summaryrefslogtreecommitdiff
path: root/Elements_of_Thermodynamics_and_heat_transfer/Chapter_15_1.ipynb
diff options
context:
space:
mode:
authorhardythe12015-06-03 15:27:17 +0530
committerhardythe12015-06-03 15:27:17 +0530
commitdf60071cf1d1c18822d34f943ab8f412a8946b69 (patch)
treeab059cf19bad4a1233a464ccf5d72cf8b3fb323c /Elements_of_Thermodynamics_and_heat_transfer/Chapter_15_1.ipynb
parentfba055ce5aa0955e22bac2413c33493b10ae6532 (diff)
downloadPython-Textbook-Companions-df60071cf1d1c18822d34f943ab8f412a8946b69.tar.gz
Python-Textbook-Companions-df60071cf1d1c18822d34f943ab8f412a8946b69.tar.bz2
Python-Textbook-Companions-df60071cf1d1c18822d34f943ab8f412a8946b69.zip
add books
Diffstat (limited to 'Elements_of_Thermodynamics_and_heat_transfer/Chapter_15_1.ipynb')
-rwxr-xr-xElements_of_Thermodynamics_and_heat_transfer/Chapter_15_1.ipynb291
1 files changed, 291 insertions, 0 deletions
diff --git a/Elements_of_Thermodynamics_and_heat_transfer/Chapter_15_1.ipynb b/Elements_of_Thermodynamics_and_heat_transfer/Chapter_15_1.ipynb
new file mode 100755
index 00000000..5c710163
--- /dev/null
+++ b/Elements_of_Thermodynamics_and_heat_transfer/Chapter_15_1.ipynb
@@ -0,0 +1,291 @@
+{
+ "metadata": {
+ "name": "",
+ "signature": "sha256:d49c3ebbe462c89b25518f64eebe9040738bf2ef82ee8e4dec85ee0229afc06b"
+ },
+ "nbformat": 3,
+ "nbformat_minor": 0,
+ "worksheets": [
+ {
+ "cells": [
+ {
+ "cell_type": "heading",
+ "level": 1,
+ "metadata": {},
+ "source": [
+ "Chapter 15 - Vapor cycles and processes"
+ ]
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Example 1 - Pg 276"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "#calculate the Thermal efficiency and Furnace efficiency\n",
+ "#Initialization of variables\n",
+ "p1=600. #psia\n",
+ "p2=0.2563 #psia\n",
+ "t1=486.21 #F\n",
+ "t2=60. #F\n",
+ "fur=0.75\n",
+ "#calculations\n",
+ "print '%s' %(\"from steam tables,\")\n",
+ "h1=1203.2\n",
+ "hf1=471.6\n",
+ "hfg1=731.6\n",
+ "h2=1088\n",
+ "hf2=28.06\n",
+ "hfg2=1059.9\n",
+ "s1=1.4454\n",
+ "sf1=0.6720\n",
+ "sfg1=0.7734\n",
+ "s2=2.0948\n",
+ "sf2=0.0555\n",
+ "sfg2=2.0393\n",
+ "xd=(s1-sf2)/sfg2\n",
+ "hd=hf2+xd*hfg2\n",
+ "xa=0.3023\n",
+ "ha=hf2+xa*hfg2\n",
+ "wbc=0\n",
+ "wda=0\n",
+ "wcd=h1-hd\n",
+ "wab=ha-hf1\n",
+ "W=wab+wcd+wbc+wda\n",
+ "Wrev=hfg1- (t2+459.7)*sfg1\n",
+ "etat=(t1-t2)/(t1+459.7)*100\n",
+ "eta=fur*etat\n",
+ "#results\n",
+ "print '%s %d %s' %(\"Thermal efficiency =\",etat,\"percent\")\n",
+ "print '%s %.1f %s' %(\"\\n Furnace efficiency =\",eta,\" percent\")\n",
+ "\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "from steam tables,\n",
+ "Thermal efficiency = 45 percent\n",
+ "\n",
+ " Furnace efficiency = 33.8 percent\n"
+ ]
+ }
+ ],
+ "prompt_number": 1
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Example 2 - Pg 277"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "#calculate the Thermal and Overall efficiency\n",
+ "#Initialization of variables\n",
+ "dhab=-123.1\n",
+ "etac=0.5\n",
+ "ha=348.5\n",
+ "etaf=0.75\n",
+ "eta=0.85\n",
+ "hf=471.6\n",
+ "hfg=731.6\n",
+ "hc=1203.2\n",
+ "dhcd=452.7\n",
+ "#calculations\n",
+ "dwabs=dhab/etac\n",
+ "hbd=ha-dwabs\n",
+ "dwcds=dhcd*eta\n",
+ "dqa=hc-hbd\n",
+ "etat=(dwcds+dwabs)/dqa*100.\n",
+ "eta=etat*etaf\n",
+ "#results\n",
+ "print '%s %.1f %s' %(\"Thermal efficiency =\",etat,\" percent\")\n",
+ "print '%s %.1f %s' %(\"\\n Overall efficiency = \",eta,\" percent\")\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Thermal efficiency = 22.8 percent\n",
+ "\n",
+ " Overall efficiency = 17.1 percent\n"
+ ]
+ }
+ ],
+ "prompt_number": 2
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Example 3 - Pg 277"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "#calculate the Thermal and Overall efficiency\n",
+ "#Initialization of variables\n",
+ "t=60 #F\n",
+ "J=778.16\n",
+ "p1=600 #psia\n",
+ "p2=0.2563 #psia\n",
+ "etaf=0.85 \n",
+ "#calculations\n",
+ "print '%s' %(\"From steam tables,\")\n",
+ "vf=0.01604 #ft^3/lbm\n",
+ "dw=-vf*(p1-p2)*144/J\n",
+ "ha=28.06 #Btu/lbm\n",
+ "hb=29.84 #Btu/lbm\n",
+ "hd=1203.2 #Btu/lbm\n",
+ "he=750.5 #Btu/lbm\n",
+ "dqa=hd-hb\n",
+ "dqr=ha-he\n",
+ "dw=dqa+dqr\n",
+ "dwturb=hd-he\n",
+ "dwpump=ha-hb\n",
+ "etat=dw/dqa*100.\n",
+ "eta=etat*etaf\n",
+ "#results\n",
+ "print '%s %.1f %s' %(\"Thermal efficiency =\",etat,\" percent\")\n",
+ "print '%s %.1f %s' %(\"\\n Overall efficiency =\",eta,\"percent\")\n",
+ " \n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "From steam tables,\n",
+ "Thermal efficiency = 38.4 percent\n",
+ "\n",
+ " Overall efficiency = 32.7 percent\n"
+ ]
+ }
+ ],
+ "prompt_number": 3
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Example 4 - Pg 278"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "#calculate the Thermal and Overall efficiency\n",
+ "#Initialization of variables\n",
+ "dhab=-1.78\n",
+ "etac=0.5\n",
+ "ha=28.06\n",
+ "eta=0.85\n",
+ "hf=471.6\n",
+ "hfg=731.6\n",
+ "hd=1203.2\n",
+ "dhcd=452.7\n",
+ "#calculations\n",
+ "dwabs=dhab/etac\n",
+ "hbd=ha-dwabs\n",
+ "dwcds=dhcd*eta\n",
+ "dqa=hd-hbd\n",
+ "etat=(dwcds+dwabs)/dqa*100.\n",
+ "eta=etat*eta\n",
+ "#results\n",
+ "print '%s %.1f %s' %(\"Thermal efficiency =\",etat,\"percent\")\n",
+ "print '%s %.1f %s' %(\"\\n Overall efficiency =\",eta,\"percent\")\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "Thermal efficiency = 32.5 percent\n",
+ "\n",
+ " Overall efficiency = 27.7 percent\n"
+ ]
+ }
+ ],
+ "prompt_number": 4
+ },
+ {
+ "cell_type": "heading",
+ "level": 2,
+ "metadata": {},
+ "source": [
+ "Example 5 - Pg 287"
+ ]
+ },
+ {
+ "cell_type": "code",
+ "collapsed": false,
+ "input": [
+ "#calculate the thermal efficiency\n",
+ "#Initialization of variables\n",
+ "p2=600 #psia\n",
+ "p1=44 #psia\n",
+ "te=486.21 #F\n",
+ "tb=273.1 #F\n",
+ "J=778.16\n",
+ "p3=0.25 #psia\n",
+ "#calculations\n",
+ "hc=241.9\n",
+ "hj=834.6\n",
+ "y=1-0.805\n",
+ "v1=0.0172\n",
+ "v2=0.016\n",
+ "ha=28.06\n",
+ "hd=hc+v1*(p2-p1)*144/J\n",
+ "hb=ha+v2*(p1-p3)*144/J\n",
+ "hh=1374\n",
+ "Qa=hh-hd\n",
+ "Qr=(ha-hj)*(1-y)\n",
+ "etat=(Qa+Qr)/Qa*100.\n",
+ "#results\n",
+ "print '%s %.1f %s' %(\"thermal efficiency =\",etat,\"percent\")\n",
+ "\n"
+ ],
+ "language": "python",
+ "metadata": {},
+ "outputs": [
+ {
+ "output_type": "stream",
+ "stream": "stdout",
+ "text": [
+ "thermal efficiency = 42.6 percent\n"
+ ]
+ }
+ ],
+ "prompt_number": 5
+ }
+ ],
+ "metadata": {}
+ }
+ ]
+} \ No newline at end of file