1. A fire hose nozzle has an orifice diameter of 1inch. According to some fire c
ID: 1861568 • Letter: 1
Question
1. A fire hose nozzle has an orifice diameter of 1inch. According to some fire codes, the nozzle must be capable of delivering at least 300gal/min If the nozzle is attached to a 3-inch diameter hose, what pressure must be maintained just upstream of the nozzle to deliver this flow rate?
2. Kerosene having a specific weight of 50.0 lb/ft3 is flowing at 10 gallons per minute from a standard 1-inch Schedule 40 steel pipe to a standard 2-inch Schedule 40 steel pipe. Calculate the difference in pressure in the two pipes.
3. A 4-inch diameter pipe carries 300 gal/min of water at a pressure of 60 psi. Determine:
a) The pressure head in feet of water
b) The velocity head
c) The total head with reference to a datum plane 20 ft below the pipe.
4. 8. Oil with a specific gravity of 0.90 is flowing downward through the venturi meter. If the pressure difference on the gauges is 2 psi , the diameters or 2" and 1", and the ele-vation difference from station 1 - 2 is 1 foot, calculate the volume flow rate of oil.
Explanation / Answer
1.
300 gal / min = 40.1 ft^3 / min = 0.6684 ft^3 /s
V1 = Q / A1 = 0.6684 / (3.14/4*(3/12)^2) = 13.62 ft/s
V2 = Q / A2 = 0.6684 / (3.14/4*(1/12)^2) = 122.61 ft/s
P1 + 1/2*rho*V1^2 = P2 + 1/2*rho*V2^2...............ignoring change in height
P1 + 1/2*62.4*13.62^2 = 0 + 1/2*62.4*122.61^2
P1 = 463255.8 lb/(ft-s^2) = 463255.8 / 32.2 lb/ft^2 = 14386.8 lb/ft^2 = 14386.8/12^2 psi = 99.91 psi
2.
For 1" sch 40 pipe, we have d1 = 1.049 "
For 2" sch 40 pipe, we have d2 = 2.067"
10 gal/min = 1.337 ft^3 / min = 0.02228 ft3/s
V1 = Q / A1 = 0.02228 / (3.14/4*(1.049/12)^2) = 3.714 ft/s
V2 = Q / A2 = 0.02228 / (3.14/4*(2.067/12)^2) = 0.9566 ft/s
P1 + 1/2*rho*V1^2 = P2 + 1/2*rho*V2^2...............ignoring change in height
P2 - P1 = -1/2*(50/32.2)*(0.9566^2 - 3.714^2)
P2 - P1 = 10 lb/ft^2
3.
300 gal/min = 0.6684 ft3/s
V = Q / A = 0.6684 / (3.14/4*(4/12)^2) = 7.663 ft/s
a) Pressure head = P / rho = (60*12^2) / 62.4 = 138.46 ft
b) Velocity head = V^2 / (2g) = 7.663^2 / (2*32.2) = 0.9118 ft
c) Total head = 138.46 + 0.9118 + 20 = 159.37 ft
4.
P1 + 1/2*rho*V1^2 + rho*g*z1 = P2 + 1/2*rho*V2^2 + rho*g*z2
P1 - P2 = 2 psi = 2*12^2 lb/ft^2 = 288 lb / ft^2
z1 - z2 = 1 ft
288 + (0.9*62.4*1) = 1/2*(0.9*62.4/32.2)*(V2^2 - V1^2)
V2^2 - V1^2 = 394.66 ft^2 / s^2....................1
Also, A1*V1 = A2*V2
3.14/4*2^2 *V 1 = 3.14/4*1^2 *V2
V2 = 4*V1.....................2
Solving 1 and 2, we get V1 = 5.13 ft/s
Vol. flow rate = A1*V1 = 3.14/4*(2/12)^2 *5.13 = 0.111 ft^3/s = 50.19 gpm
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