(b)s₂ -S₁ =c_vIn(T₂/T₁) +R(v₂/v₁) and s₂ -s₁=c_p(T₂/T₁)-R(p₂/p₁)

273.15 K = 0℃. Molecular weights of air and water are 28.97 kg/kmol and 18 kg/kmol, respectively. Universal gas constant = 8.314 kJ/kmol-K. I ton =1000 kg. 1. A regenerative power cycle with one open feedwater heater is given in Figure 1 where the operation conditions are summarized in Table 1. For a net power of 248 MW, determine (a) the temperature T2 in℃, (b) the quality x3, (c) the temperature T4, in ℃, (d) the temperature T5, in 'C. in℃, (e) the temperature T6 in ℃, (f) the temperature T7in℃, (g) the fraction of the total flow not entering the second turbine y, (h) thermal efficiency η, and (i) the mass flow rate of water m, in ton/hr. (36%)

2. A closed and rigid vessel containing air-water vapor mixture undergoes a cooling process with the volume of 2.172 m3, Fig.2. The operation conditions are summarized in Table 2. The dew point temperature of the initial state is 99.63℃. Air behaviors as an ideal gas with specific heat ratio of 1.4. Determine (a) the initial temperature of mixture Ti, in℃, (b) the initial pressure of mixture p1, in bar, (c) the mass of vapor, in kg, (d) the mass of dry air, in kg, (e) the temperature of mixture T2 when water vapor starts to condensate, in ℃, (D) the pressure of the mixture P2, in bar, as the mixture temperature reaches T2, (g) the heat transfer during the cooling process, in kJ, (h) the entropy production during the cooling process, in kJ/K, if the vessel boundary always keeps at a constant temperature of T2. (32%)

(a) Tds = du + pdo and Tds = dh -vdp

(c) For an isentropic process,

(d) The thermal eficiency of a cold air-standard Otto cycle with the compression ratio r where its processes are modeled by a closed simple compressible system.

110年 - 110 國立臺灣大學_碩士班招生考試_工程科學及海洋工程學研究所甲組:熱工學#101265