 
          3405
        
        
          Technical Committee 307 + 212 /
        
        
          
            Comité technique 307 + 212
          
        
        
          the highly conductive stainless steel cell with the controlled
        
        
          water bath was accounted for as a convection-type boundary
        
        
          condition of the problem. This heat flux was assumed to be
        
        
          proportional to the difference between the temperature of the
        
        
          cell and the temperature of the water bath at each boundary
        
        
          node, through a convection coefficient
        
        
          
            h
          
        
        
          . Thermal optimisation
        
        
          was then aimed at identifying the values of the saturated thermal
        
        
          conductivity
        
        
          
        
        
          and the convection coefficient
        
        
          
            h
          
        
        
          . Calculations
        
        
          were performed for different combinations of
        
        
          
        
        
          and
        
        
          
            h
          
        
        
          . For each
        
        
          of them, a measure of the least squares difference between
        
        
          temperature simulation results and temperature experimental
        
        
          measurements
        
        
          
        
        
          was computed for different elapsed times. The
        
        
          three-dimensional plot in Figure 4 shows the least squares
        
        
          differences
        
        
          
        
        
          between simulation results and experimental
        
        
          observations
        
        
          
        
        
          The best agreement was obtained for parameters
        
        
          
        
        
          =1.6 Wm
        
        
          -1
        
        
          K
        
        
          -1
        
        
          and
        
        
          
            h
          
        
        
          =24 Wm
        
        
          -2
        
        
          K
        
        
          -1
        
        
          .
        
        
          n of thermal conductivity
        
        
          
        
        
          and
        
        
          nvection coefficient
        
        
          
            h
          
        
        
          (Lima 2011).
        
        
          irectly measured
        
        
          parameters from independent laboratory tests.
        
        
          xperime
        
        
          eatures of the hydro-thermal coupling
        
        
          under the test conditions.
        
        
          Figure 4. Three-dimensional graph showing the differences in
        
        
          temperature between observations and calculations in the back-analysis
        
        
          of the heating pulse test. Determinatio
        
        
          co
        
        
          Back-analysed thermal parameters were used to study the
        
        
          coupled thermal and hydraulic results. Water permeability and
        
        
          elastic soil parameters used in the simulations, which are
        
        
          reported in Table 1, were obtained from independent tests.
        
        
          Controlled-gradient tests at different temperatures and constant
        
        
          volume conditions for water permeability, as well as small-
        
        
          strain shear moduli with resonant column and bender element
        
        
          tests, have been reported by Lima (2011). Figure 5 displays the
        
        
          time evolution of temperature and pore water pressure
        
        
          (experimental and simulated results) during the same heating
        
        
          and cooling paths presented in Figure 2. A good agreement is
        
        
          observed in the pore water pressure response, which shows the
        
        
          consistency between the back-calculated and d
        
        
          Figure 5. Time evolution of temperature and pore water pressure:
        
        
          ntal and simulated results (Lima 2011).
        
        
          e
        
        
          5 CONCLUSIONS
        
        
          A series of heating and cooling paths were performed on Boom
        
        
          Clay –a reference host formation for potential geological
        
        
          disposal of ‘High-Level Radioactive Waste’ in Belgium– to
        
        
          study the impact and consequences of thermal loads on this low-
        
        
          permeability clay formation. Tests were performed in a fully-
        
        
          instrumented heating cell –with several thermocouples and
        
        
          pressure transducers– under constant volume and controlled
        
        
          hydraulic boundary condition: constant water pressure at the
        
        
          bottom drainage and top end with no flow condition. Selected
        
        
          results of a comprehensive experimental programme on intact
        
        
          borehole samples have been presented and discussed in terms of
        
        
          the joint measurements of temperature and pressure changes
        
        
          during the application of heating-cooling cycles.
        
        
          Thermal and hydraulic results were calibrated and simulated
        
        
          using coupled thermo-hydro-mechanical analyses performed
        
        
          with a finite element code (CODE_BRIGHT). In particular, the
        
        
          thermal conductivity of the clay was determined by back-
        
        
          analysis of the thermal response. The coupled thermal and
        
        
          hydraulic results were also successfully simulated using
        
        
          parameters that had been back-calculated from previous heating
        
        
          pulse tests and also directly from independent laboratory tests.
        
        
          An overall examination of the results obtained allows the
        
        
          identification of the main f
        
        
          
            upper valve closed
          
        
        
          
            backpressure 1MPa
          
        
        
          
            P = 9.58 W
          
        
        
          0 0.4 0.8 1.2 1.6 2
        
        
          Time (days)
        
        
          0
        
        
          0.4
        
        
          0.8
        
        
          1.2
        
        
          1.6
        
        
          2
        
        
          Pore water pressure (MPa)
        
        
          Stage 3
        
        
          
            Pw
          
        
        
          
            1
          
        
        
          
            Pw
          
        
        
          
            2
          
        
        
          
            Pw
          
        
        
          
            1
          
        
        
          
            bottom 25 mm
          
        
        
          
            Pw
          
        
        
          
            2
          
        
        
          
            top 75 mm
          
        
        
          Experimental results Numerical simulations
        
        
          0 0.4 0.8 1.2 1.6 2
        
        
          Time (day)
        
        
          0
        
        
          20
        
        
          40
        
        
          60
        
        
          80
        
        
          100
        
        
          Temperature (ºC)
        
        
          Stage 3
        
        
          Experimental results
        
        
          Numerical simulations
        
        
          
            T
          
        
        
          
            1
          
        
        
          
            T
          
        
        
          
            2
          
        
        
          
            T
          
        
        
          
            3
          
        
        
          
            T
          
        
        
          
            1
          
        
        
          
            heater
          
        
        
          
            T
          
        
        
          
            2
          
        
        
          
            bottom 25mm
          
        
        
          
            T
          
        
        
          
            3
          
        
        
          
            top 75mm
          
        
        
          (a)