diff options
Diffstat (limited to 'Basic_Mechanical_Engineering/bme2.ipynb')
| -rw-r--r-- | Basic_Mechanical_Engineering/bme2.ipynb | 39 |
1 files changed, 2 insertions, 37 deletions
diff --git a/Basic_Mechanical_Engineering/bme2.ipynb b/Basic_Mechanical_Engineering/bme2.ipynb index d16be4dc..07d17afc 100644 --- a/Basic_Mechanical_Engineering/bme2.ipynb +++ b/Basic_Mechanical_Engineering/bme2.ipynb @@ -1,7 +1,7 @@ { "metadata": { "name": "", - "signature": "sha256:eb480946d569a90f950fa22c2b37d79f68cd522d201043a9e36d8370900550dc" + "signature": "sha256:be9b81ec82ea0e8e81e59b4d7c97d91bf099bd45d69eea5f3a2ed8e0bbebe433" }, "nbformat": 3, "nbformat_minor": 0, @@ -29,8 +29,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input data\n", "h1=60\t\t#The heat transfer in the process in kJ\n", "h2=-8\t\t#The heat transfer in the process in kJ\n", "h3=-34\t\t#The heat transfer in the process in kJ\n", @@ -68,8 +66,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input data\n", "Q=-300\t\t#Heat transfer in the system consisting of the gas in kJ\n", "u=0\t\t#Internal energy is constant\n", "\n", @@ -142,8 +138,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input data\n", "h1=35\t\t#Enthalpy of water entering the boiler in kJ/kg\n", "h2=705\t\t#Enthalpy of steam leaving the boiler in kJ/kg\n", "C=0\t\t#Change in kinetic energy is neglected\n", @@ -181,8 +175,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input data\n", "Q=-170\t\t#Sum of all heat transfers per cycle in kJ\n", "N=100\t\t#Total number of cycles per min in cycles/min\n", "Q1=0\t\t#Heat developed in a-b process in kJ/min\n", @@ -244,8 +236,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input data\n", "Q1=50\t\t#Heat developed in the 1-2 process in kJ/kg\n", "U1=20\t\t#Change in energy in the 1-2 process in kJ/kg\n", "Q2=-30\t\t#Heat developed in the 2-3 process in kJ/kg\n", @@ -302,8 +292,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input data\n", "m=3.0\t\t#Mass of substance in the system in kg\n", "P1=500.0\t\t#Initial pressure of the system in kPa\n", "P2=100.0\t\t#Final pressure of the system in kPa\n", @@ -398,8 +386,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input data\n", "p1=170\t\t#Initial pressure of the fluid in kPa\n", "p2=400\t\t#Final pressure of the fluid in kPa\n", "v1=0.03\t\t#Initial volume in m**3\n", @@ -446,8 +432,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input data\n", "E1=4000\t\t#Enthalpy at entrance in kJ/Kg\n", "E2=4100\t\t#Enthalpy at exit in kJ/kg\n", "V1=50\t\t#Velocity at entrance in m/s\n", @@ -488,8 +472,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input data\n", "W=135\t\t#Work done by the system in kJ/kg\n", "V1=0.37\t\t#Specific volume of fluid at inlet in m**3/kg\n", "V2=0.62\t\t#Specific volume of fluid at outlet in m**3/kg\n", @@ -534,8 +516,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input data\n", "m=5\t\t#Rate of fluid flow in the system in kg/s\n", "P1=620\t\t#Pressure at the entrance in kPa\n", "P2=130\t\t#Pressure at the exit in kPa\n", @@ -584,8 +564,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input Data\n", "P1=100\t\t#Pressure at Inlet in kPa\n", "P2=500\t\t#Pressure at Exit in kPa\n", "V1=0.6\t\t#Specific volume at Inlet in m**3/kg\n", @@ -631,7 +609,7 @@ "cell_type": "code", "collapsed": false, "input": [ - "#Input data\n", + "\n", "m1=5000\t\t#Steam flow rate in kg/hr\n", "Q1=-250\t\t#Heat loss from the turbine insulation to surroundings in kj/min\n", "C1=40\t \t#Velocity of steam at entrance in m/s\n", @@ -674,9 +652,7 @@ "cell_type": "code", "collapsed": false, "input": [ - " \n", "\n", - "#Input data \n", "c1=16\t\t#Velocity of steam at entrance in m/s\n", "c2=37\t\t#Velocity of steam at exit in m/s\n", "h1=2990\t\t#Specific enthalpy of steam at entrance in kJ/kg\n", @@ -720,7 +696,6 @@ "collapsed": false, "input": [ "\n", - "#Input data\n", "p1=720\t\t#Pressure at the entrance in kPa\n", "t1=850\t\t#Temperature at the entrance in degree centigrade \n", "c1=160\t\t#Velocity of the gas at entrance in m/s\n", @@ -763,8 +738,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input data\n", "p=5000\t\t#Power output of an adiabatic steam turbine in kW\n", "p1=2000\t\t#Pressure at the inlet in kPa\n", "p2=0.15\t\t#Pressure at the exit in bar\n", @@ -815,8 +788,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input Data\n", "p1=1000.0\t\t#Pressure at the inlet in kPa\n", "t1=750.0\t\t#Temperature at the inlet in K\n", "c1=200.0\t\t#Velocity at the inlet in m/s\n", @@ -866,8 +837,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Input data\n", "c1=7\t\t #Velocity of air at entrance in m/s\n", "c2=5\t\t #Velocity of air at exit in m/s\n", "p1=100\t\t #Pressure at the entrance in kPa\n", @@ -915,9 +884,6 @@ "cell_type": "code", "collapsed": false, "input": [ - "\n", - "\n", - "#Input data\n", "h1=3000\t\t#Enthalpy of the fluid passing at inlet in kJ/kg\n", "h2=2757\t\t#Enthalpy of the fluid at the discharge in kJ/kg\n", "c1=60\t\t#Velocity of the fluid at inlet in m/s\n", @@ -966,7 +932,6 @@ "collapsed": false, "input": [ "\n", - "#Input data\n", "h1=3000\t\t#Specific enthalpy of steam at inlet in kJ/kg\n", "h2=2762\t\t#Specific enthalpy of steam at the outlet in kJ/kg\n", "v1=0.187\t\t#Specific volume of steam at inlet in m**3/kg\n", |