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-rwxr-xr-x746/CH8/EX8.01/8_01.sce15
-rwxr-xr-x746/CH8/EX8.02/8_02.sce15
-rwxr-xr-x746/CH8/EX8.04/8_04.sce12
-rwxr-xr-x746/CH8/EX8.05/8_05.sce10
-rwxr-xr-x746/CH8/EX8.06/8_06.sce13
-rwxr-xr-x746/CH8/EX8.07/8_07.sce10
-rwxr-xr-x746/CH8/EX8.08/8_08.sce25
-rwxr-xr-x746/CH8/EX8.09/8_09.sce20
-rwxr-xr-x746/CH8/EX8.10/8_10.sce20
-rwxr-xr-x746/CH8/EX8.11/8_11.sce26
10 files changed, 0 insertions, 166 deletions
diff --git a/746/CH8/EX8.01/8_01.sce b/746/CH8/EX8.01/8_01.sce
deleted file mode 100755
index cddb2de1f..000000000
--- a/746/CH8/EX8.01/8_01.sce
+++ /dev/null
@@ -1,15 +0,0 @@
-//Leakage flow rate//
-pathname=get_absolute_file_path('8.01.sce')
-filename=pathname+filesep()+'8.01-data.sci'
-exec(filename)
-//Leakage flow rate (in mm^3/sec):
-Q=%pi/12*D*a^3*(p1-p2)*10^3/u/L
-//Velocity of flow(in m/sec):
-V=Q/%pi/D/a/1000
-//Specific gravity of SAE 10W oil:
-SG=0.92;
-//Reynolds Number:
-Re=SG*dw*V*a/u/1000
-//As Re<1400, flow is laminar.
-printf("\n\nRESULTS\n\n")
-printf("\n\nLeakage flow rate: %.3f mm^3/sec\n\n",Q)
diff --git a/746/CH8/EX8.02/8_02.sce b/746/CH8/EX8.02/8_02.sce
deleted file mode 100755
index 904e37f22..000000000
--- a/746/CH8/EX8.02/8_02.sce
+++ /dev/null
@@ -1,15 +0,0 @@
-//Torque and power//
-pathname=get_absolute_file_path('8.02.sce')
-filename=pathname+filesep()+'8.02-data.sci'
-exec(filename)
-//Shear stres (in lbf/ft^2):
-Tyx=u*N*2*%pi/60*D/2/(a/2)
-//Torqe(in inches-lbf):
-T=%pi/2*Tyx*D^2*L/144
-//Power dissipated in the bearing(in hp):
-P=T*N/60*2*%pi/12/550
-//Reynolds number:
-Re=SG*p*N*2*%pi/60*1.5*a/2/u/144
-printf("\n\nRESULTS\n\n")
-printf("\n\nTorque: %.3f inches-lbf\n\n",T)
-printf("\n\nPower dissipated in the bearing: %.3f hp\n\n",P)
diff --git a/746/CH8/EX8.04/8_04.sce b/746/CH8/EX8.04/8_04.sce
deleted file mode 100755
index e65781809..000000000
--- a/746/CH8/EX8.04/8_04.sce
+++ /dev/null
@@ -1,12 +0,0 @@
-//Viscosity of fluid//
-pathname=get_absolute_file_path('8.04.sce')
-filename=pathname+filesep()+'8.04-data.sci'
-exec(filename)
-//Viscosity of the liquid(in N-s/m^2):
-u=%pi/128*p*1000*D^4/Q/L/1000
-//Velocity(in m/sec)
-V=Q/(%pi/4*D^2)/1000
-//Reynolds number:
-Re=d*V*D/u/1000
-printf("\n\nRESULTS\n\n")
-printf("\n\nViscosity of fluid %.3f N-s/m^2\n\n",u)
diff --git a/746/CH8/EX8.05/8_05.sce b/746/CH8/EX8.05/8_05.sce
deleted file mode 100755
index 7d3d6eac6..000000000
--- a/746/CH8/EX8.05/8_05.sce
+++ /dev/null
@@ -1,10 +0,0 @@
-//required//
-pathname=get_absolute_file_path('8.05.sce')
-filename=pathname+filesep()+'8.05-data.sci'
-exec(filename)
-//Reservoir depth required to maintain flow(in m):
-D1=8*Q^2/(%pi)^2/D^4/g*(f*L/D+K+1)
-//Reynolds number:
-Re=4*d*Q/((%pi)*u*D)
-printf("\n\nRESULTS\n\n")
-printf("\n\nReservoir depth required to maintain flow: %.3f m\n\n",D1)
diff --git a/746/CH8/EX8.06/8_06.sce b/746/CH8/EX8.06/8_06.sce
deleted file mode 100755
index 9a2b9934a..000000000
--- a/746/CH8/EX8.06/8_06.sce
+++ /dev/null
@@ -1,13 +0,0 @@
-//Maximum and power//
-pathname=get_absolute_file_path('8.06.sce')
-filename=pathname+filesep()+'8.06-data.sci'
-exec(filename)
-//Velocity of flow(in ft/sec):
-V=Q/24/3600/(%pi/4*(D/12)^2)*42/7.48
-//Maximum spacing(in ft):
-L=2/f*D/12*(p2-p1)/(SG*d)/V^2*144
-//Power needed at each pump(in hp):
-Win=1/Effp*V*%pi/4*(D/12)^2*(p2-p1)/550*144
-printf("\n\nRESULTS\n\n")
-printf("\n\nMaximum spacing: %.3f feet\n\n",L)
-printf("\n\nPower needed at each pump: %.3f hp\n\n",Win)
diff --git a/746/CH8/EX8.07/8_07.sce b/746/CH8/EX8.07/8_07.sce
deleted file mode 100755
index cc05e2cd7..000000000
--- a/746/CH8/EX8.07/8_07.sce
+++ /dev/null
@@ -1,10 +0,0 @@
-//Volume low//
-pathname=get_absolute_file_path('8.07.sce')
-filename=pathname+filesep()+'8.07-data.sci'
-exec(filename)
-//Velocity(in ft/sec):
-V2=sqrt(2*g*l/(f*((L+l)/D*12+8)+1))
-//Volume flow rate(in gpm):
-Q=V2*%pi*(D/12)^2/4*7.48*60
-printf("\n\nRESULTS\n\n")
-printf("\n\nVolume low rate: %.3f\n\n",Q)
diff --git a/746/CH8/EX8.08/8_08.sce b/746/CH8/EX8.08/8_08.sce
deleted file mode 100755
index 7d332823e..000000000
--- a/746/CH8/EX8.08/8_08.sce
+++ /dev/null
@@ -1,25 +0,0 @@
-//Minimum diameter//
-pathname=get_absolute_file_path('8.08.sce')
-filename=pathname+filesep()+'8.08-data.sci'
-exec(filename)
-//Value of dPmax(in psi):
-dPmax=p1-p2
-//Q in cubic feet/sec:
-Q1=1500/60/7.48;
-//Initially assume diameter to be 4inches:
-D=4;
-//Reynolds number:
-Re=4*Q1/%pi/v/D*12
-//For this value,
-f=0.012;
- dP=8*f*L*p*Q1^2/(%pi)^2/D^5*1728;
-while(dP>dPmax)
- dP=8*f*L*p*Q1^2/(%pi)^2/D^5*1728;
- if(dP<dPmax)
- break
- else
- D=D+1;
- end
-end
-printf("\n\nRESULTS\n\n")
-printf("Minimum diameter that can be used:%.1f inches\n\n",D)
diff --git a/746/CH8/EX8.09/8_09.sce b/746/CH8/EX8.09/8_09.sce
deleted file mode 100755
index f2de249c9..000000000
--- a/746/CH8/EX8.09/8_09.sce
+++ /dev/null
@@ -1,20 +0,0 @@
-//Loss Coefficient//
-pathname=get_absolute_file_path('8.09.sce')
-filename=pathname+filesep()+'8.09-data.sci'
-exec(filename)
-//Average velocity (in ft/s):
-V2=4/%pi*Q/D^2*144
-//Reynolds number:
-Re=V2*D/v/12
-//For this value,
-f=0.013;
-//Power law exponent:
-n=-1.7+1.8*log10(Re)
-//Value of V/U:
-v_u=2*n^2/(n+1)/(2*n+1)
-//Value of alpha:
-alpha=(1/v_u)^3*2*n^2/(3+n)/(3+2*n)
-//Loss Coefficient for a square edged entrance:
-K=2*g*h/V2^2-f*L/D*12-alpha;
-printf("\n\nRESULTS\n\n")
-printf("\n\nLoss Coefficient for a square edged entrance: %.3f \n\n",K)
diff --git a/746/CH8/EX8.10/8_10.sce b/746/CH8/EX8.10/8_10.sce
deleted file mode 100755
index 29c0d54dd..000000000
--- a/746/CH8/EX8.10/8_10.sce
+++ /dev/null
@@ -1,20 +0,0 @@
-//Volume and increase//
-pathname=get_absolute_file_path('8.10.sce')
-filename=pathname+filesep()+'8.10-data.sci'
-exec(filename)
-//Velocity V1(in m/s):
-V1=sqrt(2*g*z0/1.04)
-//Volume flow rate(in m^3/sec):
-Q=V1*%pi*D^2/4
-Kdiff=1-1/A_R^2-Cp
-//For 2nd case:
-//Velocity(in m/s):
-V1=sqrt(2*g*z0/0.59)
-//Volume flow rate(in m^3/s):
-Qd=V1*%pi*D^2/4
-//Increase in discharge after addition of diffuser is:
-dQ=(Qd-Q)/Q*100
-printf("\n\nRESULTS\n\n")
-printf("\n\nVolume flow rate in case1: %.3f m^3/sec\n\n",Q)
-printf("\n\nVolume flow rate in case 2: %.3f m^3/sec\n\n",Qd)
-printf("\n\nIncrease in discharge after addition of diffuser is: %.3f percent\n\n",dQ)
diff --git a/746/CH8/EX8.11/8_11.sce b/746/CH8/EX8.11/8_11.sce
deleted file mode 100755
index 1ac0346b6..000000000
--- a/746/CH8/EX8.11/8_11.sce
+++ /dev/null
@@ -1,26 +0,0 @@
-//Diameter and head//
-pathname=get_absolute_file_path('8.11.sce')
-filename=pathname+filesep()+'8.11-data.sci'
-exec(filename)
-
-//Value of K*B^2:
-K_B=Q/(%pi/4*D^2)*sqrt(0.5*d1/g/d2/h)
-//Reynods number:
-ReD1=4/%pi*Q/D/v
-//By trial and error method, the value of beta is fixed at:
-betta=0.66;
-//K is then:
-K=K_B/betta^2
-//Diameter of orifice plate(in m):
-Dt=betta*D
-//Value of p3-p2(in N/m^2):
-P1=d1*Q^2/(%pi/4*D^2)^2*(1/0.65/betta^2-1)
-//Value of p1-p2(in N/m^2):
-P2=d2*g*h
-//Head loss between sections 1 and 3(in N-m/kg):
-hLT=(P2-P1)/d1
-//Expressing the permanent pressure as a fractio of the meter differential:
-C=(P2-P1)/P2
-printf("\n\n\nRESULTS\n\n")
-printf("\n\nDiameter of the orifice: %.3f m\n\n",Dt)
-printf("\n\nHead loss between secions 1 and 3: %.3f N-m/kg\n\n",hLT)