Applied Geothermics Aachen 0ct 4 2004 Numerical Simulation of a Thermal Response Test (TRT) Experiment R. Wagner Applied Geophysics, Aachen University.

Slides:



Advertisements
Similar presentations
INTRODUCTION. Seminar on IMPROVEMENT OF THERMAL EFFICIENCY BY RECOVERY OF HEAT FROM IC ENGINE EXHAUST.
Advertisements

Irene Seco Manuel Gómez Alma Schellart Simon Tait Erosion resistance and behaviour of highly organic in-sewer sediment 7th International Conference on.
Application of Steady-State Heat Transfer
Institute of Energy and Sustainable Development Improvement of a Two-Dimensional (2D) Borehole Heat Exchanger (BHE) Model Miaomiao He, Simon Rees, Li Shao.
Institute of Energy and Sustainable Development Monitoring of a Large Scale Ground Source Heat Pump System - S.Naicker, Dr. Simon Rees IESD, De Montfort.
Estimation of Convective Heat Transfer Coefficient
Inversion of coupled groundwater flow and heat transfer M. Bücker 1, V.Rath 2 & A. Wolf 1 1 Scientific Computing, 2 Applied Geophysics Bommerholz ,
Heat Transfer Chapter 2.
Chapter 2: Overall Heat Transfer Coefficient
Analysis of Simple Cases in Heat Transfer P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Gaining Experience !!!
AAE450 Spring 2009 Slide 1 of 7 Orbital Transfer Vehicle (OTV) Thermal Control Ian Meginnis February 26, 2009 Group Leader - Power Systems Phase Leader.
Geo-Exchange Addison Parks and Andy Gerla. Summer Time Ground Temperature Constant 60 ̊ F Home walls are mainly heated from the Sun’s radiation and cooled.
Chamber Dynamic Response Modeling Zoran Dragojlovic.
LINEAR SECOND ORDER ORDINARY DIFFERENTIAL EQUATIONS
Update on Various Target Issues Presented by Ron Petzoldt D. Goodin, E. Valmianski, N. Alexander, J. Hoffer Livermore HAPL meeting June 20-21, 2005.
Feasibility Analysis h T1 T2 T3 T4 T5 One Dimensional Transient Analysis One Dimensional Finite Difference Steady State Analysis T1 and T5 will be known.
Building Services Engineering CHALMERS OPTIMIZATION OF GROUND COUPLED HEAT PUMP SYSTEMS Saqib Javed (PhD Researcher) Per Fahlén (Research Leader) Johan.
Dynamic thermal rating of power transmission lines related to renewable resources Jiri Hosek Institute of Atmospheric Physics, Prague, Czech Rep.
ENGINE Leiden Combining Areal Underground and Infrastructure Data to Minimize Exploration and Economic Risks Thomas Kohl, GEOWATT AG Clément Baujard,
Numerical and Experimental Study on Bed-to-Wall Heat Transfer in Conical Fluidized Bed Reactor 17 th International Conference on Mechatronics, Electrical.
The calculation methods of technological processes of underground heat extraction Alkhasov A., Alishaev M. (IGR DSC RAS) Matters of principle are considered.
ICHS4, San Francisco, September E. Papanikolaou, D. Baraldi Joint Research Centre - Institute for Energy and Transport
Pressure drop during fluid flow
Mitglied der Helmholtz-Gemeinschaft Simulation of the efficiency of hydrogen recombiners as safety devices Ernst-Arndt Reinecke, Stephan Kelm, Wilfried.
2-D Heat Transfer Model of A Horizontal U-Tube M. S. Islam 1, A. Fujimoto 2, A. Saida 2 and T. Fukuhara 2 2-D Heat Transfer Model of A Horizontal U-Tube.
ATLAS Calorimeter Argon Gap Convection Test Bed Brian Cuerden 24 Apr
Numerical Simulations of Silverpit Crater Collapse: A Comparison of TEKTON and SALES 2 Gareth Collins, Zibi Turtle, and Jay Melosh LPL, Univ. of Arizona.
20 th June 20111Enrico Da Riva, V. Rao Project Request and Geometry constraints June 20 th 2011 Bdg 298 Enrico Da Riva,Vinod Singh Rao CFD GTK.
Nuclear Thermal Hydraulic System Experiment
1 Numerical study of the thermal behavior of an Nb 3 Sn high field magnet in He II Slawomir PIETROWICZ, Bertrand BAUDOUY CEA Saclay Irfu, SACM Gif-sur-Yvette.
Modelling & Simulation of Chemical Engineering Systems Department of Chemical Engineering King Saud University 501 هعم : تمثيل الأنظمة الهندسية على الحاسب.
Lesson 13 CONVECTION HEAT TRANSFER Given the formula for heat transfer and the operating conditions of the system, CALCULATE the rate of heat transfer.
Specify domain’s starting fluid temperature on the Initial pane Porewater temperature is 40 °C.
One-Dimensional Steady-State Conduction
ATLAS Calorimeter Argon Gap Convection Test Bed April 25,
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.
21.4 Transport properties of a perfect gas
Convection: Internal Flow ( )
Purpose Probe construction Field and laboratory measurements Data processing, applicational example Conclusions, outlook A NEW METHOD TO DETERMINE in.
Convection in Flat Plate Boundary Layers P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi A Universal Similarity Law ……
J-PARC neutrino experiment Target Specification Graphite or Carbon-Carbon composite cylindrical bar : length 900mm, diameter 25~30mm The bar may be divided.
1 NUMERICAL AND EXPERIMENTAL STUDIES OF THIN-LIQUID-FILM WALL PROTECTION SCHEMES S.I. ABDEL-KHALIK AND M. YODA G. W. Woodruff School of Mechanical Engineering.
Internal Flow: Heat Transfer Correlations. Fully Developed Flow Laminar Flow in a Circular Tube: The local Nusselt number is a constant throughout the.
Porewater temperature is 40°C Specify domain’s starting fluid temperature on the Initial pane.
Shape Factor Example The shape factor can be modeled as thermal resistance as R t =1/kS, Therefore, it can be integrated with the electric circuit analog.
Cooling of GEM detector CFD _GEM 2012/03/06 E. Da RivaCFD _GEM1.
Simulation of heat load at JHF decay pipe and beam dump KEK Yoshinari Hayato.
Date of download: 5/28/2016 Copyright © ASME. All rights reserved. From: Forced Convection Heat Transfer in Spray Formed Copper and Nickel Foam Heat Exchanger.
CFD Exercise 1 Laminar & turbulent flows with COMSOL.
Temperature in the Crust Lijuan He Institute of Geology and Geophysics, Chinese Academy of Sciences.
EVALUATION OF LOW TEMPERATURE GROUND COUPLED VERTICAL HEAT EXCHANGER IN SOUTH LOUISIANA Md Adnan Khan, E.I.T Jay Wang, Ph.D.; P.E. Louisiana Tech University.
Lesson 7: Thermal and Mechanical Element Math Models in Control Systems ET 438a Automatic Control Systems Technology 1lesson7et438a.pptx.
This study processes the optimization of heat extraction under the varied pressure and flow rate. Based on the validated model, two kinds of test tube.
Algorithm of the explicit type for porous medium flow simulation
From: Hydraulic Loss of Finite Length Dividing Junctions
BCP Analysis Update Thomas Jones 22/7/16.
HW #4 /Tutorial # 4 WRF Chapter 18; WWWR Chapter 19 ID Chapter 6
One-Dimensional Steady-State Conduction
Date of download: 10/16/2017 Copyright © ASME. All rights reserved.
超臨界CO2在增強型地熱系統儲集層中取熱之研究-子計畫三 CO2在增強型地熱系統取熱模型之建構及效能分析
Experimental study of shaft resistance of energy pile
Thermal analysis Friction brakes are required to transform large amounts of kinetic energy into heat over very short time periods and in the process they.
Modelling of Combustion and Heat Transfer in ‘Swiss Roll’ Micro-Scale Combusters M. Chen and J. Buckmaster Combustion Theory and Modelling 2004 Presented.
Heat Exchanger Design Optimization
ET 438a Automatic Control Systems Technology
E. Papanikolaou, D. Baraldi
Project GEOCOND: Advanced materials and processes to improve performance and cost-efficiency of Shallow Geothermal systems and UTES Javier Urchueguía,
Natural Circulation and Convection
EoCoE – Results of the geothermal energy part
Presentation transcript:

Applied Geothermics Aachen 0ct Numerical Simulation of a Thermal Response Test (TRT) Experiment R. Wagner Applied Geophysics, Aachen University

The thermal power P of borehole Heat Exchangers (BHE) depends on Why run a Thermal Response Test? Circulation Rate [m 3 h -1 ]Thermal Conductivity [W m -1 K -1 ] Thermal Power P [kW] Production Temperature [°C] Circulation rate of BHE fluid Fluid thermal properties Injection and production temperature Rock thermal properties Rock hydraulic properties

TRT: Experimental Setup & Theory [Gehlin, 2002]

Constraints of The Line Source Approximation Rock thermal capacity can not be calculated independently from data The accuracy significantly depends critically on the length of the test interval No lateral and vertical variation of physical parameters allowed Experimental conditions (in particular Q) must remain constant S. Signorelli, Geoscientific Investigations For The Use of Shallow Low-Enthalpy Systems, Dissertation, Swiss Federal Institute of Switzerland; Zürch, 2004

Groenholland BV Test Facility HDPE Concentric Heat Exchanger Length heat exchanger40 m Outer pipe diameter40 mm Wall thickness3.7 mm Inner pipe diameter25 mm Wall thickness2.3 mm HDPE thermal conduct.0.42 W m -1 K -1 Operation Time h [Witte et al., 2002]

TRT Data from Heat Extraction Ground temperature13.75 °C Flow0.73 m 3 h -1 Fluid heat capacity3876 J kg -1 K -1 Fluid thermal conducivity0.502 W m -1 K -1 Fluid Density1026 kg m -3 Power W

C Brute Force: Numerical Simulation Simulation of BHE Experiment using highly resolved cylindrical FD grid 4940 nodes Cell size 0.75mm … 2.5 m timesteps  t=0.38 s Courant criterion  t=0.5 ms CPU time  30 h (SUN Enterprise 450) Seeking minimum misfit by variation of  c and

R = (  ) K 2 Data evaluation: temperature residuals Groenholland test facility accuracy Temperature Residual R [K 2 ] Thermal conductivity [W m -1 K -1 ] Thermal capacity  c [MJ m -3 K -1 ]

Synthetic Data 2D FD Grid Constant heat extraction  Q = -959,6 W at center node Heat Conduction only Simulation Time d Temperature Residual R [K 2 ] Thermal conductivity [W m -1 K -1 ] Thermal capacity  c [MJ m -3 K -1 ]

Temperature Residual R [K 2 ] Thermal conductivity [W m -1 K -1 ] Thermal capacity  c [MJ m -3 K -1 ] Synthetic Data 2D FD Grid Varying heat extraction  Q = W W at center node Heat Conduction only Simulation Time d

Conclusion The evaluation of TRT experiments by means of numerical simulation of flow and heat transport yield no unique thermal rock properties Varying heat extraction/injection with time allows to calculate thermal rock properties - Problem: conventional evaluation (line source approximation) can not be applied any more Better forecast: Measurement of thermal rock properties and numerical simulation of BHE Acknowledgments Henk Witte, Groenholland BV Amsterdam