The angle of the tilt of the pipe. Angle of the tilt is as follows: O = 24.99°=0.4362 rad. L = 2.13m SG of oil = 0.8 SG of water = 1.0 Height of the oil, = 50cm Height of the Water, = 50CM Lets assume, The bottom line as reference line, Point 1 lies at bottom line in the tank, °Cw = density of water = 997 kg/m 3 °Co = density of oil, H = vertical height of water level in the tube = Lsin θ g = acceleration due to gravity. So, the total pressure at point 1 will be as follows: P 1 = o * g * h o + w * g * h w P 1 = S o * w * g * h o + w * g * h w Putting the values: P 1 = 0.8 × 997 × 9.8 × 0.5 + 997 × 9.8 × 0.5 P 1 = 8793.54 N / m 2 …………. (1) Total pressure at bottom of the tank is the cause for the rise of the water level in the tube as shown in the given diagram: So, we have: - P 1 = w * g * H = w * g * Lsin θ = 997 ∗ 9.8 * 2.13 * sin θ …………. (2), From Eq n (1) & (2), we have: sin θ = 0.4225 θ = sin − 1 ( 0.4225 ) O = 24.99 degree=0.4362 rad.
The angle of the tilt of the pipe. Angle of the tilt is as follows: O = 24.99°=0.4362 rad. L = 2.13m SG of oil = 0.8 SG of water = 1.0 Height of the oil, = 50cm Height of the Water, = 50CM Lets assume, The bottom line as reference line, Point 1 lies at bottom line in the tank, °Cw = density of water = 997 kg/m 3 °Co = density of oil, H = vertical height of water level in the tube = Lsin θ g = acceleration due to gravity. So, the total pressure at point 1 will be as follows: P 1 = o * g * h o + w * g * h w P 1 = S o * w * g * h o + w * g * h w Putting the values: P 1 = 0.8 × 997 × 9.8 × 0.5 + 997 × 9.8 × 0.5 P 1 = 8793.54 N / m 2 …………. (1) Total pressure at bottom of the tank is the cause for the rise of the water level in the tube as shown in the given diagram: So, we have: - P 1 = w * g * H = w * g * Lsin θ = 997 ∗ 9.8 * 2.13 * sin θ …………. (2), From Eq n (1) & (2), we have: sin θ = 0.4225 θ = sin − 1 ( 0.4225 ) O = 24.99 degree=0.4362 rad.
Consider 0.65 kg of N2 at 300 K, 1 bar contained in a rigid tank connected by a valve to another rigid tank holding 0.3 kg of CO2 at 300 K, 1 bar. The valve is opened and gases are allowed to mix, achieving an equilibrium state at 290 K. Determine: (a) the volume of each tank, in m³. (b) the final pressure, in bar. (c) the magnitude of the heat transfer to or from the gases during the process, in kJ. (d) the entropy change of each gas and of the overall system, in kJ/K.
(Read Image) (Answer: ω = 1.10 rad/sec CW)
What is the configuration of the control loop if steam must be shut down in case of a problem? (I found this question on the internet and was wondering what the answer is)
A.Valve is fail open, PIC is direct-acting, TIC is reverse acting, and controller algorithm is feed-forwarding.B. Valve is fail open, PIC is reverse-acting, TIC is direct acting, and controller algorithm is cascade.C. Valve is fail closed, PIC is direct-acting, TIC is reverse acting, and controller algorithm is feed-forward.D. Valve is fail closed, PIC is reverse-acting, TIC is reverse acting, and controller algorithm is cascade.
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