaks even with the other two systems. The investigation is conducted with particular reference to the operational and environmental conditions in Kuwait.     

Methodological reviews and analyses on the emerging research trends and progresses of thermoelectric generators

Thermoelectric generator is among the earliest initiated electricity‐harvesting methods. It is a very potential power harvester that can convert wasteful thermal energy into electricity. However, it often suffers from low energy conversion rate due to its inconsistent heat source, inefficient thermoelectric material (or thermoelement) performance, and incompetent structural issues. Progressively for the first time, detailed methodological surveys and analyses are made for bulk, thick, and thin films in this review. This is in order to accommodate better insights and comprehensions on the emerging trends and progresses of thermoelectric generators from 1989 to 2017. The research interests in thermoelectric generators have started back in 1989, and have continuously experienced emerging progresses in the number of studies over the last years. The methodological reviews and analyses of thermoelectric generator showed that almost 46.6% of bulk and 46.1% of thick and thin film research works, respectively, are actively progressed in 2014 to 2017. Nearly 86.2% of bulk and 44.1% of thick and thin film thermoelectric generators are realizing in between 0.001 and 4 μW cm^?2 K^?2, while 43.1% of thick and thin films are earning among 10^?6 to 0.001 μW cm^?2 K^?2. The highest achievement made until now is 2.5 W cm^?2 at a temperature difference of 140 K and thermoelectric efficiency factor of 127.55 μW cm^?2 K^?2. This achievement remarked positive elevation for the field and interest in thermoelectric power generation. Consecutively, the research trends of fundamental devices' structure, thermoelement, fabrication, substrate, and heat source characteristics are analyzed too, along with the desired improvement highlights for the applications of thermoelectric generators.     

Cooling performance and energy saving of a compression–absorption refrigeration system driven by a gas engine

The prototype of combined vapour compression–absorption refrigeration system was set up, where a gas engine drove directly an open screw compressor in a vapour compression refrigeration chiller and waste heat from the gas engine was used to operate absorption refrigeration cycle. The experimental procedure and results showed that the combined refrigeration system was feasible. The cooling capacity of the prototype reached about 589 kW at the Chinese rated conditions of air conditioning (the inlet and outlet temperatures of chilled water are 12 and 7°C, the inlet and outlet temperatures of cooling water are 30 and 35°C, respectively). Primary energy rate (PER) and comparative primary energy saving were used to evaluate energy utilization efficiency of the combined refrigeration system. The calculated results showed that the PER of the prototype was about 1.81 and the prototype saved more than 25% of primary energy compared to a conventional electrically driven vapour compression refrigeration unit. Error analysis showed that the total error of the combined cooling system measurement was about 4.2% in this work. Copyright © 2006 John Wiley & Sons, Ltd.     

An experimental investigation on electrical performance and characterization of thermoelectric generator

Thermoelectric generator (TEG) is an attractive renewable energy source that utilizes waste heat energy from various sources to produce electricity. In this paper, a novel method has been proposed to investigate and characterize the TEG module by determining the exact maximum power point (MPP) and estimate the TEG module dynamic parameters. A DC-DC boost converter with a simple control method is proposed to obtain I-V and I-P characteristics and extract the exact MPP of the TEG module. The electrical performance and dynamic parameters such as Seebeck coefficient and internal resistance of the TEG module have been estimated at the MPP. MATLAB software package is used to model and simulate the complete system. Then, by using a low-cost Arduino microcontroller and a standard TEG module (HZ-14HV), a test rig is built to examine the electrical performance of the TEG. A comparison among simulation, experimental, and manufacturing data sheet is done to validate the accuracy of the proposed system. The proposed system tests and characterizes a TEG module at five values of temperature differences in the range from 377 K to 457 K and analyses the MPP generated in the range from 5 to 13.8 W . The obtained results confirm that there is good agreement among the simulation, experimental, and data sheet. To the best of our knowledge, it is the first time to use the boost converter to estimate the electrical characteristics and the dynamic parameters of the TEG. It can be said that the proposed DC-DC boost converter with the suggested control method is helpful for testing commercial TEG modules before implementing in a TEG system.     

An assessment of the feasibility of solar absorption and vapor compression cooling systems

For absorption cooling systems to operate and produce their cooling effects they need both thermal and electrical energy, while vapor compression systems need electrical energy only. When operating on solar energy the absorption system may receive all its thermal energy needs from solar sources while its electrical needs (parasitic power) are to be supplied from conventional sources. In order to conduct a fair comparison between the two cooling systems, it is proposed to supply both systems with equal amounts of conventional power and to supplement the rest of their needs from solar sources. A solar coefficient of performance, defined as the ratio of the refrigeration effect to the solar radiation input, is introduced and used for comparing some parameters of engineering ane economic importance in both systems. Economic analysis of solar cooling systems indicates that their initial cost is a function of both their design capacities and the number of hours of full load operation required to fulfill the total daily cooling demand. It indicates, also, that the initial cost of both solar cooling systems would break even before the cost of their respective solar conversion devices do.     

Economical comparison between a solar-powered vapour absorption air-conditioning system and a vapour compression system in the Middle East

This paper presents an analysis of the general cost associated with single- and double-effect vapour absorption and vapour compression air-conditioning systems. The cost analysis covers the initial costs and the operating costs of each of the three systems. The vapour absorption system considered in this paper is based on water as the refrigerant and lithium bromide solution as the absorbent. The analysis is undertaken to help select an air-conditioning system that fulfils a 250 TOR cooling load of a five-floor student hospital in Alexandria, Egypt. The typical meteorological year database for Alexandria was used to estimate the cooling load for the building. The analysis is based on two different methods, the present worth value (PWC) and the equivalent annual cost (EAC), for initial and operating costs of each system. The selection depends on which system requires the minimum life-cycle cost (LCC) and can perform the intended function for its life span. The analysis also considers the interrelationship between economic and thermodynamic aspects, such as the dependence of operating cost on the surrounding climatic conditions. The method used and the results from this study offer useful guidelines for researchers and decision-makers when selecting an air-conditioning system. The results show that the double-effect vapour absorption system is the preferred option for its minimum present worth value as well as the equivalent annual cost.     

Energy and exergy analyses of a two‐stage vapour compression refrigeration system

In this paper exergy analysis of two‐stage vapour compression refrigeration (VCR) system has been carried out with an objective to evaluate optimum inter‐stage temperature (pressure) for refrigerants HCFC22, R410A and R717. A thermodynamic model based on the principles of mass, energy and exergy balances is developed for this purpose. The computed results illustrate the effects of evaporation and condensation temperatures, isentropic efficiencies of compressors, sub‐cooling of refrigerant and superheating of suction vapour on optimum inter‐stage saturation temperature (pressure). The optimum inter‐stage saturation temperatures (pressures) for HCFC22 and R410A are proximate to arithmetic mean of evaporation and condensation temperatures (AMT) when assuming superheating of suction vapour and non‐isentropic compression processes in low‐pressure and high‐pressure compressors. The optimum inter‐stage saturation temperatures (pressures) for HCFC22 and R410A are near to geometric mean of evaporation and condensation temperatures (GMT) when it is assumed that cycle involves the effects of sub‐cooling, superheating of suction vapour and non‐isentropic compression of the suction vapour. The optimum inter‐stage saturation temperature (pressure) for R717 is close to GMT irrespective of sub‐cooling, superheating of suction vapour and non‐isentropic compression in the cycle. The efficiency defects, computed corresponding to optimum inter‐stage temperature in condenser is higher in comparison to the other components. Finally, it is deduced that R717 is a better alternative refrigerant to HCFC22 than R410A in two‐stage VCR system. Copyright © 2009 John Wiley & Sons, Ltd.     

A thermoelectric generator and water-cooling assisted high conversion efficiency polycrystalline silicon photovoltaic system

Solar energy has been increasing its share in the global energy structure. However, the thermal radiation brought by sunlight will attenuate the efficiency of solar cells. To reduce the temperature of the photovoltaic (PV) cell and improve the utilization efficiency of solar energy, a hybrid system composed of the PV cell, a thermoelectric generator (TEG), and a water-cooled plate (WCP) was manufactured. The WCP cannot only cool the PV cell, but also effectively generate additional electric energy with the TEG using the waste heat of the PV cell. The changes in the efficiency and power density of the hybrid system were obtained by real time monitoring. The thermal and electrical tests were performed at different irradiations and the same experiment temperature of 22°C. At a light intensity of 1000 W/m², the steady-state temperature of the PV cell decreases from 86.8°C to 54.1°C, and the overall efficiency increases from 15.6% to 21.1%. At a light intensity of 800 W/m², the steady-state temperature of the PV cell decreases from 70°C to 45.8°C, and the overall efficiency increases from 9.28% to 12.59%. At a light intensity of 400 W/m², the steady-state temperature of the PV cell decreases from 38.5°C to 31.5°C, and the overall efficiency is approximately 3.8%, basically remain unchanged.     

Effects of different temperature levels at generator and evaporator on the performance of vapour absorption heat transformers

In a vapour absorption heat transformer, heat is input at both the evaporator and the generator, and useful heat is delivered at the highest temperature at the absorber. Based on an earlier thermodynamic analysis by the authors, the effects of heat supply at different temperature levels to the evaporator and generator are studied here. It is observed that, when two heat sources at different temperature levels are interchanged between the evaporator and generator, there is no noticeable change in the system performance. However, for design and operational reasons, it is recommended that the higher temperature heat source be input at the generator.     

Development of a hybrid refrigerator combining thermoelectric and vapor compression technologies

A domestic refrigerator with three compartments has been developed: refrigerator compartment, at 4 °C (vapor compression cooling system); freezer compartment, at −22 °C (vapor compression cooling system); and a new super-conservation compartment, at 0 °C (thermoelectric cooling system). The thermoelectric system designed for the super-conservation compartment eliminates the oscillation of its temperature due to the start and stop compressor cycles, obtaining a constant temperature and thus, a better preservation of the food.For the design and optimization of this application, a computational model, based in the numerical method of finite differences, has been developed. This model allows to simulate the complete hybrid refrigerator (vapor compression–thermoelectricity). The accuracy of the model has been experimentally checked, with a maximum error of 1.2 °C for temperature values, and 8% for electric power consumption.By simulations with the computational model, the design of the refrigerator has been optimized, obtaining a final prototype highly competitive, by the features on food preservation and power consumption: 1.15 kW h per day (48.1 W) for an ambient temperature of 25 °C. According to European rules, this power consumption value means that this new refrigerator could be included on energy efficiency class B.     

Comparative analysis of nanofluid‐based Organic Rankine Cycle through thermoeconomic optimization

The present work focused on the comparative analysis of organic Rankine cycle (ORC) operated with nanoparticles. The effect of CuO and Al₂O ₃ nanoparticles synthesized with water and circulated within heat exchangers are examined. Thermal efficiency and levelized energy cost (LEC) of the nanofluid based ORC are evaluated simultaneously in the present work. The optimization problem of ORC is formed and solved using heat transfer search algorithm. Operating parameters of the nanofluid based ORC such as pinch point temperature difference of heat exchangers, evaporation pressure, the mass flow rate of refrigerant, and concentration of nanoparticles are investigated in the optimization study. Further, the effect of turbine ratio, heat source temperature, and mass flow rate of heat source fluid on CuO and Al ₂O ₃ based ORC is explored and discussed. It was observed that a total variation of 35.2% was obtained at the cost of 3.5% variation in LEC between extreme design points. The maximum thermal efficiency of 19.3% and 19.32% can be obtained with CuO and Al ₂O ₃ with 2.616 and 2.62 $/kWh, respectively. Comparative results reveal that CuO based ORC shows dominance in terms of economic performance over Al ₂O ₃ based ORC for any given value of the thermal efficiency.     

A comparative study of the performance characteristics of double‐effect absorption refrigeration systems

Three classes of double‐effect lithium bromide–water absorption refrigeration systems (series, parallel and reverse parallel) with identical refrigeration capacities are studied and compared thermodynamically. In order to simulate the performances of the systems, a new set of computationally efficient formulations is used for thermodynamic properties of Li‐Br solutions at equilibrium. The simulation results are used to examine the influence of various operating parameters on the first and second law performance characteristics of the systems. In addition, the dependences are investigated of system performance on the effectivenesses of the solution heat exchangers, the pressure drops between the evaporator and the absorber and between the low‐pressure generator and the condenser, and the low‐grade heat externally supplied to the low‐pressure generator. The results reveal the advantages and disadvantages of different configurations of double‐effect lithium bromide–water absorption refrigeration systems, and are expected to be useful in the design and control of such systems. Copyright © 2010 John Wiley & Sons, Ltd.