18th International Congress of Mechanical Engineering



Similar documents
We will study the temperature-pressure diagram of nitrogen, in particular the triple point.

Thermal diffusivity and conductivity - an introduction to theory and practice

BB-18 Black Body High Vacuum System Technical Description

Testing methods applicable to refrigeration components and systems

Experimental Evaluation Of The Frost Formation

Determination of Thermal Conductivity of Coarse and Fine Sand Soils

Heat. Investigating the function of the expansion valve of the heat pump. LD Physics Leaflets P Thermodynamic cycle Heat pump

International Journal of Latest Research in Science and Technology Volume 4, Issue 2: Page No , March-April 2015

FXA Candidates should be able to : Define and apply the concept of specific heat capacity. Select and apply the equation : E = mcδθ

HVAC: Cool Thermal Storage

HEAT TRANSFER ENHANCEMENT ON DOUBLE PIPE HEAT EXCHANGER BY WIRE COILED AND TAPER WIRE COILED TURBULATOR INSERTS

Thermocline Management of Stratified Tanks for Heat Storage

Lecture: 33. Solidification of Weld Metal

Check-list for auditors. Audit visit at candidate registered laboratories

Integration of a fin experiment into the undergraduate heat transfer laboratory

Heat and cold storage with PCM

Theoretical and Experimental Investigation of Heat Transfer Characteristics through a Rectangular Microchannel Heat Sink

Physical Properties of a Pure Substance, Water

Experimental Study on Super-heated Steam Drying of Lignite

To measure the solubility of a salt in water over a range of temperatures and to construct a graph representing the salt solubility.

Research on the Air Conditioning Water Heater System

Initial Experiments of a Novel Liquid Desiccant Dehumidifier for Industrial and Comfort Air Conditioning Systems

Pre-Lab Notebook Content: Your notebook should include the title, date, purpose, procedure; data tables.

Determination of the heat storage capacity of PCM and PCM objects as a function of temperature

FUNDAMENTALS OF ENGINEERING THERMODYNAMICS

Calculating Heat Loss by Mark Crombie, Chromalox

DETERMINATION OF THE HEAT STORAGE CAPACITY OF PCM AND PCM-OBJECTS AS A FUNCTION OF TEMPERATURE. E. Günther, S. Hiebler, H. Mehling

Performance Test of Solar Assisted Solid Desiccant Dryer

Dependency of heat transfer rate on the Brinkman number in microchannels

MIT Manufacturing Processes and Systems. Homework 6 Solutions. Casting. October 15, Figure 1: Casting defects

Chapter 3.4: HVAC & Refrigeration System

AN EXPERIMENTAL STUDY OF EXERGY IN A CORRUGATED PLATE HEAT EXCHANGER

Apr 17, 2000 LAB MANUAL

TABLE OF CONTENT

Rusty Walker, Corporate Trainer Hill PHOENIX

ENHANCED STEAM CONDENSATION AS A RESULT OF HEAT TRANSFER ADDITIVES

Apparatus error for each piece of equipment = 100 x margin of error quantity measured

We will try to get familiar with a heat pump, and try to determine its performance coefficient under different circumstances.

Heat Transfer and Energy

DESIGN OF AIR CONDITIONING SYSTEM IN AUTOMOBILE

Heat transfer characteristics in latent heat storage system using paraffin wax

Experimental Analysis of an Automotive Air Conditioning System With Two-Phase Flow Measurements

Effect of Magnesium Oxide Content on Final Slag Fluidity of Blast Furnace

Experimental Study of Free Convection Heat Transfer From Array Of Vertical Tubes At Different Inclinations

Waste Heat Recovery through Air Conditioning System

NUCLEAR ENERGY RESEARCH INITIATIVE

2. Room temperature: C. Kelvin. 2. Room temperature:

Solar Hot Water Heaters

EXPERMENTATIONAL DATA ANALYSIS OF CHIMNEY OPERATED SOLAR POWER PLANT

Grant Agreement No SFERA. Solar Facilities for the European Research Area SEVENTH FRAMEWORK PROGRAMME. Capacities Specific Programme

Vapor Pressure Measurement of Supercooled Water

AIR CONDITIONING TECHNOLOGY

THE PSEUDO SINGLE ROW RADIATOR DESIGN

POURING THE MOLTEN METAL

Refrigeration Basics 101. By: Eric Nelson

Review - After School Matter Name: Review - After School Matter Tuesday, April 29, 2008

Session 2: Hot Water Supply

RESULTS OF ICARUS 9 EXPERIMENTS RUN AT IMRA EUROPE

LIPE- Institut National des Sciences Appliquées Toulouse, France Contact:

ENERGY CARRIERS AND CONVERSION SYSTEMS Vol. II - Liquid Hydrogen Storage - Takuji Hanada, Kunihiro Takahashi

An Experimenatl Study on Heat Transfer Behaviors of A Welded - Aluminum Minichannel Heat Exchanger

5.2. Vaporizers - Types and Usage

Heat Transport Study of the Laminar Heat Pipe Heat Exchanger

P. A. Hilton Ltd REFRIGERATION & AIR CONDITIONING VAPOUR COMPRESSION HEAT PUMPS VENTILATION VOCATIONAL

INTERACTION OF LIQUID MOTION ON MOBILE TANK STRUCTURE

UNIVERSITY OF MINNESOTA DULUTH DEPARTMENT OF CHEMICAL ENGINEERING ChE CONVECTIVE HEAT TRANSFER

Fall 2004 Ali Shakouri

Review on Experimental Analysis and Performance Characteristic of Heat Transfer In Shell and Twisted Tube Heat Exchanger

Investigation into the energy consumption of a data center with a thermosyphon heat exchanger

CHAPTER 2 INJECTION MOULDING PROCESS

16. Heat Pipes in Electronics Cooling (2)

FEDSM Flow Boiling Heat Transfer Enhancement in Subcooled and Saturated Refrigerants in Minichannel Heat Sinks

TRITTICO ORIGINAL BY BRAVO A WHOLE WORKSHOP IN A SINGLE MACHINE

EVERYDAY ENGINEERING EXAMPLES FOR SIMPLE CONCEPTS

CFD SIMULATION OF SDHW STORAGE TANK WITH AND WITHOUT HEATER

ME Heat Transfer Laboratory. Experiment No. 7 ANALYSIS OF ENHANCED CONCENTRIC TUBE AND SHELL AND TUBE HEAT EXCHANGERS

HEAT TRANSFER ENHANCEMENT IN FIN AND TUBE HEAT EXCHANGER - A REVIEW

Precision Mass Flow Metering For CVD Applications.

Triple Point Experiment

Comparison of Spherical and Membrane Large LNG. Carriers in Terms of Cargo Handling

FINAL REPORT For Japan-Korea Joint Research Project AREA

CONVECTION CURRENTS AND ANOMALOUS BEHAVIOUR OF WATER

HEAT TRANSFER AUGMENTATION THROUGH DIFFERENT PASSIVE INTENSIFIER METHODS

International Telecommunication Union SERIES L: CONSTRUCTION, INSTALLATION AND PROTECTION OF TELECOMMUNICATION CABLES IN PUBLIC NETWORKS

/12/$ IEEE 1488

i1.. DOE/CE/ DEVELOPMENT OF ADVANCED LOW-TEMPERATURE HEAT TRANSFER FLUIDS FOR DISTRICT HEATING AND COOLING NO.

The Second Law of Thermodynamics

Experiment 3 Pipe Friction

Using Thermocouple Sensors Connecting Grounded and Floating Thermocouples

Experimental study on frost growth and dynamic performance of air source heat pump system

Thermal Energy Storage Strategies for Commercial HVAC Systems

Chapter 18 Temperature, Heat, and the First Law of Thermodynamics. Problems: 8, 11, 13, 17, 21, 27, 29, 37, 39, 41, 47, 51, 57

Experimental investigation of Heat Transfer Enhancement of Heat Pipe Using Silver/Water Nanofluid

Comparing Air Cooler Ratings Part 1: Not All Rating Methods are Created Equal

Overview of the state of the art heat measurement technologies for larger solar thermal systems

WJP, PHY381 (2015) Wabash Journal of Physics v4.3, p.1. Cloud Chamber. R.C. Dennis, Tuan Le, M.J. Madsen, and J. Brown

Specific Volume of Liquid (Column 7). The volume per unit of mass in cubic feet per pound.

Development of High-Speed High-Precision Cooling Plate

2. CHRONOLOGICAL REVIEW ABOUT THE CONVECTIVE HEAT TRANSFER COEFFICIENT

How To Calculate The Performance Of A Refrigerator And Heat Pump

Transcription:

CYLINDRICAL ENCAPSULATED COLD STORAGE Juan José Milón Guzmán Universidad Católica San Pablo, Av. Salaverry, 31, Vallecito, Cercado, Arequipa, Perú milonjj@ucsp.edu.pe Sergio leal Braga Pontificia Universidade Católica do Rio de Janeiro, Rua Marquês de São Vicente, 225, Gávea, 22453-9, Rio de Janeiro, RJ, Brasil slbraga@mec.puc-rio.br Abstract. An experimental apparatus was developed to investigate the thermal performance of a cold storage system utilizing water as Phase Change Material (PCM) encapsulated in cylinders. The coolant is a water-alcohol mixture (5% vol.), controlled by a constant temperature bath (CTB). Temperatures varying with time are measured inside and outside the capsule. Cylinder with internal diameter and thickness of 45 mm, 1.5 mm and length 17 mm, respectively, were made in acrylic, PVC (polyvinyl chloride), bronze and aluminium materials. Several situations were investigated for different temperatures and flow regimes. The temperature field, interface position and the heat transfer inside the cylinders were monitored. Keywords: refrigeration, air conditioning, thermal storage, phase change, supercooling. 1. Introducción The thermal storage for air-conditioning systems is an important concept of many energy conservation programs in industrial and commercial applications. Water is widely used as the phase-change material (PCM) for thermal storage because of its advantages such as high value in latent heat, stable chemical properties, low cost and easy acquisition, no environmental pollution concern, and compatibility with the materials used in air-conditioning equipment. However, there are a few disadvantages in using water as PCM. Two of the most serious problems encountered are the supercooling phenomenon and the density inversion occurring in the water solidification during the thermal storage cooling process. While a quantity of water is cooled in an enclosed container, freezing does not occur at its freezing point ( C). Instead, it is normally cooled below C before ice nucleation happens. Supercooled water refers to a state of metastable liquid even though the temperature of water is below its freezing temperature (Figure 1). The metastable state will end when ice nucleation occurs and the thin plate-like crystal of dendritic ice grows into the supercooled region of water. During the dendritic ice growth process, latent heat released from the dendritic ice will be consumed by supercooled water. At the end of the growth process, the temperature of water will return to its freezing point ( C). If the metastable state exists and remains during the thermal storage process, thermal energy can only be stored in the form of sensible energy. Temperature, ºC T i T id T f a a, b c d e Thermocouple position Liquid water dendritic ice ice d T n T C b c e Time, s Figure 1. Process of supercooled water solidification.

There are several studies about solidification of water. Chen et al. (1998), studied the numerical and experimental method to analyzer the influence of nucleation agents in the water solidification process inside cylindrical copper capsules of different sizes and Chen and Lee (1999), auditioning result whit different material of capsules. Yoon et al. (21) studied experimentally the freezing phenomenon of saturated water within the supercooled region in a horizontal circular cylinder using the holographic real time interferometry technique. Milón and Braga (23) studied the phenomenon of supercooling in spherical capsules of different diameters. 2. Experimental model The experimental model, shown schematically in Figure 1, consists in a test section (a), an observing system (b), a cooling system, which includes a CTB (Constant Temperature Bath), and a measurement and data acquisition system (d). ACQUISITION SYSTEM (d) CTB UPPER RESERVOIR TEST SECTION (a) CTB-IC DIGITAL CAMERA (b) LOWER RESERVOIR AIR COMPRESSOR Figure. 2. Experimental Model. 2.1. Test section The walls are made of 1 mm thick acrylic plate externally covered with 25 mm thick insulation. A cross section is shown in the Figure 3. The diffuser function is to homogenize the coolant temperature (T C ) in the test section. The temperature control is carried out by a constant temperature bath which receives the signals from a temperature sensor RTD type PT. K type thermocouples were used for the circulating fluid temperatures registration. An overflow tank, working at atmospheric pressure, was installed to compensate the volume variation during the phase change process. In the same figure, the cylindrical capsule, filled with the PCM (distilled pure water), can be observed. To define the volume of the PCM, a sliding disk (movable in the axial direction) is used. K type thermocouples of,76 mm diameter, covered with Teflon, are also indicated in Figure 4.

RTD PT COOLANT SECONDARY DIFFUSER THERMOCOUPLES CAPSULE FIXED DISK PCM OVERFLOW TANK SLIDING DISK THERMOCOUPLES COOLANT PRIMARY DIFFUSER Figure 3. Test section details. 21 22 26 25 24 23 coolant Figure 4. thermocouples positions. 2.2. Cooling system The cooling system is schematically showed in Figure 1. It is composed by two constant temperature baths (CTB), two reservoirs (upper and lower) and the coolant. The initial temperature for the tests is set at one CTB-IC while the other CTB is set at the test temperature. The temperature control system Proportional Integral Derivative (PID) maintains the temperature into a range of ±.5 C with a refrigeration power of 8 W at ºC and 1 W of electric power heater. The coolant is an alcohol-water solution (5% in volume). 2.3. Measuring and data logging system The measurements and storage of data are made by the data acquisition system and a personal computer (PC). The acquisition equipment, which communicates with the PC by the RS232 communication port, receives, processes and transmits the temperature signals to PC, for storage and posterior analysis. 3. Experimental procedure Stage I: The initial water temperature inside the capsule (25. ºC) is imposed using the constant temperature bath for the initial condition (CTB-IC). The other CTB controls the coolant temperature in the upper reservoir.

Stage II: The coolant of the upper reservoir pass through the tests section imposing the test temperature, absorbing the initial thermal loads and passing later to the lower reservoir. Stage III: The coolant of the CTB is addressed toward the test section until the conclusion of the test. Stage IV: After each test, a pump impels the coolant toward the upper reservoir for a new test. This procedure is carried out to maintain constant the test temperature along each test. The duration of each test varies from 3 to 6 minutes, depending of the test conditions. The data is acquired once a second. 3.1. Uncertainties of measurements Uncertainties are presented in Table 1. 4. Results and discussion Table 1: Uncertainties of measurements Parameter Uncertainty Temperature.1 ºC Time.1 s Length.1 mm In Fig. 5, it can be observe some of the characteristic curves of the solidification process of the water in different materials from cylindrical capsules. It is shown the temperature variation of the different positions from the thermocouples inside of the capsule. In the cases of acrylic and PVC, the characteristic curve with more of 5% of occurrence probability it showed that the nucleation does not happen and the PCM stays in a metaestable liquid state, these experiences were stopped after 5 hours. In the cases of bronze and aluminum presented supercooling with nucleation, apparently the parameter that influenced more in this process is the thermal conductivity of the material. In Fig. 6, it is shown the advance of the solidification front according to the temperature of the TF, this for each material of the capsule. According to the statistical parameters it was observed that, for the case of PVC and acrylic only presented nucleation for temperatures of and ºC, being the acrylic the one which presents a smaller time of solidification. In the cases of bronze and aluminum, for the four temperatures, always nucleation happened. It is possible to stand out that in the cases of bronze with T C = and, supercooling does not appear. In Fig. 7, a report of the time of the solidification appears according to the temperature of the fluid of transference for the different materials from the capsules. In the case of acrylic and PVC, with temperatures greater to ºC, does not appear nucleation (it remains in liquid state), for the case of the bronze, this parameter is for smaller temperatures of - 4ºC, and in the case of aluminum, is of -6 ºC. This gives us a reference of which temperature is necessary to impose to the TF to obtain an effective solidification of the PCM within the capsule.

3 21 2 1 PVC 22 23 24 25 26 2 4 6 8 1 12 3 21 2 1 Acrylic 21 22 26 25 24 23 coolant 22 23 24 25 26 2 4 6 8 1 12 3 Bronze 21 22 2 1 23 24 25 26 2 4 6 8 1 12 3 Aluminium 21 22 2 1 23 24 25 2 4 6 8 1 12 Figure 5. Characteristic curves of cooled water encapsulated, T TF = -6 ºC

1.R solidification front.5r PVC.R 2 4 6 8 1 1.R frente de solidificación.5r Acrylic.R 2 4 6 8 1 1.R solidification front.5r Bronze -4-6.R 2 4 6 8 1 1.R solidification front.5r Aluminium -6.R 2 4 6 8 1 Figure 6. Variation of the solidification front for different capsules

14 12 solidification 1 8 6 4 2 PVC Acrylic Bronze Aluminium permanent supercooling -6-4 coolant 5. Conclusions Figure 7. Solidification time for different coolant temperature. According to the done test, the acrylic capsules and PVC with temperatures over to ºC, does not appear nucleation (it remains in metastable liquid state), for the case of the bronze, this happen for temperatures over to -4ºC and in the case of aluminum is -6 ºC. This gives us a reference of which temperature is necessary to impose to the T C to obtain an effective solidification of the PCM inside of the capsule. An indicative parameter of the time of solidification could be the material of the capsule because the results present an inverse relation with this parameter (to greater thermal conductivity, smaller time of solidification). 6. Acknowledgements This paper was supported by the Conselho Nacional de Desenvolvimento Científico e Tecnológico CNPq of Brazil. The authors also wish to thank the Agreement Pontificia Universidade Católica do Rio de Janeiro and Universidad Católica San Pablo for motivating this research work. 7. References Chen, S. L. and Lee, T. Z.,1998, A study of Supercooling Phenomenon and Frezing Probability of Water Inside Horizontal Cylinders, International Journal of Heat and Mass Transfer, Volume 41, Issues 4-5, 3, Pages 769-783. Yoon, J. I., Moon, C. G., Kim, E., Son, Y., S.J., Kim, D. and Kato T, 21, Experimental Study on Freezing of Water with Supercooled Region in a Horizontal Cylinder, Applied Thermal Engineering 21, 657-668. Milón, J.J., Braga, S.L., 24, Spherical Encapsulated Cold Storage, 4th European Thermal Science Conference. 8. Responsibility notice The authors are the only responsible for the printed material included in this paper.