diff options
Diffstat (limited to 'mechanics_of_fluid/Chapter6-_1.ipynb')
| -rwxr-xr-x | mechanics_of_fluid/Chapter6-_1.ipynb | 342 |
1 files changed, 342 insertions, 0 deletions
diff --git a/mechanics_of_fluid/Chapter6-_1.ipynb b/mechanics_of_fluid/Chapter6-_1.ipynb new file mode 100755 index 00000000..40c8d053 --- /dev/null +++ b/mechanics_of_fluid/Chapter6-_1.ipynb @@ -0,0 +1,342 @@ +{
+ "metadata": {
+ "name": "",
+ "signature": "sha256:1481d1999e9016b92221ce8448ff32599db545d782d2bf3365587f6b7e7a231e"
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+ {
+ "cells": [
+ {
+ "cell_type": "heading",
+ "level": 1,
+ "metadata": {},
+ "source": [
+ "Chapter6- Laminar Flow Between Solid Boundaries"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Ex1-pg196"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "#calculate Reynolds number and Maximum velocity and Volumetric flow rate and \"Pressure gradient along the pipe\n",
+ "RD=0.83;\n",
+ "rho_w=1000.; ## density of water in kg/m^3\n",
+ "v=2.3; ## m/s\n",
+ "d=0.012; ## m\n",
+ "u=0.08; ## dynamic viscocity in kg/m/s\n",
+ "\n",
+ "rho_oil=RD*rho_w;\n",
+ "\n",
+ "Re=rho_oil*v*d/u;\n",
+ "print'%s %.1f %s'%(\"Reynolds number =\",Re,\"\")\n",
+ "\n",
+ "v_max=2*v;\n",
+ "print'%s %.1f %s'%(\"Maximum velocity =\",v_max,\"m/s^-1\")\n",
+ "\n",
+ "\n",
+ "Q=math.pi/4*d**2*v;\n",
+ "print'%s %.2f %s'%(\"Volumetric flow rate =\",Q,\"m^3/s^-1\")\n",
+ "\n",
+ "\n",
+ "p=-128.*Q*u/math.pi/d**4;\n",
+ "print'%s %.3f %s'%(\"Pressure gradient along the pipe = \",p,\"Pa/m^-1\")"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Reynolds number = 286.3 \n",
+ "Maximum velocity = 4.6 m/s^-1\n",
+ "Volumetric flow rate = 0.00 m^3/s^-1\n",
+ "Pressure gradient along the pipe = -40888.889 Pa/m^-1\n"
+ ]
+ }
+ ],
+ "prompt_number": 1
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Ex2-pg203"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "#calculate Rate at which oil must be supplied\n",
+ "c=0.001; ## m\n",
+ "p1=15*10**3; ## Pa\n",
+ "u=0.6; ## kg/m/s\n",
+ "R=6.; ## ratio of R2/R1\n",
+ "\n",
+ "Q=math.pi*c**3*p1/(6*u*math.log(R));\n",
+ "print'%s %.8f %s'%(\"Rate at which oil must be supplied =\",Q,\"m^3/s\")\n",
+ "#without round off error we cant get exact result \n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Rate at which oil must be supplied = 0.00000731 m^3/s\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Ex3-pg206"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "#calculate \"The load the pad will support and The rate at which oil must be supplied\n",
+ "F=6*10**3; ## Pa\n",
+ "b=0.12; ## m\n",
+ "\n",
+ "f=F*b;\n",
+ "print'%s %.f %s'%(\"The load the pad will support =\",f,\"N/m\")\n",
+ "\n",
+ "\n",
+ "dp=12*10**3; ## N/m^2\n",
+ "dx=0.12; ## m\n",
+ "c=0.00018; ## m\n",
+ "u=0.5; ## kg/m/s\n",
+ "V=5.; ## m/s\n",
+ "\n",
+ "q=(dp/dx)*c**3/12./u + V*c/2.;\n",
+ "print'%s %.5f %s'%(\"The rate at which oil must be supplied =\",q,\"m^2/s\")\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "The load the pad will support = 720 N/m\n",
+ "The rate at which oil must be supplied = 0.00045 m^2/s\n"
+ ]
+ }
+ ],
+ "prompt_number": 3
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Ex4-pg209"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "#calculate \"Velocity of the dashpot\n",
+ "d_p=0.05; ## diameter of piston in m\n",
+ "d_c=0.0504; ## diameter of cylinder in m\n",
+ "SG=0.87;\n",
+ "rho_w=1000.; ## kg/m^3\n",
+ "v=10**-4; ## m^2/s\n",
+ "dp=1.4*10**6; ## Pa\n",
+ "l=0.13; ## m\n",
+ "\n",
+ "c=(d_c-d_p)/2.; ## clearance\n",
+ "\n",
+ "u=SG*rho_w*v; ## Dynamice viscocity\n",
+ "\n",
+ "Vp=dp*c**3/(6.*u*l*(d_p/2.+c));\n",
+ "print'%s %.4f %s'%(\"Velocity of the dashpot =\",Vp,\"m/s\")\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Velocity of the dashpot = 0.0065 m/s\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Ex5-pg214"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "\n",
+ "#calculate Dynamic viscosity and Kinematic viscosity and Reynolds number of sphere and Reynolds number\n",
+ "\n",
+ "d=0.00475; ## m\n",
+ "g=9.81; ## m/s^2\n",
+ "rho_s=1151.; ## kg/m^3\n",
+ "rho=880.; ## kg/m^3\n",
+ "u=0.006; ## m/s\n",
+ "\n",
+ "F=math.pi/6.*d**3*g*(rho_s-rho);\n",
+ "\n",
+ "rat_d=0.25; ## ratio of d/D\n",
+ "rat_F=1.8; ## ratio of F/Fo\n",
+ "\n",
+ "dynamic=F/(1.8*3*math.pi*u*d);\n",
+ "\n",
+ "kinematic=dynamic/rho;\n",
+ "\n",
+ "print'%s %.3f %s'%(\"Dynamic viscosity = \",dynamic,\"kg/m/s\")\n",
+ "\n",
+ "\n",
+ "print'%s %.5f %s'%(\"Kinematic viscosity =\",kinematic,\"m^2/s\")\n",
+ "\n",
+ "\n",
+ "print(\"Reynolds number of sphere \")\n",
+ "\n",
+ "Re=rho*u*d/dynamic;\n",
+ "print'%s %.3f %s'%(\"Reynolds number =\",Re,\"\")\n",
+ "\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Dynamic viscosity = 0.309 kg/m/s\n",
+ "Kinematic viscosity = 0.00035 m^2/s\n",
+ "Reynolds number of sphere \n",
+ "Reynolds number = 0.081 \n"
+ ]
+ }
+ ],
+ "prompt_number": 6
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Ex6-pg218"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "#calculate viscosity of the liquid \n",
+ "D=0.120; ## m\n",
+ "h=0.08; ## m\n",
+ "c=0.001; ## m\n",
+ "t=0.01875; ## m\n",
+ "rev=65.; ## revolutions per min\n",
+ "T=4*10**-3; ## N.m\n",
+ "\n",
+ "K1=math.pi*h/4./c;\n",
+ "K2=math.pi/32./t;\n",
+ "\n",
+ "u=T/(rev*2*math.pi/60.)/(K1*D**3+K2*D**4);\n",
+ "print'%s %.4f %s'%(\"viscosity of the liquid =\",u,\"pa.s\")\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "viscosity of the liquid = 0.0054 pa.s\n"
+ ]
+ }
+ ],
+ "prompt_number": 7
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Ex7-pg229"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "import math\n",
+ "#calculate Volumetric flow rate of oil and The load supported by the bearing\n",
+ "V=10.; ## m/s\n",
+ "h1=0.0005; ## m\n",
+ "h2=0.00025; ## m\n",
+ "L=0.1; ## m\n",
+ "b=0.1; ## m\n",
+ "RD=0.87;\n",
+ "u=2*10**-4; ## m^2/s\n",
+ "rho_w=1000.; ## kg/m^3\n",
+ "\n",
+ "H=h1/h2;\n",
+ "\n",
+ "Q=V/2*(1+H**2)/(1+H**3)*b*h1;\n",
+ "print'%s %.5f %s'%(\"Volumetric flow rate of oil =\",Q,\"m^3/s\")\n",
+ "\n",
+ "\n",
+ "F=V/2.*(1.-(1.+H**2)/(1.+H**3))*12.*RD*rho_w*u/h1**2*L**2/4.*b;\n",
+ "print'%s %.1f %s'%(\"The load supported by the bearing =\",F,\"N\")\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Volumetric flow rate of oil = 0.00014 m^3/s\n",
+ "The load supported by the bearing = 4640.0 N\n"
+ ]
+ }
+ ],
+ "prompt_number": 8
+ }
+ ],
+ "metadata": {}
+ }
+ ]
+}
\ No newline at end of file |