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diff --git a/Power_Plant_Engineering_by_P._K._Nag/Ch3.ipynb b/Power_Plant_Engineering_by_P._K._Nag/Ch3.ipynb new file mode 100644 index 00000000..72e7fae0 --- /dev/null +++ b/Power_Plant_Engineering_by_P._K._Nag/Ch3.ipynb @@ -0,0 +1,529 @@ +{ + "cells": [ + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "# Chapter 3 : Combined Cycle Power Generation" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Ex: 3.1 Pg: 143" + ] + }, + { + "cell_type": "code", + "execution_count": 25, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + " (a) The amount of mercury circulated per kg of water is 7.4151 kg \n", + " (b) The efficiency of the combined cycle is 48.1 percent\n" + ] + } + ], + "source": [ + "from __future__ import division\n", + "#Input data\n", + "p=40#Pressure in bar\n", + "T1=400+273#Temperature in K\n", + "T2=40+273#Temperature in K\n", + "x=[0,10,515.5,72.23,363.0,0.1478,0.5167,80.9*10**-6,0.0333]#Property values from table p(bar),t(degree C), hf,hg(kJ/kg),sf,sg(kJ/kg.K),vf,vg(m**3/kg)\n", + "y=[0,0.2,277.3,38.35,336.55,0.0967,0.6385,77.4*10**-6,1.163]#Property values from table p(bar),t(degree C), hf,hg(kJ/kg),sf,sg(kJ/kg.K),vf,vg(m**3/kg)\n", + "\n", + "#Calculations\n", + "h1=3216#Enthalpy in kJ/kg\n", + "s1=6.7690#Entropy in kJ/kg.K\n", + "s2=s1#Entropy in kJ/kg.K\n", + "x2=(s2-0.5725)/(8.2570-0.5725)#Dryness fraction\n", + "h2=167.57+x2*2406.7#Enthalpy in kJ/kg\n", + "h3=167.57#Enthalpy in kJ/kg\n", + "h4=(167.57+p*100*1.008*10**-3)#Enthalpy in kJ/kg\n", + "h5=1087.31#Enthalpy in kJ/kg\n", + "h6=2801.4#Enthalpy in kJ/kg\n", + "ha=x[(4)]#Enthalpy in kJ/kg\n", + "sa=x[(6)]#Entropy in kJ/kg.K\n", + "sb=sa#Entropy in kJ/kg.K\n", + "xb=(sb-y[(5)])/(y[(6)]-y[(5)])#Dryness fraction\n", + "hb=(y[(3)]+xb*(y[(4)]-y[(3)]))#Enthalpy in kJ/kg\n", + "hc=y[(3)]#Enthalpy in kJ/kg\n", + "hd=hc#Enthalpy in kJ/kg\n", + "m=(h6-h5)/(hb-hc)#Mass of mercury circulated per kg of steam\n", + "Q1=m*(ha-hd)+(h1-h6)+(h5-h4)#Heat supplied in kJ/kg\n", + "Q2=(h2-h3)#Heat rejected in kJ/kg\n", + "nc=(1-(Q2/Q1))*100#Efficiency in percent\n", + "\n", + "#Output\n", + "print \" (a) The amount of mercury circulated per kg of water is %3.4f kg \\n (b) The efficiency of the combined cycle is %3.1f percent\"%(m,nc)" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Ex: 3.2 Pg: 145" + ] + }, + { + "cell_type": "code", + "execution_count": 24, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + "(a) Rate of heat transfer in the steam generator is 14.844 kW \n", + " (b) The net power output of the binary cycle is 4030 kW \n", + " (c) The rate of heat transfer to the industrial process is 5799 kW\n" + ] + } + ], + "source": [ + "from __future__ import division\n", + "#Input data\n", + "m=5#Mass flow rate in kg/s\n", + "p1=40#Pressure in bar\n", + "T1=440+273#Temperature in K\n", + "p2=1.5#Pressure in bar\n", + "p3=1#Pressure in bar\n", + "T3=60+273#Temperature in K\n", + "p4=16#Pressure in bar\n", + "T4=100+273#Temperature in K\n", + "p5=9#Pressure in bar\n", + "\n", + "#Calculations\n", + "h1=3307.1#Enthalpy in kJ/kg\n", + "s1=6.9041#Entropy in kJ/kg.K\n", + "s2=s1#Entropy in kJ/kg.K\n", + "h2=2570.8#Enthalpy in kJ/kg\n", + "h3=417.46#Enthalpy in kJ/kg\n", + "h6=(251.13+(1.0172*10**-3)*(p3-0.1994)*100)#Enthalpy in kJ/kg\n", + "m3=(m/2)#Mass flow rate in kg/s\n", + "m6=m3#Mass flow rate in kg/s\n", + "h4=(m3*h3+m6*h6)/m#Enthalpy in kJ/kg\n", + "h5=(h4+(1.0291*10**-3)*(p1-p3)*100)#Enthalpy in kJ/kg\n", + "ha=241.58#Enthalpy in kJ/kg\n", + "sa=0.7656#Entropy in kJ/kg.K\n", + "sb=sa#Entropy in kJ/kg.K\n", + "hb=229.43#Enthalpy in kJ/kg\n", + "hc=71.93#Enthalpy in kJ/kg\n", + "hd=hc+(0.7914*10**-3*(p4-p5)*100)#Enthalpy in kJ/kg\n", + "Q1=(m*(h1-h5))/1000#Heat supplied in kW\n", + "Wnets=(m*((h1-h2)-(h5-h4)))#Net workdone by steam in kW\n", + "mR12=(m3*(h2-h3))/(ha-hd)#Mass of R12 in kg/s\n", + "WnetR=(mR12*((ha-hb)-(hd-hc)))#Net workdone by R12 in kW\n", + "T=Wnets+WnetR#Total output in kW\n", + "Qh=(m6*(h2-h6))#Heat rejected in kW\n", + "\n", + "#Output\n", + "print \"(a) Rate of heat transfer in the steam generator is %3.3f kW \\n (b) The net power output of the binary cycle is %d kW \\n (c) The rate of heat transfer to the industrial process is %3.0f kW\"%(Q1,T,Qh)" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Ex: 3.3 Pg: 146" + ] + }, + { + "cell_type": "code", + "execution_count": 27, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + " (a) The flow rate of air is 396.33 kg/s and steam is 82.22 kg/s \n", + " (b) The power outputs of the gas turbine is 87.77 MW and steam turbine is 112.23 MW \n", + " (c) The thermal efficiency of the combined plant is 50 percent \n", + " (d) The air fuel ratio is 42.7\n" + ] + } + ], + "source": [ + "from numpy import mat\n", + "#Input data\n", + "rp=7.5#Pressure ratio \n", + "T1=15+273#Inlet air temperature in K\n", + "T3=750+273#Maximum temperature in K\n", + "T6=100+273#Temperature in K\n", + "p1=50#Pressure in bar\n", + "T7=600+273#Temperature in K\n", + "p2=0.1#Pressure in bar\n", + "P=200#Total power in MW\n", + "CV=43.3#calorific value in MJ/kg\n", + "cpg=1.11#Specific heat for gas in kJ/kg.K\n", + "g=1.33#Ratio of specific heats for gas\n", + "cpa=1.005#Specific heat for air in kJ/kg.K\n", + "g1=1.4#Ratio of specific heats for air\n", + "\n", + "#Calculations\n", + "T2=(T1*rp**((g1-1)/g1))#Temperature in K\n", + "T4=(T3/rp**((g-1)/g))#Temperature in K\n", + "ha=3670#Enthalpy in kJ/kg\n", + "hb=2305#Enthalpy in kJ/kg\n", + "hc=192#Enthalpy in kJ/kg\n", + "hd=hc#Enthalpy in kJ/kg\n", + "#ma*cpg*(T3-T6)=ms*(ha-hd)\n", + "#ma*cpg*(T3-T4)-ma*cpa*(T2-T1)+ms*(ha-hb)=P*1000\n", + "#Solving these two equations\n", + "A=mat([[cpg*(T3-T6), (hd-ha)],[cpg*(T3-T4)-cpa*(T2-T1), (ha-hb)]])#Coefficient matrix\n", + "B=mat([[0],[(P*10**3)]])#Constant matrix\n", + "X=(A**-1)*B#Variable matrix\n", + "\n", + "Wgt=(cpg*(T3-T4)-cpa*(T2-T1))*X[0]*10**-3#Net workdone by Gas turbine in MW\n", + "Wst=(P-Wgt)#Net workdone by steam turbine in MW\n", + "Q1=(X[0]*cpg*(T3-T2+T3-T4))#Heat supplied in MW\n", + "nth=(P/(Q1*10**-3))*100#Thermal efficiency in percent\n", + "af=(CV*10**3)/(cpg*(T3-T2+T3-T4))#Air fuel ratio\n", + "\n", + "#Output\n", + "print \" (a) The flow rate of air is %3.2f kg/s and steam is %3.2f kg/s \\n (b) The power outputs of the gas turbine is %3.2f MW and steam turbine is %3.2f MW \\n (c) The thermal efficiency of the combined plant is %3.0f percent \\n (d) The air fuel ratio is %3.1f\"%(X[0],X[1],Wgt,Wst,nth,af)" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Ex: 3.4 Pg: 148" + ] + }, + { + "cell_type": "code", + "execution_count": 29, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + "(a) Total power output is 82422.08 kW and overall efficiency is 41.54 percent lost heat coefficient is 0.351\n", + " Exergy efficiency is 40 percent \n", + "\n", + " Input is 212810 kW \n", + " Total Output is 82422 kW \n", + " Total losses is 123309 kW \n", + " Exergy outut + exergy destruction = 205731 kW which is 1.3 percent gretter than the exergy input\n" + ] + } + ], + "source": [ + "from __future__ import division\n", + "from math import log\n", + "#Input data\n", + "p1=1#Pressure in bar\n", + "T1=25+273#Temperature in K\n", + "rp=8#Pressure ratio of compressor\n", + "Tm=900+273#Maximum temperature in K\n", + "pd=3#pressure drop in combustion chamber in percent\n", + "nc=0.88#Efficiency of compressor\n", + "nt=0.88#Efficiency of turbine\n", + "CV=44.43#Calorific value of fuel in MJ/kg\n", + "cpa=1.006#Specific heat of air in kJ/kg.K\n", + "cpg=1.148#Specific heat of gas in kJ/kg.K\n", + "g1=1.333#Specific heat ratio of gas\n", + "g=1.4#Specific heat ratio of air\n", + "T3=425+273#Temperature in K\n", + "p2=40#Pressure in bar\n", + "p3=0.04#Condensor pressure in bar\n", + "Th=170.4+273#Temperature of feed water to the HRSG in K\n", + "nst=0.82#Efficiency of steam turbine\n", + "pdh=5#Pressure drop in HRSG in kPa\n", + "m=29.235#Steam flow rate in kg/s\n", + "A=1.0401#si=1.0401+0.1728*(h/c)\n", + "B=0.1728#si=1.0401+0.1728*(h/c)\n", + "\n", + "#Calculations\n", + "#Gas turbine plant\n", + "T2=(rp**((g-1)/(g*nt)))*T1#Temperature in K\n", + "#Combustor\n", + "pc=((pd/100)*rp)#Pressure loss in bar\n", + "pcx=(rp-pc)#Pressure in bar\n", + "f=((cpg*(Tm-T1))-(cpa*(T2-T1)))/((CV*10**3)-(cpa*(T2-T1)))#Fuel flow rate in kg/s\n", + "af=(1-f)/f#Air fuel ratio\n", + "#C8H18+12.5O2->8CO2+9H2O\n", + "afc=(12.5*32)/(0.232*114)#Air fuel ratio for stoichiometric combustion\n", + "ea=((af-afc)/afc)*100#Excess air in percent\n", + "#Gas turbine\n", + "p4=p1+0.05#Pressure in bar\n", + "T4=(Tm/(pcx/p4)**(((g1-1)*nt)/g1))#Temperature in K\n", + "#HRSG\n", + "T5=250+30#Temeprature in K\n", + "ha=3272#Enthalpy in kJ/kg\n", + "hf=1087.31#Enthalpy in kJ/kg\n", + "ws=(cpg*((T4-273)-T5))/(ha-hf)#Flow rate in kg/s\n", + "he=721.1#Enthalpy in kJ/kg\n", + "T6=(T4-273)-((ws*(ha-he))/cpg)#Temperature in degree C\n", + "#Power output\n", + "sa=6.853#Entropy in kJ/kg.K\n", + "sbs=sa#Entropy in kJ/kg.K\n", + "xbs=(sbs-0.4266)/8.052#Dryness fraction\n", + "hbs=(121.46+xbs*2432.9)#ENthalpy in kJ/kg\n", + "Wst=(m*(ha-hbs)*nst)#Workdone in kW\n", + "wg=(m/ws)#gas flow rate in kg/s\n", + "wa=(1-f)*wg#Air flow rate entering the compressor in kg/s\n", + "Wgt=(wg*cpg*(Tm-T4))-(wa*cpa*(T2-T1))#Power output of gas turbine in kW\n", + "TO=Wst+Wgt#Total power output in kW\n", + "wf1=(f*wa)#Fuel mass flow rate in kg/s\n", + "wf=4.466#Rounding off of wf1 for exact answers\n", + "no=(TO/(wf*(CV*10**3)))*100#Overall efficiency of the combined plant in percent\n", + "ns=((ha-hbs)/(ha-he))*nst#Efficiency of steam plant\n", + "ngtp=(Wgt/(wf*(CV*10**3)))#Efficiency of the GT plant\n", + "xL=((wg*cpg*(T6-(T1-273)))/(wf*(CV*10**3)))#Lost heat coefficient\n", + "nov=(ns+ngtp-ns*ngtp-ngtp*xL)#The overall efficiency\n", + "#Energy fluxes and irreversibilities\n", + "si=(A+B*((18*1)/(8*12)))#si for octane C8H18\n", + "dHo=(wf*CV*10**3)#Power in kW\n", + "dGo=(si*dHo)#Power in kW\n", + "TS=(dGo-dHo)#Power in kW\n", + "#Compressor\n", + "dS=(cpa*log(T2/T1))-(((cpa*(g-1))/g)*log(rp))#change in entropy in kJ/kg.K\n", + "Ic=(wa*T1*dS)#power in kW\n", + "Icx=((wg*T1*((cpg*log(Tm/T1))-(((cpg*(g1-1))/g1)*log(pcx))))-(wa*T1*((cpa*log(T2/T1))-(((cpa*(g-1))/g)*log(rp))))+TS)#Compressor in kW\n", + "Icg=(-cpg*log(Tm/T4))-(((cpg*(g1-1))/g1)*log(p4/pcx))#Difference in entropy in kJ/kg.K\n", + "IGT=(Icg*T1*wg)#Gas turbine in kW\n", + "se=2.046#Enntropy in kJ/kg.K\n", + "sae=(sa-se)#Difference in entropy in kJ/kg.K\n", + "s64=(cpg*log((T6+273)/T4))-(((cpg*(g1-1))/g1)*log(p4/p1))#Difference in entropy in kJ/kg.K\n", + "Ih=(T1*m*sae)+(wg*T1*s64)#For HRSG in kW\n", + "hb=(ha-(nst*(ha-hbs)))#Enthalpy in kJ/kg\n", + "xb=(hb-121.46)/2432.9#Dryness Fraction\n", + "sb=(0.4226+xb*8.052)#Entropy in kJ/kg.K\n", + "Ist=(m*(sb-sa)*T1)#For steam turbine in kW\n", + "Iexh=(wg*cpg*((T6-(T1-273))-(T1*log((T6+273)/T1))))#For exhaust in kW\n", + "Tl=Icx+Icg+IGT+Ih+Ist+Iexh#Exergy losses in kW\n", + "T=Tl+Wgt+Wst#Total exergy output and exergy destruction in kW\n", + "ee=((Wst+Wgt)/T)*100#Exergy efficiency in percent\n", + "\n", + "#Output\n", + "print \"(a) Total power output is %3.2f kW and overall efficiency is %3.2f percent lost heat coefficient is %3.3f\\n Exergy efficiency is %3.0f percent \\n\\n Input is %3.0f kW \\n Total Output is %3.0f kW \\n Total losses is %3.0f kW \\n Exergy outut + exergy destruction = %3.0f kW which is 1.3 percent gretter than the exergy input\"%(TO,no,xL,ee,dGo,(Wgt+Wst),Tl,T)" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Ex: 3.5 Pg: 154" + ] + }, + { + "cell_type": "code", + "execution_count": 30, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + "The overall efficiency of the combined cycle is 77.5 percent\n" + ] + } + ], + "source": [ + "#Input data\n", + "n1=0.5#Efficiency of mercury\n", + "n2=0.4#Efficiency of steam\n", + "n3=0.25#Efficiency of composite cycle\n", + "\n", + "#Calculations\n", + "n=(1-(1-n1)*(1-n2)*(1-n3))*100#Overall efficiency of the combined cycle in percent\n", + "\n", + "#Output\n", + "print \"The overall efficiency of the combined cycle is %3.1f percent\"%(n)" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Ex: 3.6 Pg: 156" + ] + }, + { + "cell_type": "code", + "execution_count": 17, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + "The overall efficiency of the combined plant is 58 percent\n" + ] + } + ], + "source": [ + "#Input data\n", + "z=30.0#Percentage of total energy of fuel\n", + "n=40.0#Cycle efficiency in percent\n", + "\n", + "#Calculations\n", + "on=((z/100)+(1-(z/100))*(n/100))*100#Overall efficiency in percent\n", + "\n", + "#Output\n", + "print \"The overall efficiency of the combined plant is %3.0f percent\"%(on)" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Ex: 3.7 Pg: 158" + ] + }, + { + "cell_type": "code", + "execution_count": 32, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + "(a) The output voltage is 1.1629 V \n", + " (b) The current density in the cathode is 4.239 A/cm**2 and anode is 1.092 A/cm**2 \n", + " (c) Power output per unit area is 3.66 W/cm**2 \n", + " (d) Thermal efficiency is 44.3 percent\n" + ] + } + ], + "source": [ + "from __future__ import division\n", + "from math import exp\n", + "#Input data\n", + "Tc=1250+273#Cathode temperature in K\n", + "Ta=500+273#Anode temperature in K\n", + "e=1.602*10**-19#Charge in coloumb\n", + "K=1.38*10**-23#Boltzmann constant in J/molecule.K\n", + "b=18#Constant\n", + "\n", + "#Calculations\n", + "Va=((b*K*Ta)/e)#Voltage of anode in V\n", + "Vc=((b*K*Tc)/e)#Voltage of cathode in V\n", + "Vo=Vc-Va#Output voltage in V\n", + "Ja=(120*Ta**2*exp(-b))#Current density in Cathode in A/cm**2\n", + "Jc=(120*Tc**2*exp(-b))#Current density in Anode in A/cm**2\n", + "P=Vo*(Jc-Ja)#Power output per unit area in /cm**2\n", + "nth=(((Tc-Ta)/Tc)*(b/(b+2)))*100#Thermal efficiency in percent\n", + "\n", + "#Output\n", + "print \"(a) The output voltage is %3.4f V \\n (b) The current density in the cathode is %3.3f A/cm**2 and anode is %3.3f A/cm**2 \\n (c) Power output per unit area is %3.2f W/cm**2 \\n (d) Thermal efficiency is %3.1f percent\"%(Vo,Jc,Ja,P,nth)" + ] + }, + { + "cell_type": "markdown", + "metadata": {}, + "source": [ + "## Ex: 3.8 Pg: 159" + ] + }, + { + "cell_type": "code", + "execution_count": 35, + "metadata": { + "collapsed": false + }, + "outputs": [ + { + "name": "stdout", + "output_type": "stream", + "text": [ + "(a) The thermal efficiency of thermocouple generator is 9.1 percent \n", + " (b) The number of thermo couples in series is 309 \n", + " (c) The lenght of the thermal elements is 0.519 cm and area is 43.48 cm**2 \n", + " (d) The output open-circuit voltage is 0.6 V \n", + " (e) At full load: \n", + " The heat input is 3.558 kW \n", + " The heat rejected is 3.236 kW \n", + " At no load: \n", + " The heat input is 2.093 kW \n", + " The heat rejected is 2.093 kW \n", + " (f) The overall efficiency of the combined thermo-electric steam power plant is 34.18 percent\n" + ] + } + ], + "source": [ + "from __future__ import division\n", + "from math import sqrt\n", + "#Input data\n", + "P=100#Power in kW\n", + "V=115#Voltage in V\n", + "To=1500#Outer temperature in K\n", + "Te=1000#Exit temperature in K\n", + "Ta=350#Ambient temperature in K\n", + "nth=30#Thermal efficiency in percent\n", + "nge=92#Generator efficiency in percent\n", + "#Properties of thermoelectrons \n", + "a=0.0012#At 1250K in V/K\n", + "kp=0.02#In W/cm.K\n", + "kn=0.03#In W/cm.K\n", + "dp=0.01#In ohm.cm\n", + "dn=0.012#In ohm.cm\n", + "J=20#Current density in A/cm**2\n", + "\n", + "#Calculations\n", + "zmax=(a**2/(sqrt(dp*kp)+sqrt(dn*kn))**2)#Maximum value of figure of merit in K**-1\n", + "mo=sqrt(1+(zmax*((To+Te)/2)))#Optimum value of the resistance ratio\n", + "nmax=(((To-Te)/To)*((mo-1)/(mo+(Te/To))))*100#Maximum thermal efficiency in percent\n", + "Vl=(a*(To-Te)*(mo/(mo+1)))#Voltage per couple in V\n", + "nc=(V/Vl)#Number of couples in series\n", + "L=((a*(To-Te))/((1+mo)*(dp+dn)))/J#Length in cm\n", + "A=((P*Te)/V)/J#Area in cm**2\n", + "I=(J*A)#Current in A\n", + "Vo=(a*(To-Te))#Voltage in V\n", + "Q1=((a*I*To)-((1/2)*(L/A)*I**2*(dp+dn))+((A/L)*(kp+kn)*(To-Te)))/1000#Heat input to the thermoelectric generator in kW\n", + "Q2=((a*I*Te)+((A/L)*(kp+kn)*(To-Te))+P)/1000#Heat rejected at full load in kW\n", + "Q1n=(((A/L)*(kp+kn)*(To-Te)))/1000#At no load heat input in kW\n", + "Q2n=Q1n#At no load heat rejected in kW\n", + "no=((nmax/100)+(1-(nmax/100))*(nth/100)*(nge/100))*100#Overall efficiency in percent\n", + "\n", + "#Output\n", + "print \"(a) The thermal efficiency of thermocouple generator is %3.1f percent \\n (b) The number of thermo couples in series is %d \\n (c) The lenght of the thermal elements is %3.3f cm and area is %3.2f cm**2 \\n (d) The output open-circuit voltage is %3.1f V \\n (e) At full load: \\n The heat input is %3.3f kW \\n The heat rejected is %3.3f kW \\n At no load: \\n The heat input is %3.3f kW \\n The heat rejected is %3.3f kW \\n (f) The overall efficiency of the combined thermo-electric steam power plant is %3.2f percent\"%(nmax,nc,L,A,Vo,Q1,Q2,Q1n,Q2n,no)" + ] + } + ], + "metadata": { + "kernelspec": { + "display_name": "Python 2", + "language": "python", + "name": "python2" + }, + "language_info": { + "codemirror_mode": { + "name": "ipython", + "version": 2 + }, + "file_extension": ".py", + "mimetype": "text/x-python", + "name": "python", + "nbconvert_exporter": "python", + "pygments_lexer": "ipython2", + "version": "2.7.9" + } + }, + "nbformat": 4, + "nbformat_minor": 0 +} |