Pn = P. (1 +r) mWDn = Pn x Cn x fn + WDT(n)P = 0.5CpAppu,3r= 1+ 0.5 (a x b x h)TY UTM%RCo-CtTMx 100%CoAH, (R, + R,), AH, (R, +R,)¸ AH, (R; + R,UTMR =%DHH 2HDetention timeDynamic Viscosityutes1.14 x 10 N/mt P.-P.(1+r)" WD. = P.x C.x.+ WDP-0SCoApuA 60 MLD water treatment plant has 4 mechanical flocculators. The design criteria for each flocculator are asfollows:P-GuVr-I+0.5 (ax b x h)%R =x 100%AH, (R, +R,) AH, (R, +R,) AH, (R, +R, )R, =Number of paddlesNumber of plates per paddleArea of each plateCoefficient of dragRelative velocity of paddleDetention time4H24Q Zoom0.6 m?!!1.8%3D0.55 m/s%3D25 minutes%3DDynamic ViscosityDensity of water1.14 x 10 3 Ns/m²1000 kg/m3Compute the power required for the tank.A1437 WB90 W4 752 WD2614 W

P.-P.(1+1)" wD.P.C WD A 60 MLD water treatment plant has 4 mechanical flocculators. The design criteria for each flocculator are a follows: P-GV r-+05 (axb x h) R x 100% AH, (R, +R,) AH, (R, +R,) AH, (R, + R,) H 2 Number of paddles Number of plates per paddle Area of each plate Coefficient of drag Relative velocity of paddle Detention time 4 %3D R, = H 2 4 %3D Q Zoom 0.6 m2 %3D 1.8 %3D 0.55 m/s %3D 25 minutes %3D Dynamic Viscosity Density of water 1.14 x 10 3 Ns/m2 1000 kg/m3 %3D Compute the power required for the tank. A 1437 W 90 W 4 752 W 2614 W

P.-P.(1+1)" wD.P.C WD A 60 MLD water treatment plant has 4 mechanical flocculators. The design criteria for each flocculator are a follows: P-GV r-+05 (axb x h) R x 100% AH, (R, +R,) AH, (R, +R,) AH, (R, + R,) H 2 Number of paddles Number of plates per paddle Area of each plate Coefficient of drag Relative velocity of paddle Detention time 4 %3D R, = H 2 4 %3D Q Zoom 0.6 m2 %3D 1.8 %3D 0.55 m/s %3D 25 minutes %3D Dynamic Viscosity Density of water 1.14 x 10 3 Ns/m2 1000 kg/m3 %3D Compute the power required for the tank. A 1437 W 90 W 4 752 W 2614 W

Structural Analysis

6th Edition

ISBN:9781337630931

Author:KASSIMALI, Aslam.

Publisher:KASSIMALI, Aslam.

Chapter2: Loads On Structures

Section: Chapter Questions

Problem 1P

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A 4m Oil (0.90) 3.75 mm B Mercury (13.57) This vertical pipeline with attached gage and manometer contains oil and mercury as shown. The manometer is open to the atmosphere. There is no flow in the pipe. Express the pressure reading at A in bar. Do not write the unit. You will only input the numerical answer in the space provided. Unit of the Correct Answer: bar Decimal Places required in the final answer: 3
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Part d
H= Ht= Nf= Nd= find: - a) total discharge, b) P.W.P.. at A anc c) head to satisfy f Q=k - H - L Nd Q= ic F.S. G,-1 H/ Ah /Nd i = %3D 1+e AL ic= ie= FS= h (ooint= Ht - Na(point)"Ah h, (point) = h, (point) he (point) u or P.W.P. (ooint= h, (point) Yw Ipoint he ht hp PWP a b cl cm cr 1B, actor of safety equal to 2 against boiling. y= 19 kN/m3 k= 0.001 G= 2 r 04 k6.0 m/day bld impermeable layer 10 15 20
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MY REGISTRATION NO IS 5350
Design Characteristics Binch Sch 40 Steel pips hug ht Twenty feet) 90⁰ 40 7 a pump and for the 20 Standard elbow the various pump IZA Specity System shown below Hinch sch 40 steel pipes. ✓ B 1² iioft "PB = Hopsig =1759pm Length of Suction line = 25ft Length of discharge line = бодн Determine the NPSHR ? Show Calwlations Flowrate=
fl a f P₂/ Water system show in the figure below L = 160 m, d = 100 mm Given: hp = 10 Bar djet= 50 mm Find: Q, h at point 2 Draw H.G.L and find V of flow out of the Jet. WIL. ¥5 Water Pump 0 hp 1 L=160m d=100 mm √30 f = 0.02 Open Jet 2160m T Reference line لمود
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