▪The PCM-epoxi nano-composite materials obtained as cross-linked three dimensional structures are attractive for space heating and cooling of buildings.

Slides:



Advertisements
Similar presentations
Boiling heat transfer of liquid nitrogen in the presence of electric fields P Wang, P L Lewin, D J Swaffield and G Chen University of Southampton, Southampton,
Advertisements

ENERGY CONVERSION MME 9617A Eric Savory
INTRODUCTION. Seminar on IMPROVEMENT OF THERMAL EFFICIENCY BY RECOVERY OF HEAT FROM IC ENGINE EXHAUST.
Laminar Flame Theory By Eng. Mohamad Okour UINVERSITY OF JORDAN MECHANICAL ENGINEERING DEPARTEMENT.
G  Love: Heated Gloves* Kristin Brodie, Jeff Colton, Colin Galbraith, Bushra Makiya and Tiffany Santos Summary: The goal of this project was to create.
So Far: Conservation of Mass and Energy Pressure Drop in Pipes Flow Measurement Instruments Flow Control (Valves) Types of Pumps and Pump Sizing This Week:
Characterization and modeling the thermo- mechanical cure-dependent properties of epoxy molding compound Reporter: Shi Lei Date:
Chapter 3.2: Heat Exchanger Analysis Using -NTU method
Chapter 2: Overall Heat Transfer Coefficient
Experiment : 5/03/2012 Presentation : 12/03/2012 Group B1/B Vartak Shankul Shisheer 10D Abhishek Mathur 10D Kunal Bhoyar 10D
DMSE G Love Prototype Presentation Kristin Brodie Jeff Colton Colin Galbraith Bushra Makiya Tiffany Santos.
Terry A. Ring Chemical Engineering University of Utah
CHE/ME 109 Heat Transfer in Electronics
Thermal Development of Internal Flows P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi Concept for Precise Design ……
XII International Symposium on Explosive Production of New Materials: Science, Technology, Business and Innovations, EPNM.
Correlations for INTERNAL CONVECTION P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi An Essential Part of Exchanging Heat……..
Liquid Argon in a Large Tank --- Some Thermodynamic Calculations Zhijing Tang November 4, 2004.
The PCM-epoxi nano-composite materials obtained as cross-linked three dimensional structures are attractive for space heating and cooling of buildings.
Wittaya Julklang, Boris Golman School of Chemical Engineering Suranaree University of Technology STUDY OF HEAT AND MASS TRANSFER DURING FALLING RATE PERIOD.
P.M.Pavel and M.Constantinescu. ICF-AR “Ilie Murgulescu” Bucuresti Romanian Academy of Science Institute of Physical Chemistry “Ilie Murgulescu” Spl. Independentei.
STRUCTURAL EVALUATION OF MATERIALS BASED ON XANTHAN GUM AND LIGNIN Irina Elena Raschip, Maria-Cristina Popescu “Petru Poni” Institute of Macromolecular.
Parameters for the thermal decomposition of epoxy resin/carbon fiber composites in cone calorimeter 4 th ICHS Conference, September 14, 2011 D. Quang Dao.
Fouling Factor: After a period of operation the heat transfer surfaces for a heat exchanger become coated with various deposits present in flow systems,
Unsteady Heat Transfer Many heat transfer problems require the understanding of the complete time history of the temperature variation. For example, in.
Heat Transfer Equations For “thin walled” tubes, A i = A o.
Biosystems engineering
Reporter: Lin, An Advisor: Chen, Chuh-Yean Date: 6/11.
Reporter: Yu-Syuan Lu Advisor: Wei-Tong Liao Date:05/18/2011.
Priplast Polyester Oligomers
Principles of Solar Engineering D. Y. Goswami, F. Kreith, J. F. KreiderPrinciples of Solar Engineering Chapter 4: Thermal Energy Storage and Transport.
So Far: Conservation of Mass and Energy Pressure Drop in Pipes Flow Measurement Instruments Flow Control (Valves) Types of Pumps and Pump Sizing This Week:
Chemical and Materials Engineering Department, University of Cincinnati, Cincinnati, OH Nanoscale Ni/NiO films for electrode and electrochemical Devices.
30 th June 20111Enrico Da Riva, V. Rao Parametric study using Empirical Results June 30 th 2011 Bdg 298 Enrico Da Riva,Vinod Singh Rao CFD GTK.
Silesian University of Technology in Gliwice Inverse approach for identification of the shrinkage gap thermal resistance in continuous casting of metals.
Experimental and numerical studies on the bonfire test of high- pressure hydrogen storage vessels Prof. Jinyang Zheng Institute of Process Equipment, Zhejiang.
Heat Transfer Equations. Fouling Layers of dirt, particles, biological growth, etc. effect resistance to heat transfer We cannot predict fouling factors.
Professor: Cheng-Ho Chen Student: Huang-Chi Hu Reporting date: 2015 / 03 / 25 1.
Heat Transfer Equations For “thin walled” tubes, A i = A o.
Chapter 2 Conduction Chapter 2.
HW/Tutorial # 1 WRF Chapters 14-15; WWWR Chapters ID Chapters 1-2
Crystal Growth General Formalism    Phase growing into  with velocity v : f ( “site factor” ) : fraction of sites where a new atom can be incorporated.
HW/Tutorial # 1 WRF Chapters 14-15; WWWR Chapters ID Chapters 1-2 Tutorial #1 WRF#14.12, WWWR #15.26, WRF#14.1, WWWR#15.2, WWWR#15.3, WRF#15.1, WWWR.
Heat Transfer by Convection
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 6 Introduction to convection.
‘SOLAR WATER HEATING SYSTEM WITH PHASE CHANGE MATERIAL’
Winter/ IntroductionM. Shapiro 1 Can calculate Q 12 [J] from the first law of thermo. קצב מעבר חום heat transfer rate can’t calculate from thermo.
Thermal Spray Coatings Asst.Prof.Dr. Ali Sabea Hammood Materials Engineering Department Materials Engineering Department Faculty of Engineering Faculty.
Clemson Hydro Heat Transport Temperature of a wolf pup.
Heat Transport Temperature of a wolf pup.
CASE STUDY : Solar Powered air conditioning as a solution to reduce environmental pollution in Tunisia.
Mariella Constantinescu Rumanian, born at in Bucharest
Submitted by Y.Venkata Ramireddy M.Sc Chemistry
HW/Tutorial # 1 WRF Chapters 14-15; WWWR Chapters ID Chapters 1-2
Introduction Methods Results Conclusions
Building Energy Analysis
APTES-BNNs / Epoxy Composites
Modeling a PCM storage unit for solar thermal cooling in Masdar City
From: Modeling a Phase Change Thermal Storage Device
M. Mahmoodi1, M. Arjmand2, U. Sundararaj2 and S. S. Park1
Unsteady Heat Transfer (Ch. 9- YAC)
UNIT - 4 HEAT TRANSFER.
Chapter 8 : Natural Convection
Experimental study of shaft resistance of energy pile
TEM – Lecture 2 Basic concepts of heat transfer:
Transient Heat Conduction
PRODUCT IDENTIFICATION STANDARD ACE FOAM SIZE (±1 TOLERANCE VALUE)
Chapter 19 FORCED CONVECTION
Chapter 19 FORCED CONVECTION
Forced Convection Trials at 100°C Natural Convection Trials at 100°C
Presentation transcript:

▪The PCM-epoxi nano-composite materials obtained as cross-linked three dimensional structures are attractive for space heating and cooling of buildings able to reduce the space and costs for containerization. ▪The use of PCM in buildings is possible only if some regulations and performance criteria are applied in accordance with the European Directions: resistance and stability, fire security, human health and environmental protection, energy saving and thermal insulation. ▪The stability of buildings depends on materials used for. Properties of nanocomposites substantially improved:  Mechanical properties : strength, modulus and dimensional stability  Thermal stability: Thermal resistance, flame retardancy and reduced smoke emissions  Decreased permeability to gases, water and hydrocarbons M.Constantinescu 1, D.Constantinescu 2, L.Dumitrache 3,,C.Perianu Marin 2, A.Stoica 1, M.Ladaniuc 3 P.M.Pavel 1 and M.Olteanu 1. 1 AR-ICF “Ilie Murgulescu”, 2 INCERC Bucharest, 3 ICECHIM Bucharest Romanian Academy of Science Institute of Physical Chemistry “Ilie Murgulescu” Spl. Independentei 202, Bucharest, + Hardening reaction of epoxi resin with PCM Nano composites preparation Demands for a Phase Change Material Physico-chemical: -Phase change temperature in the required domain -High latent heat of phase change and caloric capacity -High thermal conductivity -Low undercooling -Low volume changes -Reversible phase transition -Good physical and chemical stability Kinetical : -High nucleation and crystal grow velocity Economical : -low cost -Reciclability -Non-toxicity Material characterization and testing DSC for PEG 2000+Al DSC for epoxi-PEG Al SEM micrographs for polyethylene glycol (PEG) % epoxy resin Ropoxid % PEG +Al powder melted and mixed. Then hardener TETA or I 3361 was used Objectives and importance of energy storage in PCM Energy storage aims to reduce the conventional energy consumtion with a direct impact on CO 2 emissions. The advantages of phase change materials: A constant temperature domain for the phase transformation, chosen for each application. High storage density kWh/m 3 Directions of research on heat storage in phase change materials : ▪Finding new materials with superior performances ▪Elimination of existent material disadvantages. An epoxi-PCM was obtained and characterized whereas PCM was used polyethylene glycol of different molecular weights (1000, 1500, 2000). DSC for PEG 1500+Al CONCLUSIONS 1.The nanocomposite materials for buildings were obtained by using melted (PCM wt%Al powder for enhancing the thermal conductivity of the system ) 70 wt%, incorporated in an epoxidic resin 30 wt%. For all Epoxi-PCM materials was used Ropoxid 501 (Policolor), with 26% hardener threeethylentetramine (TETA) or I 3361 (Policolor). The composition of the materials was PCM ( polyethyleneglycoles 1000, 1500 and 2000) 70wt% and 30%epoxy resin, which hardened at the ambient temperature in 24 h and the process was ended in 7 days as can be seen from the process kinetics. 2.The materials were characterized and present good mechanical, thermal and chemical properties suitable for building materials. 3.The transfer coefficients calculated from the thermal discharging experiments in the shown set up indicated an acceptable value and time evolution. 4.These nano composites can be used for different applications in active or pasive systems, depending on their melting temperature. The geometry used depends also on their melting temperature and on the chosen application. 5. Energy storage in building materials will reduce the conventional energy consumptions, will increase the living comfort, decreasing the CO 2 emissions. PCM epoxy Maximum PCM in an epoxi matrix Nano composites PEG 1000,1500, PEG 2000 for different applications PC H2OH2O H2OH2O vacuu m Warm water thermocouples w0w0 w1w Amplifier interface air Thermostat Experimental set-up for heat transfer coefficient determination *interface pipe for transfer fluid-PEG Experimental cell SEM micrographs for polyethylene glycol (PEG) 1500SEM micrographs for polyethylene glycol (PEG) 1000 (PCM)-EPOXI COMPOSITE BUILDING MATERIALS Kinetics of hardening reaction for the studied systems in isotherm regime from DSC experiments Ropoxid 501+I 3361, 0 PCM - Ropoxid 501+I 3361 PCM had no influence on the kinetics of the hardening process The thermo-physical properties of the PEG-epoxi composites. Type Temperature 0 C Density ρ Kg/m 3 Dimensional variation, d mm (L,B,W) Tempera ture 0 C Thermal conductivity W/(mK) Thermal diffusivity Mean value m 2 /s Specific heat,c, kJ/(kgK) Epoxy PEG T m T f  Epoxy PEG T m T f  Epoxy PEG T f * T ies and T int are the temperatures of the transfer fluid at exit respectively entrance at the interface PEG-transfer fluid, T f is the phase change temperature, ΔT = T ies - T int Temperature distribution in the PEG 1500 system at thermal discharge 1/k chf = 1/k exp – d 1 / λ *k chf is the heat transfer coefficient at the interface PEG-transfer fluid during phase change, d 1 /λ is the thermal resistance of the PEG layer between the thermocouple T 1 and the interface PEG-transfer fluid, k exp is the experimental heat transfer coefficient between the thermocouple T 1 and the transfer fluid, λ = W/mK is the thermal conductivity of PEG, d 1 = m is the distance between the thermocouple T 1 and the interface PEG-transfer fluid. κ exp = q chf (T 1 - T c ) = [q exp - q sens ] /(T 1 - T c ) *q chf is the rate of heat flow during the phase change, q exp is the rate of experimental heat flow, q sens is the rate of sensible heat flow, T c = (T int + T ies )/2 is the mean temperature of the transfer fluid. q sens =  PEG V PEG c PEG (T 0 - T fin )[1 - (T med - T fin )/(T 0 - T fin )]/(AcΔt ) *T 0 = [T 1 (t 0 ) + T 4 (t 0 )]/2 = o C is the mean temperature of PEG at the start of thermal discharge, T fin = [T 1 (t fin ) + T 4 (t fin )]/ o C is the mean temperature of PEG at the end of thermal discharge, T med = [T 1 (t) + T 4 (t)]/2 is the mean temperature of PEG at the momemnt t, Δt-time between two readings of T 1 and T 4, V PEG = m 3 is volume, c PEG = 2440 J/KgK specific heat,  PEG = Kg/m 3 density of PEG. Time evolution of q exp, q chf and k chf q exp =  c c c D c (T int - T ies )/A c *A c = m 2 is the surface of the interface between PEG and transfer fluid, D c = 0.5 l/min is the flow rate,  c = Kg/m 3 is the density and c c = 4183 J/KgK specific heat of the transfer fluid. where: * T f is the phase change temperature, “a” was calculated from thermal conductivity, thermal diffusivity and density were measured in standard conditions. The maximum error for dimensional variation was ± 1.5% even after PCM was melted PEG + Ropoxid 501Ropoxid 501 Ropoxid 501 TETA Heat transfer coefficients determination