COMPARING THE THERMAL PERFORMANCE OF GROUND HEAT EXCHANGERS OF VARIOUS LENGTHS

Size: px
Start display at page:

Download "COMPARING THE THERMAL PERFORMANCE OF GROUND HEAT EXCHANGERS OF VARIOUS LENGTHS"

Transcription

1 COMPARING THE THERMAL PERFORMANCE OF GROUND HEAT EXCHANGERS OF VARIOUS LENGTHS Marco Fossa Diptem, University of Genova, Via Opera pia 15a, Genova, ITALY Odile Cauret EDF R&D, "Energy in Buildings and Territories" Department, Moret-sur-Loing, France Michel Bernier École Polytechnique de Montréal, Département de génie mécanique, Montréal H3C 3A7, Canada ABSTRACT In many ground-coupled heat pump systems, borehole heat exchangers (BHE) represent the most important cost item. Therefore, alternative BHE construction should be investigated. In this paper the possibility of using short BHE (drilling depth lower than 50 m) is considered, based on the premise that shorther BHE drilling technologies and procedures could result in a lower cost per unit length of ground heat exchanger. The objective of this study is to compare the thermal performances of standard depth BHE with short ones, for a given building load. The thermal response of several BHE arrangements, expressed in the form of g-functions, are obtained using the so-called finite line source method with appropriate spatial superposition. The results are discussed with reference to literature data and also examined with respect to annual hourly simulations, in order to assess advantages of short BHE arrangements compared to current drilling solutions. 1. INTRODUCTION Ground-coupled heat pump (GCHP) systems are now routinely installed to provide space conditioning in a wide range of applications from small residences to large commercial buildings. In closed systems, a fluid is circulated in the ground heat exchanger and then in the evaporator of the heat pump (winter operating mode). Typically, the ground heat exchanger consists of vertical boreholes heat exchangers (BHE) that are approximately 100 m deep and have a diameter of about 100 mm. The number of boreholes in the bore field can range from one for a residence to several dozens in commercial applications. GCHP systems equipped with vertical BHE are characterised by relatively low operating costs. However, they require a high initial investment, mainly due to borehole drilling and installation. Therefore, in order to insure a durable development of GCHP systems, drilling and installation costs have to be reduced. In that context, this study explores the possibility of using short boreholes. Reducing drilling depth below 50 m could permit the use of geotechnical drilling materials and techniques that are less expensive and better adapted than standard deep vertical boreholes, in particular in Europe. However, using shorter boreholes can have consequences in term of thermal performances will the possible result that more

2 boreholes may be required. The objective of this study is to compare the thermal performances of standard depth BHE with short BHE, for a given building load.. THEORETICAL BACKGROUND AND ANALYSIS The thermal interaction between the ground and a BHE arrangement, when underground water circulation can be neglected, is governed by the three-dimensional time-dependent conduction equation. Due to its complexity this equation is usually solved numerically. However, a number of one-dimensional (in the radial direction) and two-dimensional (radial and axial) analytical solutions exists. Combined with spatial superposition, these solutions can be used to obtain a quasi three-dimensional solution to heat transfer from BHE leading to relatively short computational time even for multi- annual hourly simulations. Analytical approaches can be divided into models based on the line source theory and models based on the cylinder source method (CSM). Both methods give the radial temperature distribution as a function of time. The line source theory, introduced by Kelvin in 188 (cited by Ingersoll et al., 1954), approximates the BHE as an infinitely long line in an infinite medium subjected to a constant heat transfer rate per unit length. The medium is assumed to be initially at a uniform temperature and the thermal properties are assumed constant, The cylindrical source method was first introduced by Carslaw and Jaeger (1947). This method is similar to the line source method except that the constant heat transfer rate condition per unit length ( Q ) is applied to a cylindrical surface of radius r cyl. The ground temperature excess, with respect to far field temperature (T gr, ), is expressed in terms of Bessel s functions. Carslaw and Jaeger (1947) have also presented an abbreviated expression using a G function: Q T ( r) Tgr, = G( Fo, r / r cyl ) (1) k where: α t Fo = () r cyl and k and α are the ground thermal conductivity and thermal diffusivity, respectively. Tabulated values of G are presented by Carslaw and Jaeger (1947). Recently Bernier (001) provided a correlation to approximate the G-function A number of authors, including Deerman and Kavanaugh (1991) and Bernier et al. (004) have employed the CSM solution with success. A new insight to the linear source theory is given by the analysis of the finite linear source model (FLS). Even if the problem was already tackled by Eskilson (1987), a major contribution to the FSL solution was given first by Zeng et al. (00) and later by Lamarche and Beauchamp (007). The Lamarche and Beauchamp solution in particular provides the averaged (along the depth) borehole temperature in terms of the complementary error function (erfc) according to the expression: T ave ( r) T gr, Q = π k β + 1 β erfc z β + 4 ( γ z) erfc( γ z) β dz D A β + 1 z β dz D B (3) where β is the radial distance made dimensionless by the BHE depth H, and γ is related to a Fourier number based on the BHE depth, Fo H :

3 0.5 α t 0.5 γ = 0.5 = 0.5Fo H H (4) In Eq. (3), D A and D B are also expressed as a function of erfc, and they are constants at given time and depth H. The first integral is improper and has to be handled with suitable numerical techniques. Readers are referred to the work of Lamarche and Beauchamp (007) and Cauret and Bernier (009) for more details. In this paper the FLS solution expressed by Eq. (3) is iteratively calculated until a given degree of accuracy is obtained in either the proper or improper integral by employing the extended midpoint algorithm (Press et al., 199).Of practical interest is the calculation of the time varying temperature at the borehole boundary, i.e. for r = r b. A hybrid method, which combines the advantages of numerical and analytical techniques, is used to account for borehole thermal interaction.it exploits the linear properties of the conduction equation to perform a solution superposition. The superposition of single solutions can be made either with respect to similar thermal pulses applied in different BHE in a bore field (spatial superposition ) or to a series of different thermal pulses applied in a single BHE (superposition in time). The spatial superposition can be applied to calculate the response of a BHE field to a heat step pulse, resulting in a mean borehole wall temperature for the whole bore field. The superposition in time was first suggested by Eskilson (1987) and then refined as a numerical technique by Yavuzturk and Spitler (1999) and by Bernier et al. (004). The best known hybrid approach is the one introduced by Eskilson (1987). It is based on dimensionless temperature response factors, called g-functions. They were obtained using a - D numerical calculation using the transient finite-difference equations on the radial-axial coordinate system with a given borehole wall temperature. Eskilson (1987) established that the thermal response is a function of four parameters: i) the Fourier number, ii) r b /H, iii) B/H where B is the distance between boreholes, iv) the bore field configuration. Therefore, the thermal response of a given bore field geometry can be expressed as: Q ave Tave( rb ) Tgr, = g ( ln(9 FoH ), rb / H, B / H, borefield geometry) π k (5) where T ave (r b ) is the average borehole wall temperature for the whole borefield, and Q ave is the average heat transfer rate per unit length. Eskilson (1987) has evaluated g-functions for a number of configurations. However, in the case of the present study, the g-functions available in the literature did not cover the full range of bore field configurations. Therefore, g- functions were generated using the FLS solution combined with spatial superposition. The procedure is as follows: first, the temperature at each borehole wall (at r=r b ) is evaluated. This temperature is the result of the heat transfer rate (constant at all BHE) applied to the borehole itself and of the thermal influence of the other boreholes in the bore field. Mathematically, for N boreholes and a given heat transfer rate per unit length, this can be expressed as: N T i ( rb ) = T j ( rj i, t) (6) where r j-i represents the distance between borehole i and j with r j-i equal to r b for i=j. The FLS solution (Eq. 3) is thus applied N times to obtain the average borehole temperature of borehole i. Finally the average borehole temperature of the whole bore field, T ave, is obtained as: T ave ( r ) 1 b = N N T ( r i b ) (7)

4 By repeating the calculation at different time steps (i.e. various Fo), it is possible to infer the thermal response of the whole bore field and, using Eq. (5), to calculate the g-function of the BHE system under investigation. Finally, by varying the field geometry and depth, it is possible to compare the performance of different BHE arrangements, including short and long BHE arrays. Once a g-function is available, the time superposition can be applied to investigate the ground response of complex heat loads made by a series of basic heat pulses. Once the g-functions are known, it is possible to use them in cases of time varying heat pulses. This can be accomplished using temporal superposition (see for example, Yavuzturk and Spitler, 1999). One other method that has been suggested is the one developed by Bernier (Bernier et al., 004, Bernier et al., 008). In this method, the mean borehole fluid temperature at time t, T f,t, can be obtained using the following relationship: 1 T f,t = Tgr, + Tp,t + Q' ave Rb ( MLAA ) (8) kh where, T p,t is the temperature penalty at time t, R b is the steady-state borehole thermal resistance per unit length of bore, H is the borehole length, and MLAA is a multiple load aggregation algorithm. The temperature penalty accounts for thermal interaction among boreholes. It uses g-functions (generated as described in this paper by the FLS method) to obtain the average temperature increase (decrease) at the borehole wall caused by the thermal interaction from the other boreholes. It is evaluated using the average heat transfer rate over the period from time =0 to the time=t. The MLAA term on the right hand side of equation 1 account for heat transfer at the borehole level (excluding borehole interaction). This term represents the temperature difference between the borehole wall and the undisturbed ground. This difference is evaluated using the cylinder source model combined with temporal superposition as outlined by Bernier et al. (004). 3. RESULTS AND DISCUSSION The objective of this study is to use g-functions to compare the thermal performance of short and standard BHE depths. The standard reference configurations are 100 m deep while the short BHEs have depths of 60, 50, 40 and 30 m. Results concerning 50 and 40 m are here discussed. Before performing the comparisons described above, a number of preliminary runs have been made in order to assess the reliability of the numerical technique and of the FLS method itself, with respect to the numerical solutions obtained by Eskilson. The configurations that were examined included single boreholes, x8 in line, and square bore fields, up to 8x8. Figures 1 and report some results of this preliminary analysis with 8x1 and 3x3 geometries. As indicated in equation 5, g-functions are a function of time (expressed here by the natural logarithm of 9 times the Fourier number). They are also a function of r b /H ( in this case), of the bore field configuration (8x1 and 3x3 in this case), and of the borehole spacing ratio B/H. The FLS solutions are here overlapped to the original Eskilson graphical solutions for different borehole spacing ratio B/H, where the single BHE case is represented by B/H=. As can be observed in both figures, the agreement among the FLS and the Eskilson results is very good. For the sake of brevity it is not possible to show all the results obtained, but it must be outlined that the FLS solutions sometimes overestimated the Eskilson g-function for small values of the parameter B/H (as in Figure ), while in other cases the behaviour was opposite, with the FLS solution underestimating the Eskilson g-function for large values of the B/H parameter (as in Figure 1). This behaviour was also observed by Sherif (007).

5 B/H= g-function B/H=0.1 B/H=0.15 B/H=0. B/H= g-function B/H=0.05 B/H=0.15 B/H=0.3 B/H=0.1 B/H=0. 1 B/H= ln(9fo H ) ln(9fo H ) Calculated g-function values and comparison with graphical results by Eskilson. Figure 1: 8 boreholes in line Figure : 9 boreholes in a regular square 0 As a general finding, the FLS solution agreed with the original Eskilson solution within ±10%. This discrepancy could be ascribed to the different boundary condition employed in the FLS method (constant heat flux along BHE) with respect to boundary condition employed in the original work by Eskilson (constant temperature along BHEs). In order to assess the effect of the boundary conditions on the solution in terms of g-function, a single FLS calculation (8x4 array, B/H=0.05) was made by modifying the numerical routine in order to iteratively change the heat flux at each BHE until a common BHE temperature was obtained. This single attempt revealed that the FLS solutions obtained with both boundary conditions are very similar: both the constant flux and the (almost) constant temperature solutions obtained with the FLS method overestimate (8% for ln(9fo H )=3) the Eskilson values. These evidences deserve an in-depth examination and the matter will be discussed in a future paper. Given that the g-functions generated by the FLS are reliable, attention will now be turned to the thermal performance comparison between shorth and long boreholes. In order to perform this comparison, the FLS equations were solved iteratively by changing the borehole-toborehole distance B, until the asymptotic value of the g-function of the short field had attained approximately the same values as the standard ones. The asymptotic value of the g- function indicates that the bore field as reached a somewhat steady-state condition. It must be noticed that the analysis was carried out by imposing that the overall length of standard and short BHE arrays were the same. Furthermore, the borehole radius, r b, was constant and equal 0.05m. Figures 3a and 3b show the calculated g-function values of equivalent BHE configurations with respect to a reference one, constituted by 4 ground heat exchangers in line, having different spacings. The equivalent short BHE configurations considered here are x4 and 1x10 with corresponding depths of 50 and 40 m, respectively. The examination of Figure 3a reveals that it is possible to obtain shorth boreholes that have the same steady-state g-function as longer boreholes. For example, in Figure 3a the shorth x4 configuration with B=7 m and H=50 m is equivalent, at steady-state, to the standard 100 deep configuration with B/H=0.05. A

6 g-function x4 B/H=0.05 x4 B=7m 1x4 B/H=0.1 x4 B=10m 1x4 B/H=0.15 x4 B=13m 1x4 B/H=0. x4 B=16m 1x4 B/H=0.3 x4 B=0m g-function x4 B/H=0.05 1x10 B=4m 1x4 B/H=0.1 1x10 B=6m 1x4 B/H=0.15 1x10 B=7m 1x4 B/H=0. 1x10 B=9m 1x4 B/H=0.3 1x10 B=11m H=100 H=50 4 H=40 H= ln(9fo H ) similar conclusion can be drawn in Figure 3b with 1x10, B=4 m and H=40 m configuration having the same steady-state value as the 1x4, 100 m deep configuration. Even though short and long boreholes may have the same g-functions at steady-state, they do not have the same performance during their life time. To illustrate this, the two top curves in Figure 3a will be used. Assuming that α=0.1 m /day and t=3650 days (10 years), then the value of ln(9fo H ) is equal to 0.73 and for the short and long boreholes respectively. Reading the g-functions from Figures 3a, one obtains values of 10.8 and 9.4 for the short and long boreholes, respectively. This indicates that, for a given heat pulse, the long borehole will have a lower borehole wall temperature. Thus, in a heat rejection situation the long borehole performs better than the shorther borehole with B=7 m. In order to have a short borehole perform better than the longer one, the borehole spacing has to be increased. For example, if B=10m (fourth line from the top) the g-function is then 8.7 giving the short borehole configuration a thermal performance advantage. The thermal performance of short and long borehole can also be compared by performing annual hourly simulations. Following the example provided above, a 0 year hourly simulation is performed for a 1x4 standard 100m deep borehole (B=5m) and a 4x short 50 m deep borehole (B=8m). A typical medium size building was used. Its building load is shown in Figure ln(9fo H ) Figures 3a and 3b: Calculated g-function values and possible equivalent configurations. Reference case is 4 boreholes in line with H=100m Figure 4: Hourly building load for simulation of long and short BHE configurations.

7 (a) (b) Figure 5a and 5b: Hourly response of long (a) and short (b) BHE fields in terms of mean fluid temperature In order to simplify the analysis a constant COP of 4 was used in both heating and cooling and the borehole resistance was artificially set to zero. The ground thermal conductivity was set to.5 W/mK and T gr, =10 C. Equation 8 was used to obtain the mean fluid temperature. Results are shown in Figures 5a and 5b for the standard and the short boreholes, respectively. As can be seen both bore fields experience the same thermal performance with the mean fluid temperature being almost equal during every hour of a 0 year simulation. 4. CONCLUSIONS In this paper, the thermal response of a number of BHE arrangements, expressed in the form of g-functions, are obtained using the so-called finite line source method with appropriate spatial superposition. The generated g-functions are generally in good agreement with those of Eskilson. However, an in-depth study is needed to clearly understand some minor differences. These new g-functions have been used to compare the thermal performances of short boreholes (H< 50 m) with standard ones (H=100m) for a constant overall length. This study shows that shorter and standard boreholes can have similar performances during a great part of their working time, provided that shorter boreholes are spaced further apart than

8 standard ones. In this sense either a long terms analysis, based on the g-function approach, or a more detailed one based on the BHE response to short term thermal pulses (hourly loads managed by an aggregation algorithm) are necessary to perform a correct comparison of various BHE length, to infer the right spacings in case of short borehole fields and to draw some general sizing rules. This last aspect will be the subject of a future investigation. REFERENCES Bernier, M.A. (001). Ground Coupled Heat Pump System Simulation. ASHRAE Transactions, 106(1), Bernier, M.A., Pinel, P., Labib, R. Paillot, R. (004). A Multiple Load Aggregation Algorithm for Annual Hourly Simulations of GCHP Systems. International Journal of Heating, Ventilating, Air-Conditioning and Refrigeration Research, 10(4), Bernier, M.A., Chahla, A., Pinel, P Long-term Ground Temperature Changes in Geo-Exchange Systems, ASHRAE Transactions, 114() pp Zeng, H.Y., Diao, N.R., Fang, Z.H. (00). A Finite Line-Source Model for Boreholes in Geothermal Heat Exchangers. Heat Transfer-Asian Research, 31(7), Lamarche, L. Beauchamp, B. (007). A New Contribution to the Finite Line-Source Model for Geothermal Boreholes. Energy and Buildings, 39, Yavuzturk, C., Spitler, J.D. (1999). A Short Time Step Response Factor Model for Vertical Ground Loop Heat Exchangers. ASHRAE Transactions. 105(), Press, W.H., Flannery, B.P., Teukolsky, S.A. (199), Numerical Recipes in Fortran 77, Cambridge Press, Carslaw, H.S. and Jaeger, J.C Conduction of Heat in Solids. Oxford, U.K., Claremore Press. Ingersoll, L.R., Zobel, O.J. and Ingersoll, A.C. (1954). Heat Conduction with Engineering, Geological, and other Applications. New York, McGraw-Hill. Deerman, J.D. and Kavanaugh, S.P. (1991) Simulation of Vertical U-tube Ground Coupled Heat Pump Systems using the Cylindrical Heat Source Solution. ASHRAE Transactions 97(1), Eskilson, P. (1987) Thermal Analysis of Heat Extraction Boreholes. Ph.D. thesis, Lund University of Technology, Sweden. Cauret, O., Bernier, M. (009) Experimental Validation of an Underground Compact Collector Model, Proc. Effstock Conference, Stockholm, June 009. Sheriff, F. (007), Génération de facteurs de réponse pour champs de puits géothermiques verticaux, M.Sc.A., Département de Génie Mécanique. École Polytechnique de Montréal, Québec, Canada.

Analytical Modelling of Short-term Response of Ground Heat Exchangers in Ground Source Heat Pump Systems

Analytical Modelling of Short-term Response of Ground Heat Exchangers in Ground Source Heat Pump Systems Analytical Modelling of Short-term Response of Ground Heat Exchangers in Ground Source Heat Pump Systems Saqib Javed 1, Johan Claesson 1 and Per Fahlén 1 1 Chalmers University of Technology, Gothenburg,

More information

Modeling of Vertical Ground Loop Heat Exchangers with Variable Convective Resistance and Thermal Mass of the Fluid

Modeling of Vertical Ground Loop Heat Exchangers with Variable Convective Resistance and Thermal Mass of the Fluid Modeling of Vertical Ground Loop Heat Exchangers with Variable Convective Resistance and Thermal Mass of the Fluid Xiaowei Xu Jeffrey D. Spitler, Ph.D., PE Oklahoma State University Stillwater, OK, 7475

More information

Analytical Studies of the Influence of Regional Groundwater Flow by on the Performance of Borehole Heat Exchangers

Analytical Studies of the Influence of Regional Groundwater Flow by on the Performance of Borehole Heat Exchangers Analytical Studies of the Influence of Regional Groundwater Flow by on the Performance of Borehole Heat Exchangers Claesson, Johan; Hellström, Göran Published in: [Host publication title missing] Published:

More information

A dynamic model of a vertical direct expansion ground heat exchanger

A dynamic model of a vertical direct expansion ground heat exchanger A dynamic model of a vertical direct expansion ground heat exchanger B. Beauchamp 1, L. Lamarche 1 and S. Kajl 1 1 Department of mechanical engineering École de technologie supérieure 1100 Notre-Dame Ouest,

More information

Modelling of Thermal Behavior of Borehole Heat Exchangers of Geothermal Heat Pump Heating Systems

Modelling of Thermal Behavior of Borehole Heat Exchangers of Geothermal Heat Pump Heating Systems Modelling of Thermal Behavior of Borehole Heat Exchangers of Geothermal Heat Pump Heating Systems Gornov V.F. 1, Peskov N.V. 1,2, Vasilyev G.P. 1, Kolesova M.V. 1 1 JSC «INSOLAR-INVEST», Bol shaya Filevskaya

More information

This article appeared in a journal published by Elsevier. The attached copy is furnished to the author for internal non-commercial research and

This article appeared in a journal published by Elsevier. The attached copy is furnished to the author for internal non-commercial research and This article appeared in a journal published by Elsevier. The attached copy is furnished to the author for internal non-commercial research and education use, including for instruction at the authors institution

More information

Long-Term Performance of Borehole Heat Exchanger Fields with Groundwater Movement

Long-Term Performance of Borehole Heat Exchanger Fields with Groundwater Movement Excerpt from the Proceedings of the COMSOL Conference 2 Paris Long-Term Performance of Borehole Heat Exchanger Fields with Groundwater Movement S. Lazzari *,1, A. Priarone 2 and E. Zanchini 1 1 Dipartimento

More information

The thermal conductance of collection tubes in geothermal energy systems

The thermal conductance of collection tubes in geothermal energy systems Advanced Computational Methods and Experiments in Heat Transfer XIII 83 The thermal conductance of collection tubes in geothermal energy systems R. L. Frederick & A. Zenteno Departamento de Ingeniería

More information

Effective Borehole Thermal Resistance of A Single U-Tube Ground Heat Exchanger

Effective Borehole Thermal Resistance of A Single U-Tube Ground Heat Exchanger Numerical Heat Transfer, Part A: Applications An International Journal of Computation and Methodology ISSN: 1040-7782 (Print) 1521-0634 (Online) Journal homepage: http://www.tandfonline.com/loi/unht20

More information

Finite-Element Evaluation of Thermal Response Tests Performed on U-Tube Borehole Heat Exchangers

Finite-Element Evaluation of Thermal Response Tests Performed on U-Tube Borehole Heat Exchangers Excerpt from the Proceedings of the COMSOL Conference 2008 Hannover Finite-Element Evaluation of Thermal Response Tests Performed on U-Tube Borehole Heat Exchangers E. Zanchini,1 and T. Terlizzese 1 1

More information

An effectiveness - based analysis of ground coupled heat exchangers

An effectiveness - based analysis of ground coupled heat exchangers Scholars' Mine Masters Theses Student Research & Creative Works Spring 2014 An effectiveness - based analysis of ground coupled heat exchangers Chou Shen Follow this and additional works at: http://scholarsmine.mst.edu/masters_theses

More information

Heat Transfer Analysis of Centric Borehole Heat Exchanger with Different Backfill Materials

Heat Transfer Analysis of Centric Borehole Heat Exchanger with Different Backfill Materials Proceedings World Geothermal Congress 2015 Melbourne, Australia, 19-25 April 2015 Heat Transfer Analysis of Centric Borehole Heat Exchanger with Different Backfill Materials Lei H.Y. and Dai C.S. Geothermal

More information

Comparison of different Line Source Model approaches for analysis of Thermal Response Test in a U-pipe Borehole Heat Exchanger PATRICIA M.

Comparison of different Line Source Model approaches for analysis of Thermal Response Test in a U-pipe Borehole Heat Exchanger PATRICIA M. Comparison of different Line Source Model approaches for analysis of Thermal Response Test in a U-pipe Borehole Heat Exchanger PATRICIA M. MONZÓ Master of Science Thesis Stockholm, Sweden 2011 Comparison

More information

Comparison of different Line Source Model approaches for analysis of Thermal Response Test in a U-pipe Borehole Heat Exchanger PATRICIA M.

Comparison of different Line Source Model approaches for analysis of Thermal Response Test in a U-pipe Borehole Heat Exchanger PATRICIA M. Comparison of different Line Source Model approaches for analysis of Thermal Response Test in a U-pipe Borehole Heat Exchanger PATRICIA M. MONZÓ Master of Science Thesis Stockholm, Sweden 2011 Comparison

More information

A COUPLED FEM MODEL FOR NUMERICAL SIMULATION OF RECHARGEABLE SHALLOW GEOTHERMAL BHE SYSTEMS

A COUPLED FEM MODEL FOR NUMERICAL SIMULATION OF RECHARGEABLE SHALLOW GEOTHERMAL BHE SYSTEMS PROCEEDINGS, Thirty-Eighth Workshop on Geothermal Reservoir Engineering Stanford University, Stanford, California, February 11-13, 2013 SGP-TR-198 A COUPLED FEM MODEL FOR NUMERICAL SIMULATION OF RECHARGEABLE

More information

Analytical and Experimental Study on Coaxial Borehole Heat Exchangers

Analytical and Experimental Study on Coaxial Borehole Heat Exchangers University of Windsor Scholarship at UWindsor Electronic Theses and Dissertations 8-3-2017 Analytical and Experimental Study on Coaxial Borehole Heat Exchangers David Tyler Gordon University of Windsor

More information

An investigation on thermal interaction coefficient for multiple borehole heat exchangers

An investigation on thermal interaction coefficient for multiple borehole heat exchangers An investigation on thermal interaction coefficient for multiple borehole heat exchangers Ahmet Gultekin, Murat Aydin, Altug Sisman* Istanbul Technical University, Energy Institute, Istanbul, 34469, Turkey

More information

Computational modelling of a ground heat exchanger with groundwater flow

Computational modelling of a ground heat exchanger with groundwater flow Bulgarian Chemical Communications, Volume 48, Special Issue E (pp. 55-63) 2016 Computational modelling of a ground heat exchanger with groundwater flow Lazaros Aresti 1, Paul Christodoulides 2, Georgios

More information

Innovative Methodology to Compute the Temperature Evolution of Pile Heat Exchangers

Innovative Methodology to Compute the Temperature Evolution of Pile Heat Exchangers Proceedings World Geothermal Congress 2015 Melbourne, Australia, 19-25 April 2015 Innovative Methodology to Compute the Temperature Evolution of Pile Heat Exchangers Charles Maragna and Xavier Rachez BRGM,

More information

Numerical Evaluation of Long-Term Performance of Borehole Heat Exchanger Fields

Numerical Evaluation of Long-Term Performance of Borehole Heat Exchanger Fields Presented at the COMSOL Conference 2009 Milan Numerical Evaluation of Long-Term Performance of Borehole Heat Exchanger Fields A. Priarone *, S. Lazzari, E. Zanchini Dipartimento di Ingegneria Energetica,

More information

IMPROVEMENTS OF THERMAL RESPONSE TESTS FOR GEOTHERMAL HEAT PUMPS

IMPROVEMENTS OF THERMAL RESPONSE TESTS FOR GEOTHERMAL HEAT PUMPS - 1 - IMPROVEMENTS OF THERMAL RESPONSE TESTS FOR GEOTHERMAL HEAT PUMPS R. Wagner, E. Rohner, Geowatt AG, Dohlenweg 28, CH-8050 Zürich Abstract: At present, the ground thermal conductivity at borehole heat

More information

Principles of Food and Bioprocess Engineering (FS 231) Problems on Heat Transfer

Principles of Food and Bioprocess Engineering (FS 231) Problems on Heat Transfer Principles of Food and Bioprocess Engineering (FS 1) Problems on Heat Transfer 1. What is the thermal conductivity of a material 8 cm thick if the temperature at one end of the product is 0 C and the temperature

More information

Postprint.

Postprint. http://www.diva-portal.org Postprint This is the accepted version of a paper presented at International Ground-Source Heat Pump Association Research Conference 2018. Citation for the original published

More information

Chapter 4: Transient Heat Conduction. Dr Ali Jawarneh Department of Mechanical Engineering Hashemite University

Chapter 4: Transient Heat Conduction. Dr Ali Jawarneh Department of Mechanical Engineering Hashemite University Chapter 4: Transient Heat Conduction Dr Ali Jawarneh Department of Mechanical Engineering Hashemite University Objectives When you finish studying this chapter, you should be able to: Assess when the spatial

More information

Aalborg Universitet. CLIMA proceedings of the 12th REHVA World Congress volume 3 Heiselberg, Per Kvols. Publication date: 2016

Aalborg Universitet. CLIMA proceedings of the 12th REHVA World Congress volume 3 Heiselberg, Per Kvols. Publication date: 2016 Downloaded from vbn.aau.dk on: januar 19, 2019 Aalborg Universitet CLIMA 2016 - proceedings of the 12th REHVA World Congress volume 3 Heiselberg, Per Kvols Publication date: 2016 Document Version Publisher's

More information

AN EXPERIMENTAL STUDY OF THE FROST FORMATION ON A COLD SURFACE IN FREE CONVECTIVE FLOW

AN EXPERIMENTAL STUDY OF THE FROST FORMATION ON A COLD SURFACE IN FREE CONVECTIVE FLOW AN EXPERIMENTAL STUDY OF THE FROST FORMATION ON A COLD SURFACE IN FREE CONVECTIVE FLOW Giovanni Tanda, Marco Fossa DITEC, Università degli Studi di Genova via all Opera Pia 15a, I-16145 Genova, ITALY E-mail:

More information

HEAT TRANSFER IN A LOW ENTHALPY GEOTHERMAL WELL

HEAT TRANSFER IN A LOW ENTHALPY GEOTHERMAL WELL HEAT TRANSFER IN A LOW ENTHALPY GEOTHERMAL WELL Marcel Rosca University of Oradea, Armata Romana 5, RO-37 Oradea, Romania Key Words: low enthalpy, numerical modeling, wellbore heat transfer, Oradea reservoir,

More information

Comparison of Two Different Models for Pile Thermal Response Test Interpretation

Comparison of Two Different Models for Pile Thermal Response Test Interpretation Comparison of Two Different Models for Pile Thermal Response Test Interpretation Authors: Dr Fleur Loveridge 1, Prof William Powrie 2 & Duncan Nicholson 3 1. Corresponding author: Lecturer in Geomechanics

More information

ME 309 Fluid Mechanics Fall 2010 Exam 2 1A. 1B.

ME 309 Fluid Mechanics Fall 2010 Exam 2 1A. 1B. Fall 010 Exam 1A. 1B. Fall 010 Exam 1C. Water is flowing through a 180º bend. The inner and outer radii of the bend are 0.75 and 1.5 m, respectively. The velocity profile is approximated as C/r where C

More information

Effect of embedment depth and stress anisotropy on expansion and contraction of cylindrical cavities

Effect of embedment depth and stress anisotropy on expansion and contraction of cylindrical cavities Effect of embedment depth and stress anisotropy on expansion and contraction of cylindrical cavities Hany El Naggar, Ph.D., P. Eng. and M. Hesham El Naggar, Ph.D., P. Eng. Department of Civil Engineering

More information

THE ANALYSIS OF EXPANSION THERMAL RESPONSE TEST (TRT) FOR BOREHOLE HEAT EXCHANGERS (BHE)

THE ANALYSIS OF EXPANSION THERMAL RESPONSE TEST (TRT) FOR BOREHOLE HEAT EXCHANGERS (BHE) PROCEEDINGS, Thirty-Seventh Workshop on Geothermal Reservoir Engineering Stanford University, Stanford, California, January 30 - February, 0 SGP-TR-94 THE ANALYSIS OF EXPANSION THERMAL RESPONSE TEST (TRT)

More information

Specific heat capacity. Convective heat transfer coefficient. Thermal diffusivity. Lc ft, m Characteristic length (r for cylinder or sphere; for slab)

Specific heat capacity. Convective heat transfer coefficient. Thermal diffusivity. Lc ft, m Characteristic length (r for cylinder or sphere; for slab) Important Heat Transfer Parameters CBE 150A Midterm #3 Review Sheet General Parameters: q or or Heat transfer rate Heat flux (per unit area) Cp Specific heat capacity k Thermal conductivity h Convective

More information

This section develops numerically and analytically the geometric optimisation of

This section develops numerically and analytically the geometric optimisation of 7 CHAPTER 7: MATHEMATICAL OPTIMISATION OF LAMINAR-FORCED CONVECTION HEAT TRANSFER THROUGH A VASCULARISED SOLID WITH COOLING CHANNELS 5 7.1. INTRODUCTION This section develops numerically and analytically

More information

Lumped parameter thermal modelling

Lumped parameter thermal modelling Chapter 3 umped parameter thermal modelling This chapter explains the derivation of a thermal model for a PMSM by combining a lumped parameter (P) model and an analytical distributed model. The whole machine

More information

Chapter 4 TRANSIENT HEAT CONDUCTION

Chapter 4 TRANSIENT HEAT CONDUCTION Heat and Mass Transfer: Fundamentals & Applications Fourth Edition Yunus A. Cengel, Afshin J. Ghajar McGraw-Hill, 2011 Chapter 4 TRANSIENT HEAT CONDUCTION LUMPED SYSTEM ANALYSIS Interior temperature of

More information

EVALUATION METHOD OF GROUND WATER VELOCITY APPLYING THE GRADIENT OF THERMAL RESPONSE

EVALUATION METHOD OF GROUND WATER VELOCITY APPLYING THE GRADIENT OF THERMAL RESPONSE EVALUATION METHOD OF GROUND WATER VELOCITY APPLYING THE GRADIENT OF THERMAL RESPONSE T. Katsura Faculty of Environmental Engineering, The University of Kitakyushu Kitakyushu 808-0135, Japan Tel: +81-93-695-3236

More information

Development of a Thermo-Hydro-Geochemical Model for Low Temperature Geoexchange Applications

Development of a Thermo-Hydro-Geochemical Model for Low Temperature Geoexchange Applications Development of a ThermoHydroGeochemical Model for Low Temperature Geoexchange Applications F. Eppner *1, P. Pasquier 1, and P. Baudron 1 1 Department of Civil, Geological and Mining Engineering, Polytechnique

More information

QUESTION ANSWER. . e. Fourier number:

QUESTION ANSWER. . e. Fourier number: QUESTION 1. (0 pts) The Lumped Capacitance Method (a) List and describe the implications of the two major assumptions of the lumped capacitance method. (6 pts) (b) Define the Biot number by equations and

More information

On Clean Cooling Systems for Wind Turbine Nacelle operating in Hot Climate

On Clean Cooling Systems for Wind Turbine Nacelle operating in Hot Climate International Conférence en Clean Cooling Technologiesin the ME NA Regions ICT3_MENA 201 Bou Smail, W. Tipaza, 5-6 October 2015 On Clean Cooling Systems for Wind Turbine Nacelle operating in Hot Climate

More information

Conduction Heat Transfer. Fourier Law of Heat Conduction. Thermal Resistance Networks. Resistances in Series. x=l Q x+ Dx. insulated x+ Dx.

Conduction Heat Transfer. Fourier Law of Heat Conduction. Thermal Resistance Networks. Resistances in Series. x=l Q x+ Dx. insulated x+ Dx. Conduction Heat Transfer Reading Problems 17-1 17-6 17-35, 17-57, 17-68, 17-81, 17-88, 17-110 18-1 18-2 18-14, 18-20, 18-34, 18-52, 18-80, 18-104 Fourier Law of Heat Conduction insulated x+ Dx x=l Q x+

More information

Thermal Diffusivity of Plastic

Thermal Diffusivity of Plastic Thermal Diffusivity of Plastic School of Physics and Astronomy University of Manchester Amir El-hamdy Sohail Mahmood November 19, 2015 Date Performed: October 6-13, 2015 Demonstrator: Henry Cox Abstract

More information

NEW ANALYTICAL SOLUTION FOR SOLVING STEADY-STATE HEAT CONDUCTION PROBLEMS WITH SINGULARITIES

NEW ANALYTICAL SOLUTION FOR SOLVING STEADY-STATE HEAT CONDUCTION PROBLEMS WITH SINGULARITIES THERMAL SCIENCE: Year 3, Vol. 7, No. 3, pp. 665-67 665 NEW ANALYTICAL SOLUTION FOR SOLVING STEADY-STATE HEAT CONDUCTION PROBLEMS WITH SINGULARITIES by Najib LARAQI a* and Eric MONIER-VINARD b a Paris West

More information

This chapter focuses on the study of the numerical approximation of threedimensional

This chapter focuses on the study of the numerical approximation of threedimensional 6 CHAPTER 6: NUMERICAL OPTIMISATION OF CONJUGATE HEAT TRANSFER IN COOLING CHANNELS WITH DIFFERENT CROSS-SECTIONAL SHAPES 3, 4 6.1. INTRODUCTION This chapter focuses on the study of the numerical approximation

More information

Dynamic simulation and Control of a CO 2 Compression and Purification Unit for Oxy-Coal-Fired Power Plants

Dynamic simulation and Control of a CO 2 Compression and Purification Unit for Oxy-Coal-Fired Power Plants Dynamic simulation and Control of a CO 2 Compression and Purification Unit for Oxy-Coal-Fired Power Plants Authors A. Chansomwong, K.E. Zanganeh, A. Shafeen, P.L. Douglas,E. Croiset, L.A. Ricardez-Sandoval,

More information

MECH 375, Heat Transfer Handout #5: Unsteady Conduction

MECH 375, Heat Transfer Handout #5: Unsteady Conduction 1 MECH 375, Heat Transfer Handout #5: Unsteady Conduction Amir Maleki, Fall 2018 2 T H I S PA P E R P R O P O S E D A C A N C E R T R E AT M E N T T H AT U S E S N A N O PA R T I - C L E S W I T H T U

More information

S.E. (Chemical) (Second Semester) EXAMINATION, 2012 HEAT TRANSFER (2008 PATTERN) Time : Three Hours Maximum Marks : 100

S.E. (Chemical) (Second Semester) EXAMINATION, 2012 HEAT TRANSFER (2008 PATTERN) Time : Three Hours Maximum Marks : 100 Total No. of Questions 12] [Total No. of Printed Pages 7 Seat No. [4162]-187 S.E. (Chemical) (Second Semester) EXAMINATION, 2012 HEAT TRANSFER (2008 PATTERN) Time : Three Hours Maximum Marks : 100 N.B.

More information

Thermal Response Test experiments and modelling applied to shallow geothermal piles of different geometry

Thermal Response Test experiments and modelling applied to shallow geothermal piles of different geometry IGSHPA Research rack Stockholm September 18-20, 2018 hermal Response est experiments and modellin applied to shallow eothermal piles of different eometry Marco Fossa Fabio Minchio Davide Rolando ABSRAC

More information

Introduction to Heat and Mass Transfer. Week 5

Introduction to Heat and Mass Transfer. Week 5 Introduction to Heat and Mass Transfer Week 5 Critical Resistance Thermal resistances due to conduction and convection in radial systems behave differently Depending on application, we want to either maximize

More information

IBL. Design of Geothermal Heat Source Systems for Heating and Cooling Applications

IBL. Design of Geothermal Heat Source Systems for Heating and Cooling Applications Design of Geothermal Heat Source Systems for Heating and Cooling Applications - Introduction: Mechanisms of thermal transport, thermal properties of rock - Thermal response test - Design calculation methods,

More information

Heat and Mass Transfer Unit-1 Conduction

Heat and Mass Transfer Unit-1 Conduction 1. State Fourier s Law of conduction. Heat and Mass Transfer Unit-1 Conduction Part-A The rate of heat conduction is proportional to the area measured normal to the direction of heat flow and to the temperature

More information

Journal of Composite Materials. On Cyclical Hygrothermal Fields in Laminated Plates. Keywords: cyclical hygrothermal field, laminated plate

Journal of Composite Materials. On Cyclical Hygrothermal Fields in Laminated Plates. Keywords: cyclical hygrothermal field, laminated plate On Cyclical Hygrothermal Fields in Laminated Plates Journal: Journal of Composite Materials Manuscript ID: JCM--00 Manuscript Type: Original Manuscript Date Submitted by the Author: -Sep- Complete List

More information

Inverse Heat Flux Evaluation using Conjugate Gradient Methods from Infrared Imaging

Inverse Heat Flux Evaluation using Conjugate Gradient Methods from Infrared Imaging 11 th International Conference on Quantitative InfraRed Thermography Inverse Heat Flux Evaluation using Conjugate Gradient Methods from Infrared Imaging by J. Sousa*, L. Villafane*, S. Lavagnoli*, and

More information

ANALYSIS OF TRANSIENT HEAT CONDUCTION IN DIFFERENT GEOMETRIES BY POLYNOMIAL APPROXIMATION METHOD

ANALYSIS OF TRANSIENT HEAT CONDUCTION IN DIFFERENT GEOMETRIES BY POLYNOMIAL APPROXIMATION METHOD Int. J. Mech. Eng. & Rob. Res. Devanshu Prasad, Research Paper ISSN 78 9 www.ijmerr.com Vol., No., April IJMERR. All Rights Reserved ANALYSIS OF TRANSIENT HEAT CONDUCTION IN DIFFERENT GEOMETRIES Y POLYNOMIAL

More information

EXPERIENCE FROM THE FIRST THERMAL RESPONSE TEST (TRT) EQUIPMENT IN FINLAND. N. Leppäharju, I. Martinkauppi, M. Nousiainen

EXPERIENCE FROM THE FIRST THERMAL RESPONSE TEST (TRT) EQUIPMENT IN FINLAND. N. Leppäharju, I. Martinkauppi, M. Nousiainen EXPERIENCE FROM THE FIRST THERMAL RESPONSE TEST (TRT) EQUIPMENT IN FINLAND N. Leppäharju, I. Martinkauppi, M. Nousiainen Geological Survey of Finland P.O. Box 97, FI-67101 Kokkola, Finland nina.leppaharju@gtk.fi

More information

Documentation of the Solutions to the SFPE Heat Transfer Verification Cases

Documentation of the Solutions to the SFPE Heat Transfer Verification Cases Documentation of the Solutions to the SFPE Heat Transfer Verification Cases Prepared by a Task Group of the SFPE Standards Making Committee on Predicting the Thermal Performance of Fire Resistive Assemblies

More information

Modeling Transient Conduction in Enclosed Regions Between Isothermal Boundaries of Arbitrary Shape

Modeling Transient Conduction in Enclosed Regions Between Isothermal Boundaries of Arbitrary Shape JOURNAL OF THERMOPHYSICS AND HEAT TRANSFER Vol. 19, No., July September 2005 Modeling Transient Conduction in Enclosed Regions Between Isothermal Boundaries of Arbitrary Shape Peter Teertstra, M. Michael

More information

Thermal Power Calibration of the TRIGA Mark II Reactor

Thermal Power Calibration of the TRIGA Mark II Reactor ABSTRACT Thermal Power Calibration of the TRIGA Mark II Reactor Žiga Štancar Jožef Stefan Institute Jamova cesta 39 1000, Ljubljana, Slovenia ziga.stancar@gmail.com Luka Snoj Jožef Stefan Institute Jamova

More information

EMPIRICAL MODEL OF A 11 kw (NOMINAL COOLING) R134a WATER-WATER HEAT PUMP

EMPIRICAL MODEL OF A 11 kw (NOMINAL COOLING) R134a WATER-WATER HEAT PUMP EMPIRICAL MODEL OF A 11 kw (NOMINAL COOLING) R134a WATER-WATER HEAT PUMP Sébastien A. Brideau 1, Ian Beausoleil-Morrison 1, and Michaël Kummert 1 Department of Mechanical and Aerospace Engineering, Carleton

More information

Transactions on Modelling and Simulation vol 10, 1995 WIT Press, ISSN X

Transactions on Modelling and Simulation vol 10, 1995 WIT Press,  ISSN X High temperature heat transfer in glass during cooling - an experimental and computational approach K. Storck, M. Karlsson, B. Augustsson,* D. Loyd Applied Thermodynamics and Fluid Mechanics, Department

More information

AEROELASTIC ANALYSIS OF COMBINED CONICAL - CYLINDRICAL SHELLS

AEROELASTIC ANALYSIS OF COMBINED CONICAL - CYLINDRICAL SHELLS Proceedings of the 7th International Conference on Mechanics and Materials in Design Albufeira/Portugal 11-15 June 2017. Editors J.F. Silva Gomes and S.A. Meguid. Publ. INEGI/FEUP (2017) PAPER REF: 6642

More information

Diffusion in cylindrical geometry

Diffusion in cylindrical geometry 4/30/0 Random walk, etc. iffusion, cylindrical iffusion in cylindrical geometry In this exercise we will solve the diffusion equation in cylindrical geometry. We will use the same approach that was used

More information

ELECTRICAL AND THERMAL DESIGN OF UMBILICAL CABLE

ELECTRICAL AND THERMAL DESIGN OF UMBILICAL CABLE ELECTRICAL AND THERMAL DESIGN OF UMBILICAL CABLE Derek SHACKLETON, Oceaneering Multiflex UK, (Scotland), DShackleton@oceaneering.com Luciana ABIB, Marine Production Systems do Brasil, (Brazil), LAbib@oceaneering.com

More information

Aspect Ratio Considerations for Flat Bottom Hole Defects in Active Thermography

Aspect Ratio Considerations for Flat Bottom Hole Defects in Active Thermography More info about this article: http://www.ndt.net/?id=20749 Aspect Ratio Considerations for Flat Bottom Hole Defects in Active Thermography Abstract by M. Frendberg Beemer and S. Shepard Thermal Wave Imaging,

More information

Introduction to Heat and Mass Transfer. Week 8

Introduction to Heat and Mass Transfer. Week 8 Introduction to Heat and Mass Transfer Week 8 Next Topic Transient Conduction» Analytical Method Plane Wall Radial Systems Semi-infinite Solid Multidimensional Effects Analytical Method Lumped system analysis

More information

Delft University of Technology. Thermal Cone Penetration Test (T-CPT) Vardon, Phil; Baltoukas, Dimitris; Peuchen, Joek

Delft University of Technology. Thermal Cone Penetration Test (T-CPT) Vardon, Phil; Baltoukas, Dimitris; Peuchen, Joek Delft University of Technology Thermal Cone Penetration Test (T-CPT) Vardon, Phil; Baltoukas, Dimitris; Peuchen, Joek Publication date 2018 Document Version Publisher's PDF, also known as Version of record

More information

Heat processes. Heat exchange

Heat processes. Heat exchange Heat processes Heat exchange Heat energy transported across a surface from higher temperature side to lower temperature side; it is a macroscopic measure of transported energies of molecular motions Temperature

More information

Comparison of Finite Element Analysis to IEC for Predicting Underground Cable Ampacity

Comparison of Finite Element Analysis to IEC for Predicting Underground Cable Ampacity Comparison of Finite Element Analysis to IEC-60287 for Predicting Underground Cable Ampacity Simon Dubitsky Tor Ltd, St. Petersburg, Russia simon.dubitsky@ieee.org Georgy Greshnyakov Sevkabel Research

More information

Numerical Simulation and Air Conditioning System Improvement for the Experimental Hall at TLS J.C. Chang a, M.T. Ke b, Z.D. Tsai a, and J. R.

Numerical Simulation and Air Conditioning System Improvement for the Experimental Hall at TLS J.C. Chang a, M.T. Ke b, Z.D. Tsai a, and J. R. Numerical Simulation and Air Conditioning System Improvement for the Experimental Hall at TLS J.C. Chang a, M.T. Ke b, Z.D. Tsai a, and J. R. Chen a a National Synchrotron Radiation Research Center (NSRRC)

More information

12.009/ Problem Set 2

12.009/ Problem Set 2 12.009/18.352 Problem Set 2 Due Thursday, 26 February 2015 100 points total Problem 1: 15 pts (a,b)=(10,5) Problem 2: 45 pts (a,b,c,d,e,f)=(5,5,5,10,10,10) Problem 3: 40 pts (a,b,c,d,e,f)=(5,5,5,5,10,10)

More information

Chapter 2 Thermal Loading in Cutting Tools

Chapter 2 Thermal Loading in Cutting Tools Chapter 2 Thermal Loading in Cutting Tools When wood is processed by machines, the chip slides on the surface of the tool and friction work transforms into heat. Most of this heat flows into the direct

More information

Measurement of electric potential fields

Measurement of electric potential fields Measurement of electric potential fields Matthew Krupcale, Oliver Ernst Department of Physics, Case Western Reserve University, Cleveland Ohio, 44106-7079 18 November 2012 Abstract In electrostatics, Laplace

More information

ANALYTICAL AND NUMERICAL MODELING OF FOUNDATION HEAT EXCHANGERS LU XING. Huazhong University of Science & Technology. Wuhan, China

ANALYTICAL AND NUMERICAL MODELING OF FOUNDATION HEAT EXCHANGERS LU XING. Huazhong University of Science & Technology. Wuhan, China ANALYTICAL AND NUMERICAL MODELING OF FOUNDATION HEAT EXCHANGERS By LU XING Bachelor of Science in Mechanical Engineering Huazhong University of Science & Technology Wuhan, China 2008 Submitted to the Faculty

More information

Research on Performance of Ground-Source Heat Pump Double U Underground Pipe Heat Exchange

Research on Performance of Ground-Source Heat Pump Double U Underground Pipe Heat Exchange Open Journal of Modelling and Simulation, 2013, 1, 1-6 http://dx.doi.org/10.4236/ojmsi.2013.11001 Published Online January 2013 (http://www.scirp.org/journal/ojmsi) Research on Performance of Ground-Source

More information

Application of the Multi-current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols

Application of the Multi-current Transient Hot-Wire Technique for Absolute Measurements of the Thermal Conductivity of Glycols International Journal of Thermophysics, Vol. 26, No. 3, May 2005 ( 2005) DOI: 10.1007/s10765-005-5568-4 Application of the Multi-current Transient Hot-Wire Technique for Absolute Measurements of the Thermal

More information

Numerical studies on natural ventilation flow in an enclosure with both buoyancy and wind effects

Numerical studies on natural ventilation flow in an enclosure with both buoyancy and wind effects Numerical studies on natural ventilation flow in an enclosure with both buoyancy and wind effects Ji, Y Title Authors Type URL Numerical studies on natural ventilation flow in an enclosure with both buoyancy

More information

Fundamentals of Ground Source GTHP Pump Technology

Fundamentals of Ground Source GTHP Pump Technology M546 June 2015 Geo-Thermal Heating Fundamentals Chapter 1 Fundamentals of Ground Source GTHP Pump Technology Edward F Wahl, PhD, PE February 2015 copyright 2015 Edward F Wahl, PhD CHAPTER 1. Fundamentals

More information

Application of Hot Wire Technique and Comsol Multiphysics in the Heat Transfer Monitoring in Solids.

Application of Hot Wire Technique and Comsol Multiphysics in the Heat Transfer Monitoring in Solids. Application of Hot Wire Technique and Comsol Multiphysics in the Heat Transfer Monitoring in Solids. J. Hernández Wong 1, V. Suarez 1, J. Guarachi 1, A. Calderón 1, A. G. Juárez Gracia 1, J.B. Rojas- Trigos

More information

Heat and Mass Transfer Prof. S.P. Sukhatme Department of Mechanical Engineering Indian Institute of Technology, Bombay

Heat and Mass Transfer Prof. S.P. Sukhatme Department of Mechanical Engineering Indian Institute of Technology, Bombay Heat and Mass Transfer Prof. S.P. Sukhatme Department of Mechanical Engineering Indian Institute of Technology, Bombay Lecture No. 18 Forced Convection-1 Welcome. We now begin our study of forced convection

More information

1. Nusselt number and Biot number are computed in a similar manner (=hd/k). What are the differences between them? When and why are each of them used?

1. Nusselt number and Biot number are computed in a similar manner (=hd/k). What are the differences between them? When and why are each of them used? 1. Nusselt number and Biot number are computed in a similar manner (=hd/k). What are the differences between them? When and why are each of them used?. During unsteady state heat transfer, can the temperature

More information

Thermal conductivity measurement of two microencapsulated phase change slurries

Thermal conductivity measurement of two microencapsulated phase change slurries Thermal conductivity measurement of two microencapsulated phase change slurries Xiaoli Ma (corresponding author), Siddig Omer, Wei Zhang and S. B. Riffat Institute of Sustainable Energy Technology, School

More information

ASSUMPTIONS: (1) Homogeneous medium with constant properties, (2) Negligible radiation effects.

ASSUMPTIONS: (1) Homogeneous medium with constant properties, (2) Negligible radiation effects. PROBEM 5.88 KNOWN: Initial temperature of fire clay bric which is cooled by convection. FIND: Center and corner temperatures after 50 minutes of cooling. ASSUMPTIONS: () Homogeneous medium with constant

More information

GEOTHERMAL HELICAL HEAT EXCHANGER

GEOTHERMAL HELICAL HEAT EXCHANGER Proceedings of BS213: GEOTHERMAL HELICAL HEAT EXCHANGER Xavier MOCH 1,2, Marc PALOMARES 2, Fabrice CLAUDON 3, Bernard SOUYRI 1 and Benoît STUTZ 1 1 LOCIE - CNRS UMR 271, Le Bourget-du-Lac, France 2 RYB-Terra,

More information

Analysis of the Cooling Design in Electrical Transformer

Analysis of the Cooling Design in Electrical Transformer Analysis of the Cooling Design in Electrical Transformer Joel de Almeida Mendes E-mail: joeldealmeidamendes@hotmail.com Abstract This work presents the application of a CFD code Fluent to simulate the

More information

New correlations for the standard EN 1264

New correlations for the standard EN 1264 New correlations for the standard EN 164 Federico Boldrin, Michele De arli, Giacomo Ruaro DFT Dipartimento di Fisica Tecnica, Università degli Studi di Padova, Italy orresponding email: michele.decarli@unipd.it

More information

Experiment 1. Measurement of Thermal Conductivity of a Metal (Brass) Bar

Experiment 1. Measurement of Thermal Conductivity of a Metal (Brass) Bar Experiment 1 Measurement of Thermal Conductivity of a Metal (Brass) Bar Introduction: Thermal conductivity is a measure of the ability of a substance to conduct heat, determined by the rate of heat flow

More information

Non-fourier Heat Conduction in a Long Cylindrical Media with Insulated Boundaries and Arbitrary Initial Conditions

Non-fourier Heat Conduction in a Long Cylindrical Media with Insulated Boundaries and Arbitrary Initial Conditions Australian Journal of Basic and Applied Sciences, 3(): 65-663, 009 ISSN 1991-8178 Non-fourier Heat Conduction in a Long Cylindrical Media with Insulated Boundaries and Arbitrary Initial Conditions Mehdi

More information

The temperature of a body, in general, varies with time as well

The temperature of a body, in general, varies with time as well cen58933_ch04.qd 9/10/2002 9:12 AM Page 209 TRANSIENT HEAT CONDUCTION CHAPTER 4 The temperature of a body, in general, varies with time as well as position. In rectangular coordinates, this variation is

More information

Supercritical Helium Cooling of the LHC Beam Screens

Supercritical Helium Cooling of the LHC Beam Screens EUROPEAN ORGANIZATION FOR NUCLEAR RESEARCH European Laboratory for Particle Physics Large Hadron Collider Project LHC Project Report Supercritical Helium Cooling of the LHC Beam Screens Emmanuel Hatchadourian,,

More information

On A Comparison of Numerical Solution Methods for General Transport Equation on Cylindrical Coordinates

On A Comparison of Numerical Solution Methods for General Transport Equation on Cylindrical Coordinates Appl. Math. Inf. Sci. 11 No. 2 433-439 (2017) 433 Applied Mathematics & Information Sciences An International Journal http://dx.doi.org/10.18576/amis/110211 On A Comparison of Numerical Solution Methods

More information

Investigations of hot water temperature changes at the pipe outflow

Investigations of hot water temperature changes at the pipe outflow Investigations of hot water temperature changes at the pipe outflow Janusz Wojtkowiak 1,*, and Czesław Oleśkowicz-Popiel 1 1 Poznan University of Technology, Faculty of Civil and Environmental Engineering,

More information

ENCE 3610 Soil Mechanics. Site Exploration and Characterisation Field Exploration Methods

ENCE 3610 Soil Mechanics. Site Exploration and Characterisation Field Exploration Methods ENCE 3610 Soil Mechanics Site Exploration and Characterisation Field Exploration Methods Geotechnical Involvement in Project Phases Planning Design Alternatives Preparation of Detailed Plans Final Design

More information

3D UNSTEADY STATE ANALYSIS OF THERMAL PERFORMANCE OF DIFFERENTLY INSULATED FLOORS IN CONTACT WITH THE GROUND

3D UNSTEADY STATE ANALYSIS OF THERMAL PERFORMANCE OF DIFFERENTLY INSULATED FLOORS IN CONTACT WITH THE GROUND 3D UNSTEADY STATE ANALYSIS OF THERMAL PERFORMANCE OF DIFFERENTLY INSULATED FLOORS IN CONTACT WITH THE GROUND Giovanni Pernigotto, Giacomo Pernigotto, Marco Baratieri 2*, Andrea Gasparella 2 University

More information

Colloquium 2016: Assessment of the subsurface thermal conductivity for geothermal applications

Colloquium 2016: Assessment of the subsurface thermal conductivity for geothermal applications Page 1 of 66 Colloquium 2016: Assessment of the subsurface thermal conductivity for geothermal applications Jasmin Raymond Institut national de la recherche scientifique, Centre Eau Terre Environnement,

More information

Low Temperature Plasma Technology Laboratory

Low Temperature Plasma Technology Laboratory Low Temperature Plasma Technology Laboratory Equilibrium theory for plasma discharges of finite length Francis F. Chen and Davide Curreli LTP-6 June, Electrical Engineering Department Los Angeles, California

More information

6.2 Modeling of Systems and Components

6.2 Modeling of Systems and Components Chapter 6 Modelling of Equipment, Processes, and Systems 61 Introduction Modeling is one of the most important elements of thermal system design Most systems are analyzed by considering equations which

More information

Thermo-mechanics behaviour of energy pile subjected by monotonic thermal loading

Thermo-mechanics behaviour of energy pile subjected by monotonic thermal loading Thermo-mechanics behaviour of energy pile subjected by monotonic thermal loading M. E. SURYATRIYASTUTI a, H. MROUEH a, S. BURLON b a Laboratoire génie civil et géo-environnement (LGCgE), Polytech Lille-Université

More information

Numerical Analysis of Plate Heat Exchanger Performance in Co-Current Fluid Flow Configuration

Numerical Analysis of Plate Heat Exchanger Performance in Co-Current Fluid Flow Configuration Numerical Analysis of Plate Heat Exchanger Performance in Co-Current Fluid Flow Configuration H. Dardour, S. Mazouz, and A. Bellagi Abstract For many industrial applications plate heat exchangers are demonstrating

More information

A numerical study of heat transfer and fluid flow over an in-line tube bank

A numerical study of heat transfer and fluid flow over an in-line tube bank Fluid Structure Interaction VI 295 A numerical study of heat transfer and fluid flow over an in-line tube bank Z. S. Abdel-Rehim Mechanical Engineering Department, National Research Center, Egypt Abstract

More information

Chapter 5 MATHEMATICAL MODELING OF THE EVACATED SOLAR COLLECTOR. 5.1 Thermal Model of Solar Collector System

Chapter 5 MATHEMATICAL MODELING OF THE EVACATED SOLAR COLLECTOR. 5.1 Thermal Model of Solar Collector System Chapter 5 MATHEMATICAL MODELING OF THE EVACATED SOLAR COLLECTOR This chapter deals with analytical method of finding out the collector outlet working fluid temperature. A dynamic model of the solar collector

More information

Applied Fluid Mechanics

Applied Fluid Mechanics Applied Fluid Mechanics 1. The Nature of Fluid and the Study of Fluid Mechanics 2. Viscosity of Fluid 3. Pressure Measurement 4. Forces Due to Static Fluid 5. Buoyancy and Stability 6. Flow of Fluid and

More information