C.V.: Water from state 1 to state 2.
Process: constant volume (reversible isometric)
1: v1 = V/m = 0.35/10 = 0.035 ft3/lbm
⇒ x1 = 2.692 x 10-5
u1 = 45.11 Btu/lbm, s1 = 0.08779 Btu/lbm R Continuity eq. (same mass) and constant volume fixes v2
State 2: T2, v2 = v1 ⇒ x2 = (0.035 - 0.01799) / 3.3279 = 0.00511
u2 = 321.35 + 0.00511×788.45 = 325.38 Btu/lbm
s2 = 0.5033 + 0.00511×1.076 = 0.5088 Btu/lbm R
Energy eq. has zero work, thus provides heat transfer as
1Q2 = m(u2 - u1) = 10(325.38 - 45.11) = 2802.7 Btu
Entropy equation for the total control volume gives for a reversible process:
m(s2 - s1) = QL/T0
⇒ QL = mT0(s2 - s1)
= 10(77 + 459.67)(0.5088 - 0.08779)
= 2259.4 Btu
and the energy equation for the heat pump gives
WHP = 1Q2 - QL
= 2802.7 - 2259.4 = 543.3 B