Two incompressible fluids of densities p, and p2 are mixed in a square tank. Fluid-1 is pumped into the tank at the rate of 24 kg/s, and fluid-2 is pumped into the tank at the rate of 0.050 m³/s. After complete mixing, the mixture leaves the tank through pipe-3. You are given: p1 = 800 kg/m³, p2 = 1000 kg/m³, 0 = 60°, B = 0.9 m. a) Define your control volume, indicate control surfaces and number each active control surface. b) Determine the mixture density and the volume flowrate out of the tank if the mixture level in the tank is constant. c) Determine the mass and volume flowrates out of the tank if the mixture level in the tank is decreasing at a rate of 0.04 m/s. Note that the density of the mixture will| be the same as in part b. В В Mixture Fluid-1 Pipe-3 Fluid-2

Two incompressible fluids of densities p, and p2 are mixed in a square tank. Fluid-1 is pumped into the tank at the rate of 24 kg/s, and fluid-2 is pumped into the tank at the rate of 0.050 m³/s. After complete mixing, the mixture leaves the tank through pipe-3. You are given: p1 = 800 kg/m³, p2 = 1000 kg/m³, 0 = 60°, B = 0.9 m. a) Define your control volume, indicate control surfaces and number each active control surface. b) Determine the mixture density and the volume flowrate out of the tank if the mixture level in the tank is constant. c) Determine the mass and volume flowrates out of the tank if the mixture level in the tank is decreasing at a rate of 0.04 m/s. Note that the density of the mixture will| be the same as in part b. В В Mixture Fluid-1 Pipe-3 Fluid-2

Elements Of Electromagnetics

7th Edition

ISBN:9780190698614

Author:Sadiku, Matthew N. O.

Publisher:Sadiku, Matthew N. O.

ChapterMA: Math Assessment

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Chemical and Phase Equilibrium

Phase diagrams or equilibrium phase diagrams are the graphical representations that show the phase transformations of the constituting elements with respect to the pressure, temperature, and compositions. The diagrams show the conditions that limit the different phases, namely solid, liquid, and gas. The diagram can also be utilized to verify the relations between the state variables. Most of the phase diagrams are temperature-pressure phase diagrams, with the variable parameter as the composition. Usually other variables such as solubility and pressure parameters are not indicated in the phase diagram. For a one-component system (unary phase diagram), the phase diagram is generally a function of temperature and pressure as the state variables, or temperature and volume. However, for a binary system (two-phase) having two components, the phase diagram is a function of temperature and composition as the state variables only. Coexisting of the different phases of the constituting elements is indicated in the phase diagram. A ternary phase diagram can be characterized by consisting of three phases in equilibrium.

Question

Two incompressible fluids of densities p, and p2 are mixed in a square tank. Fluid-1 is pumped into the tank at the rate of 24 kg/s, and fluid-2 is pumped into the tank at
the rate of 0.050 m³/s. After complete mixing, the mixture leaves the tank through pipe-3. You are given: P1 = 800 kg/m³, P2 = 1000 kg/m³, 0 = 60°, B = 0.9 m.
a)
Define your control volume, indicate control surfaces and number each active control surface.
b)
Determine the mixture density and the volume flowrate out of the tank if the mixture level in the tank is constant.
c)
Determine the mass and volume flowrates out of the tank if the mixture level in the tank is decreasing at a rate of 0.04 m/s. Note that the density of the mixture will
be the same as in part b.
В
В
Mixture
Fluid-1
Pipe-3
Fluid-2

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