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With this assumption, a two-equation version of Huang s three-equation model (which included ltration ow Huang 1979) can be expressed as the following differential permeability-based model: 2 pv m m pv e l pv e l T + rl = mm + rl pv t T t x x x 2 e pv e T 2 T f T + (rc p ) - hfg r l l = fB 2 + B - hfg r l l B pv t T t x x x where: r = the density (kg m-3) rl = the liquid (water) density (kg m-3) el = the volume fraction of liquid (water) in porous medium pv = the partial pressure of water vapour (N m-2) T = the temperature (K) mm = the differential permeability (s) x = the spatial dimension in the direction of transfer (m) hfg = the latent heat of vapourisation (of water) (kJ kg-1) f = the thermal conductivity of porous medium (W m-1K -1) cp = the speci c heat capacity (kJ kg-1 K-1) (subscript B refers to the bulk porous material).

Equation 31 describes mass conservation of liquid water (the mass of water vapour in the pores is assumed to be negligible due to the low vapour density compared with that of water) Equation 32 describes heat energy conservation The local volume fraction of liquid in porous material (el) is governed by the vapour pressure (pv) and temperature (T) through the material sorption isotherm The sorption isotherm of a material relates the local volume fraction of liquid in material to the local relative humidity of air at constant temperature Relationships for a variety of construction materials can be found in the literature (eg Hansen 1996) Partial discretisation and solution of equations for heat and mass transfer In many applications, reducing Equations 31 and 32 to a pair of ordinary differential equations (ODEs) by discretising the spatial terms only can have advantages over full discretisation.

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Figure 3.4 Fit of the southern continents and India (redrawn from Smith & Hallam, 1970, with permission from Nature 225, 139 44. Copyright 1970 Macmillan Publishers Ltd).

First, the equations can be reduced to a form that is consistent with any other equations present in the model (for instance, if plant were to be included see 5) Second, the equations can then be solved using one of a large number of standard ODE solvers, some of which are especially suited to problems involving mixed dynamics so called stiff problems (see Section 54) The spatial terms, for example, the vapour pressure terms on the right hand side of Equation 31, can be dealt with as follows: 2 pv x 2 @ pv (n + 1) - 2 pv (n) + pv (n - 1) Dx 2 (31).

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Here, wCHR(1, TCIN, Design) is the model prediction at full-load (qCHR = 1) and at the speci c design inlet temperature of the cooling medium TCIN, Design. The power demand of a chiller under a particular combination of load and cooling medium supply temperature can then be evaluated from: WCHR (qCHR , TCIN ) = cF wCHR (qCHR , TCIN )WCHR (1, TCIN,Design ) (4.11)

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Finally, here s a list of the miscellaneous things you ll need as well: Hot glue sticks Fine-grit sandpaper Superglue Extra X-Acto blades (always a good thing to have on hand!) Electrical tape An electric drill and the following bit sizes: 1/8 , 15/64 , 3/16 , and 1/4 . (I d suggest borrowing these from a friend, since it s better than buying them to only use this once.)

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