Question

A dye suction device is arranged, as shown in Figure 3. The volumetric flow rate of air through the main pipe at circular cross-section (1) is given as Q = 0.0164 m³/s and the volumetric flow rate of the dye which is sucked from resorvoir A is given as Q = 0.00082 m³/s. The air and the dye flow is mixed in the main pipe and the mixture flow is then sprayed into a material to be dyed at cross-section (3). The pressure at point B where the sucked dye enters into main pipe is given as 0.95P2 and the diameter of the suction pipe which connects the reservoir A to the main pipe is D?= 1 cm. Determine the manometric (gauge) pressure of reservoir A, PA and the density of the mixture flow, pk at section (3). The fluids are incompressible and the friction can be neglected. The pressure at Sections (1) and (3) in the main pipe is assumed to be atmospheric except Section (2) and any variation of the velocity over the pipe cross section can be neglected. The diameter of the cross-section (1), D?=10 cm, the diameter of the cross-section (2), D2= 5 cm, the diameter of the cross-section (3), D3= 10 cm, the dye density, $\rho_b$ = 800 kg/m³ and air density, $\rho_{air}$= 1.2 kg/m³. The value of gravitational acceleration, g is 9.81 N/kg. (30 Points)

          A dye suction device is arranged, as shown in Figure 3. The volumetric flow rate of air through the main pipe at circular cross-section (1) is given as Q = 0.0164 m³/s and the volumetric flow rate of the dye which is sucked from resorvoir A is given as Q = 0.00082 m³/s. The air and the dye flow is mixed in the main pipe and the mixture flow is then sprayed into a material to be dyed at cross-section (3). The pressure at point B where the sucked dye enters into main pipe is given as 0.95P2 and the diameter of the suction pipe which connects the reservoir A to the main pipe is D?= 1 cm. Determine the manometric (gauge) pressure of reservoir A, PA and the density of the mixture flow, pk at section (3). The fluids are incompressible and the friction can be neglected. The pressure at Sections (1) and (3) in the main pipe is assumed to be atmospheric except Section (2) and any variation of the velocity over the pipe cross section can be neglected. The diameter of the cross-section (1), D?=10 cm, the diameter of the cross-section (2), D2= 5 cm, the diameter of the cross-section (3), D3= 10 cm, the dye density, $\rho_b$ = 800 kg/m³ and air density, $\rho_{air}$= 1.2 kg/m³. The value of gravitational acceleration, g is 9.81 N/kg. (30 Points)
        
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A dye suction device is arranged, as shown in Figure 3. The volumetric flow rate of air through the main pipe at circular cross-section (1) is given as Q = 0.0164 m³/s and the volumetric flow rate of the dye which is sucked from resorvoir A is given as Q = 0.00082 m³/s. The air and the dye flow is mixed in the main pipe and the mixture flow is then sprayed into a material to be dyed at cross-section (3). The pressure at point B where the sucked dye enters into main pipe is given as 0.95P2 and the diameter of the suction pipe which connects the reservoir A to the main pipe is D?= 1 cm. Determine the manometric (gauge) pressure of reservoir A, PA and the density of the mixture flow, pk at section (3). The fluids are incompressible and the friction can be neglected. The pressure at Sections (1) and (3) in the main pipe is assumed to be atmospheric except Section (2) and any variation of the velocity over the pipe cross section can be neglected. The diameter of the cross-section (1), D?=10 cm, the diameter of the cross-section (2), D2= 5 cm, the diameter of the cross-section (3), D3= 10 cm, the dye density,  = 800 kg/m³ and air density, ρair= 1.2 kg/m³. The value of gravitational acceleration, g is 9.81 N/kg. (30 Points)

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A dye suction device is arranged, as shown in Figure 3. The volumetric flow rate of air through the main pipe at circular cross-section (1) is given as Q = 0.0164 m^3/s and the volumetric flow rate of the dye which is sucked from reservoir A is given as Q = 0.00082 m^3/s. The air and the dye flow are mixed in the main pipe, and the mixture flow is then sprayed into a material to be dyed at cross-section (3). The pressure at point B, where the sucked dye enters into the main pipe, is given as 0.95P2, and the diameter of the suction pipe which connects reservoir A to the main pipe is D = 1 cm. Determine the manometric (gauge) pressure of reservoir A, Pa, and the density of the mixture flow, Pk, at section (3). The fluids are incompressible, and the friction can be neglected. The pressure at sections (1) and (3) in the main pipe is assumed to be atmospheric, except section (2), and any variation of the velocity over the pipe cross-section can be neglected. The diameter of the cross-section (1), D = 10 cm, the diameter of the cross-section (2), D2 = 5 cm, the diameter of the cross-section (3), D = 10 cm, the dye density, Pb = 800 kg/m^3, and air density, Pair = 1.2 kg/m^3. The value of gravitational acceleration, g, is 9.81 N/kg. (30 Points)
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Transcript

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00:01 So the solution is there is a water reserver so there is water reserver which is drawn like that so there is the pipe to be attached so there is the water reservoir and there is d2 there is a radius r2 and there is a radius r1 and the diameter t1 so the pressure at 1 so there is p1 plus rho water gh is equals to p atm so there is p1 is equals to p atm minus rho water gh so now for pressure pressure at 2 so there is p2 is equals to p2 is equals to p atm from volume flow rate correlation is v1 pi upon 4 d1 square equals to v2 pi upon 4 d2 square so there is v2 is equals to v1 multiplying by d1 upon d2 whole square this is my equation number 1 so the bernoulli theorem…
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