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Diffstat (limited to '3751/CH12/EX12.3/Ex12_3.sce')
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diff --git a/3751/CH12/EX12.3/Ex12_3.sce b/3751/CH12/EX12.3/Ex12_3.sce new file mode 100644 index 000000000..8593ca45a --- /dev/null +++ b/3751/CH12/EX12.3/Ex12_3.sce @@ -0,0 +1,59 @@ +//Fluid Systems - By Shiv Kumar +//Chapter 12- Reciprocating Pumps +//Example 12.3 +//To Calculate The Maximum Speed at which pump may be run and Determine Resultant Suction Head at Begining, Middle and End of the Stroke. + + clc + clear + +//Given Data:- + D=150; //Diameter of Plunger, mm + L=250; //Stroke length, mm + l_s=10; //Length of Suction Pipe, m + d=75; //Diameter of Suction Pipe, mm + hs=4; //Suction Head, m of water + Ha=10.34; //Atmospheric Pressure, m of water + Habs=2.44; //Absolute Pressure Head, m of water + +//Data Used:- + g=9.81; //Acceleration due to gravity, m/s^2 + + +//Computations:- + Hv=Ha-Habs; //Vaccume Pressure, m of water + //For Maximum Resultant Suction Head, + Hs=Hv; + A=(%pi/4)*(D/1000)^2; //m^2 + a_s= (%pi/4)*(d/1000)^2; //m^2 + r=L/2000; //m + omega=sqrt((Hs-hs)*g*a_s/(l_s*A*r)); //radian/sec + N=60*omega/(2*%pi); //rpm + +//Result 1 + printf(" The Maximum Speed at which pump may be run, N=%.2f rpm \n",N) //The answer vary due to round off error + + //At Begining + Has=(l_s/g)*(A/a_s)*omega^2*r*cosd(0); //m + Hs=hs+Has; //Resultant Head at Begining of Stroke, m of water + +//Result 2 + printf(" Resultant Head at Begining of Stroke, Hs=%.1f m of water \n",Hs) + + + //At Middle + Has=(l_s/g)*(A/a_s)*omega^2*r*cosd(90); //m + Hs=hs+Has; //Resultant Head at Middle of Stroke (Has=0), m of water + +//Result 3 + printf(" Resultant Head at Middle of Stroke, Hs=%.f m of water \n",Hs) + + + //At the End + Has=(l_s/g)*(A/a_s)*omega^2*r*cosd(180); //m + Hs=hs+Has; //Resultant Head at End of Stroke, m of water + // Resultant Head at End of Stroke is not calculated and displayed as result in the textbook. + +//Result 4 + printf(" Resultant Head at End of Stroke, Hs=%.1f m of water \n ",Hs) + + |