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3. Derive energy balance equation, water vapor mass balance equation, and determine the heat transfer rate for the heating pr
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Answer #1

Let h_d be enthalpy of dry air and h_w be enthalpy of water vapour.

Then total enthalpy at temperature (t°C) = h = malha + w* h) = malCpt + wlhfg+Cpwt))

Where C_{p_{a}} = specific heat of air ,C_{p_{w}} = Specific heat of water, h_{fg} = latent heat of water, 0 = та = humidity ratio

In above equations, reference is taken that at 0C 0 = Py and also for saturated liquid water Hy = 0

Energy balance

maihı = mach2 mal(Cpeti + wi(hfg+Cpwtı)) +q = ma2(Cpet2 + w2(hfg + Cpwtz)) -Ans

Mass balance

As there is no other air or water vapour addition into the control volume

For air: Incoming air mass rate = outgoing air mass rate > ma = mas -Ans

For water vapour: Incoming water mass rate = outgoing water mass rate > mw, = mw

=> W1*ma, = W2 * max> W1= wz -Ans

Putting the values from answers from mass balance into the energy balance we will get

(Cpti + wlhfg+Cpwtı))+q = (Cp t2 + whfg+Cputz)) - Modified Energy balance equation

Heat transfer rate

From the last equation we can obtain q

q = (Cp t2 + wlhfg+Cpwtz)) - (Cpti + wlhfg + Cpwti)) ☆q = Cp.(t2 – tı) + Cpu (t2 – tı)-Ans

Approx numerical values of the constants used Cp. = 1.005kJ/kgK, Cp = 1.88kJ/kgk, hfq = 2501kJ/kg

PS: if this answer was helpful, would really appreciate your upvote

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