= 21 1.0 3) A diffuse surface at T = (600 + 200C)K.has the spectral, hemispherical emissivity illustrated. Determine the following: 0.8 2,-2 m 2 - 5 m (2) a. the total, hemispherical emissivity is ε = (+0.001) 0.4 b. the total emissive power is E = kW/m2 (+0.1%) 2 5 2. (um)
1.0 A diffuse surface at T = (9400) K. has the spectral, hemispherical emissivity illustrated. Determine the following: E2 0.8 2. = 2 um 12 = 5 um a. the total, hemispherical emissivity is ε = (+0.001) E, () E1 0.4 b. the total emissive power is E = kW/m² (+0.1%) 0 2 5 (um)
1.0 A diffuse surface at T = (2200) K. has the spectral, hemispherical emissivity illustrated. Determine the following: 0.8 21 = 2 pm 12 = 5 um a. the total, hemispherical emissivity is ε = (+0.001) E, () E1 0.4 b. the total emissive power is E = kW/m² (+ 0.1%) 0 2 5 (um)
1.0 3) A diffuse surface at T = (600 + 200)K.has the spectral, hemispherical emissivity illustrated. Determine the following: 0.8 2 - 2 2 - 5 3 a. the total, hemispherical emissivity is a = (+0.001) 0.4 b. the total emissive power is E = kW/m2 (+0.1%) 0 5 2. Gum
1.0 3) A diffuse surface at T = 1200K.has the spectral, hemispherical emissivity illustrated. Determine the following: o. E2 00 2. = 2 um 12 = 5 um 3 a. the total, hemispherical emissivity is a = (+0.001) E1 0.4 b. the total emissive power is E = kW/m² (+ 0.1%) 0 0 2 5 2. (um)
Enter your assigned value for Y and C: y = 47 5 = 8 (You will lose 1 pt. if missing). 2) Hot air enters a heat exchanger at 350°C and exits at (130+y). The heat extracted is used to boil (0.2 + 4/300) kg/s of 100°C water (from saturated liquid to saturated steam). The heat exchanger is a single-shell shell-and-tube heat exchanger with two tube passes. The overall heat transfer coefficient for the hot side is 240 W/(m2). Assume...
Enter your assigned value for Y and C: y = 47 5 = 8 (You will lose 1 pt. if missing). 2) Hot air enters a heat exchanger at 350°C and exits at (130+y). The heat extracted is used to boil (0.2 + 4/300) kg/s of 100°C water (from saturated liquid to saturated steam). The heat exchanger is a single-shell shell-and-tube heat exchanger with two tube passes. The overall heat transfer coefficient for the hot side is 240 W/(m2). Assume...
A small object with an opaque, diffuse surface at a temperature of 500 K is suspended in a large furnace with walls at 2000 K. Assume that the walls of the furnace provide a diffuse irradiation to the object at a blackbody temperature equal to the furnace wall temperature. The object’s surface has a spectral hemispherical emissivity and absorptivity as given below. (a) Determine the total emissivity and total absorptivity of the object’s surface. Partial Ans: ?=0.021 (b) Evaluate the...
Enter your assigned value for Y and C: W = 47 5 = 8 (You will lose 1 pt. if missing). 1) 2.5 m/s of air at 150°C is used to heat (0.25 +/250) kg/s of 20°C water. The heat exchanger is a finned-tube cross flow heat exchanger with both sides unmixed. The overall heat transfer coefficient associated with the hot side is 120 W/(m2). The hot- side area is 20 m². Assume a constant specific heat for air and...
Enter your assigned value for Y and C: W = 47 5 = 8 (You will lose 1 pt. if missing). 1) 2.5 m/s of air at 150°C is used to heat (0.25 +/250) kg/s of 20°C water. The heat exchanger is a finned-tube cross flow heat exchanger with both sides unmixed. The overall heat transfer coefficient associated with the hot side is 120 W/(m2). The hot- side area is 20 m². Assume a constant specific heat for air and...