diff options
author | Thomas Stephen Lee | 2015-09-04 22:04:10 +0530 |
---|---|---|
committer | Thomas Stephen Lee | 2015-09-04 22:04:10 +0530 |
commit | 41f1f72e9502f5c3de6ca16b303803dfcf1df594 (patch) | |
tree | f4bf726a3e3ce5d7d9ee3781cbacfe3116115a2c /Fundamentals_Of_Thermodynamics/Chapter2_6.ipynb | |
parent | 9c9779ba21b9bedde88e1e8216f9e3b4f8650b0e (diff) | |
download | Python-Textbook-Companions-41f1f72e9502f5c3de6ca16b303803dfcf1df594.tar.gz Python-Textbook-Companions-41f1f72e9502f5c3de6ca16b303803dfcf1df594.tar.bz2 Python-Textbook-Companions-41f1f72e9502f5c3de6ca16b303803dfcf1df594.zip |
add/remove/update books
Diffstat (limited to 'Fundamentals_Of_Thermodynamics/Chapter2_6.ipynb')
-rwxr-xr-x | Fundamentals_Of_Thermodynamics/Chapter2_6.ipynb | 379 |
1 files changed, 0 insertions, 379 deletions
diff --git a/Fundamentals_Of_Thermodynamics/Chapter2_6.ipynb b/Fundamentals_Of_Thermodynamics/Chapter2_6.ipynb deleted file mode 100755 index 08e192fe..00000000 --- a/Fundamentals_Of_Thermodynamics/Chapter2_6.ipynb +++ /dev/null @@ -1,379 +0,0 @@ -{
- "metadata": {
- "name": "",
- "signature": "sha256:96f5bd0fa542764d6a8f75d5a1a42e4b79791697476f4029d0fa0fea1de65bed"
- },
- "nbformat": 3,
- "nbformat_minor": 0,
- "worksheets": [
- {
- "cells": [
- {
- "cell_type": "heading",
- "level": 1,
- "metadata": {},
- "source": [
- "Chapter2:SOME CONCEPTS AND DEFINITIONS"
- ]
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Ex2.1:pg-19"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "#example 1\n",
- "#weight of a person\n",
- "\n",
- "\n",
- "m=1 #kg\n",
- "g=9.75 #acc.due to gravity in m/s^2\n",
- "F=m*g #weight of 1 kg mass in N\n",
- "print\"\\n hence,weight of person is\",round(F,2),\" N\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "\n",
- " hence,weight of person is 9.75 N\n"
- ]
- }
- ],
- "prompt_number": 20
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Ex2.1E:pg-20"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "#example 2\n",
- "#weight of a person\n",
- "\n",
- "\n",
- "m=1 #lbm\n",
- "g=32 #acc.due to gravity in ft/s^2\n",
- "F=m*g/32.174 #weight of 1 lbm mass in lbf\n",
- "print\"\\n hence,weight of person is\",round(F,4),\" lbf\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "\n",
- " hence,weight of person is 0.9946 lbf\n"
- ]
- }
- ],
- "prompt_number": 3
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Ex2.2:pg-24"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "#example 3\n",
- "#average volume and density\n",
- "\n",
- "Vliq=0.2 #volume of liquid in m^3\n",
- "dliq=997 #density of liquid in kg/m^3\n",
- "Vstone=0.12 #volume of stone in m^3\n",
- "Vsand=0.15 #volume of sand in m^3\n",
- "Vair=0.53 #vo;ume of air in m^3\n",
- "mliq=Vliq*dliq #mass of liquid in kg\n",
- "dstone=2750 #density of stone in kg/m^3\n",
- "dsand=1500 #density of sand in kg/m^3\n",
- "mstone=Vstone*dstone #volume of stone in m^3\n",
- "msand=Vsand*dsand #volume of sand in m^3\n",
- "Vtot=1 #total volume in m^3\n",
- "dair=1.1 #density of air in kg/m^3\n",
- "mair=Vair*dair #mass of air\n",
- "mtot=mair+msand+mliq+mstone #total mass in kg\n",
- "v=Vtot/mtot #specific volume in m^3/kg\n",
- "d=1/v #overall density in kg/m^3\n",
- "print\"\\n hence,average specific volume is\",round(v,6),\"m^3/kg\" \n",
- "print\"\\n and overall density is\", round(d),\"kg/m^3\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "\n",
- " hence,average specific volume is 0.001325 m^3/kg\n",
- "\n",
- " and overall density is 755.0 kg/m^3\n"
- ]
- }
- ],
- "prompt_number": 8
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Ex2.3:pg-26"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "#example 4\n",
- "#calculating the required force\n",
- "import math\n",
- "\n",
- "Dcyl=0.1 #cylinder diameter in m\n",
- "Drod=0.01 #rod diameter in m\n",
- "Acyl=math.pi*Dcyl**2/4 #cross sectional area of cylinder in m^2\n",
- "Arod=math.pi*Drod**2/4 #cross sectional area of rod in m^2\n",
- "Pcyl=250000 #inside hydaulic pressure in Pa\n",
- "Po=101000 #outside atmospheric pressure in kPa\n",
- "g=9.81 #acc. due to gravity in m/s^2\n",
- "mp=25 #mass of (rod+piston) in kg\n",
- "F=Pcyl*Acyl-Po*(Acyl-Arod)-mp*g #the force that rod can push within the upward direction in N\n",
- "print\"\\n hence,the force that rod can push within the upward direction is\",round(F,1),\" N\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "\n",
- " hence,the force that rod can push within the upward direction is 932.9 N\n"
- ]
- }
- ],
- "prompt_number": 2
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Ex2.4:pg-28"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "#example 5\n",
- "#Calculating atmospheric pressure \n",
- "\n",
- "dm=13534 #density of mercury in kg/m^3\n",
- "H=0.750 #height difference between two columns in metres\n",
- "g=9.80665 #acc. due to gravity in m/s^2\n",
- "Patm=dm*H*g/1000 #atmospheric pressure in kPa\n",
- "print\"\\n hence, atmospheric pressure is\",round(Patm,2),\"kPa\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "\n",
- " hence, atmospheric pressure is 99.54 kPa\n"
- ]
- }
- ],
- "prompt_number": 10
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Ex2.5:pg-28"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "#example 6\n",
- "#pressure inside vessel\n",
- "\n",
- "dm=13590 #density of mercury in kg/m^3\n",
- "H=0.24 #height difference between two columns in metres\n",
- "g=9.80665 #acc. due to gravity in m/s^2\n",
- "dP=dm*H*g #pressure difference in Pa\n",
- "Patm=13590*0.750*9.80665 #Atmospheric Pressure in Pa\n",
- "Pvessel=dP+Patm #Absolute Pressure inside vessel in Pa\n",
- "Pvessel=Pvessel/101325 #Absolute Pressure inside vessel in atm\n",
- "print\"\\n hence, the absolute pressure inside vessel is\",round(Pvessel,3),\"atm\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "\n",
- " hence, the absolute pressure inside vessel is 1.302 atm\n"
- ]
- }
- ],
- "prompt_number": 14
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Ex2.5E:pg-28"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "#example 7\n",
- "#pressure inside vessel\n",
- "\n",
- "dm=848 #density of mercury in lbm/ft^3\n",
- "H=9.5 #height difference between two columns in inches\n",
- "g=32.174 #acc. due to gravity in ft/s^2\n",
- "dP=dm*H*g #pressure difference in lbf/in^2\n",
- "Patm=848*9.5*32.174/(1728*32.174) #Atmospheric Pressure in lbf/in^2\n",
- "Pvessel=dP+Patm #Absolute Pressure inside vessel in lbf/in^2\n",
- "Pvessel=848*29.5*32.174/(1728*32.174)+Patm #Absolute Pressure inside vessel in lbf/in^2\n",
- "print\"\\n hence, the absolute pressure inside vessel is\",round(Pvessel,2),\"lbf/in^2\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "\n",
- " hence, the absolute pressure inside vessel is 19.14 lbf/in^2\n"
- ]
- }
- ],
- "prompt_number": 9
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Ex2.6:pg-29"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "#example 8\n",
- "#calculating pressure\n",
- "\n",
- "dg=750 #density of gaasoline in kg/m^3\n",
- "dR=1206 #density of R-134a in kg/m^3\n",
- "H=7.5 #height of storage tank in metres\n",
- "g=9.807 #acc. due to gravity in m/s^2\n",
- "dP1=dg*g*H/1000 #in kPa\n",
- "Ptop1=101 #atmospheric pressure in kPa\n",
- "P1=dP1+Ptop1\n",
- "print\"hence,pressure at the bottom of storage tank if fluid is gasoline is\",round(P1,1),\"kPa\" \n",
- "dP2=dR*g*H/1000 #in kPa\n",
- "Ptop2=1000 #top surface pressure in kPa\n",
- "P2=dP2+Ptop2\n",
- "print\"\\n hence, pressure at the bottom of storage tank if liquid is R-134a is\",round(P2),\"kPa\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "hence,pressure at the bottom of storage tank if fluid is gasoline is 156.2 kPa\n",
- "\n",
- " hence, pressure at the bottom of storage tank if liquid is R-134a is 1089.0 kPa\n"
- ]
- }
- ],
- "prompt_number": 17
- },
- {
- "cell_type": "heading",
- "level": 2,
- "metadata": {},
- "source": [
- "Ex2.7:pg-29"
- ]
- },
- {
- "cell_type": "code",
- "collapsed": false,
- "input": [
- "#example 9\n",
- "#calculating balancing force\n",
- "\n",
- "Po=100#Outside atmospheric pressure in kPa\n",
- "F1=25 #net force on the smallest piston in kN\n",
- "A1=0.01 #cross sectional area of lower piston in m^2\n",
- "P1=Po+F1/A1 #fluid pressure in kPa\n",
- "d=900 #density of fluid in kg/m^3\n",
- "g=9.81 #acc. due to gravity in m/s^2\n",
- "H=6 #height of second piston in comparison to first one in m\n",
- "P2=P1-d*g*H/1000 #pressure at higher elevation on piston 2 in kPa\n",
- "A2=0.05 #cross sectional area of higher piston in m^3\n",
- "F2=(P2-Po)*A2 #balancing force on second piston in kN\n",
- "print\"\\n hence, balancing force on second larger piston is\",round(F2,1),\"N\""
- ],
- "language": "python",
- "metadata": {},
- "outputs": [
- {
- "output_type": "stream",
- "stream": "stdout",
- "text": [
- "\n",
- " hence, balancing force on second larger piston is 122.4 N\n"
- ]
- }
- ],
- "prompt_number": 19
- }
- ],
- "metadata": {}
- }
- ]
-}
\ No newline at end of file |