diff options
Diffstat (limited to 'Practical_C_Programming/Chapter_2_3.ipynb')
| -rw-r--r-- | Practical_C_Programming/Chapter_2_3.ipynb | 32 |
1 files changed, 3 insertions, 29 deletions
diff --git a/Practical_C_Programming/Chapter_2_3.ipynb b/Practical_C_Programming/Chapter_2_3.ipynb index 36e059c9..d166fe06 100644 --- a/Practical_C_Programming/Chapter_2_3.ipynb +++ b/Practical_C_Programming/Chapter_2_3.ipynb @@ -1,7 +1,7 @@ { "metadata": { "name": "", - "signature": "sha256:1bdbe534af4c41744d0b20620d61031047f924bf7d6e0c91a540c9ad26997cbe" + "signature": "sha256:69b330a048da570dabedd3e4e55c16ec334a711968bec2056bd27ef834d8f06e" }, "nbformat": 3, "nbformat_minor": 0, @@ -30,7 +30,7 @@ "input": [ "\n", "\n", - "\t# a-oxygen b-stagnant water\n", + "\n", "T = 310 \t\t\t\t\t# [K]\n", "\t# Since the solubility of oxygen in water at 310 K is extremely low, we are dealing with \tdilute solutions\n", "k_L = 3.3*10**-5 \t\t\t\t# [coefficient based on the oxygen concentration \t\t\t\t\t\tdifference in the water, m/s]\n", @@ -254,8 +254,6 @@ "input": [ "\n", "\n", - "#Variable declaration\n", - "\t# a-UF6 b-air\n", "M_a = 352 \t\t\t\t\t# [molecular weight of UF6, gram/mole]\n", "M_b = 29 \t\t\t\t\t# [gram/mole]\n", "d = 0.01 \t\t\t\t\t# [diameter, m]\n", @@ -485,8 +483,7 @@ "\n", "\n", "import math\n", - "#Variable declaration\n", - "\t# a-liquid benzene b-nitrogen\n", + "\n", "T = 300 \t\t\t\t\t\t# [K]\n", "l = 3 \t\t\t\t\t\t\t# [length of vertical plate, m]\n", "b = 1.5 \t\t\t\t\t\t# [width of vertical plate, m]\n", @@ -556,9 +553,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Variable declaration\n", - "\t# a-water b-air\n", "dp1 = 10**-3 \t\t\t\t\t# [diameter of spherical drop of water, m]\n", "Tair = 323 \t\t\t\t\t# [K]\n", "P = 101.3 \t\t\t\t\t# [kPa]\n", @@ -672,11 +666,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Variable declaratiopn\n", - "\n", - "\t# Example 2.6 using equation 2.73\n", - "\t# Values of the dimensionless parameters calculated in Example 2.6\n", "Re = 1223 \t\t\t\t# [Renoylds Number]\n", "Sc = 0.905 \t\t\t\t# [Schmidt Number]\n", "c = 0.039 \t\t\t\t# [molar density, kg/cubic m]\n", @@ -725,10 +714,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Variable declaration\n", - "\n", - "# a-water b-air\n", "D = 25.4*10**-3 \t\t\t\t# [diameter of wetted wall tower, m]\n", "Gy = 10 \t\t\t\t\t# [mass velocity, kg/square m.s]\n", "T1 = 308 \t\t\t\t\t# [K]\n", @@ -811,10 +796,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "\n", - "#Variable declaration\n", - "\t# a-water b-dry air\n", "D = 25.4*10**-3 \t\t\t# [Internal diameter of tower, m]\n", "Z = 1.5 \t\t\t\t# [length of the wetted section, m]\n", "Gy = 10 \t\t\t\t# [mass velocity of air, kg/square m.s]\n", @@ -880,8 +861,6 @@ "collapsed": false, "input": [ "\n", - "#Variable declaration\n", - "\t# a-water b-dry air\n", "Gy = 10.0 \t\t\t\t# [kg/square m.s]\n", "dp = 3.5*10**-3 \t\t\t# [diameter of spherical glass beads, m]\n", "D = 25.4*10**-3 \t\t\t# [Internal diameter of tower, m]\n", @@ -967,11 +946,6 @@ "collapsed": false, "input": [ "\n", - "\n", - "#Variable declaration\n", - "\t# a-oxygen b-water\n", - "\t# To design the deaerator, We will use commercially available microporous polypropylene \thollow fibers in a module\n", - "\n", "m = 40000.0 \t\t\t\t\t# [kg/hr]\n", "Twater = 298 \t\t\t\t\t# [K]\n", "v = 0.1 \t\t\t\t\t# [superficial velocity, m/s]\n", |