import math
p1=15. #in bar
p2=1.013 #in bar
t1=283. #in K
t2=273. #in K
v1=10. #in l
v2=p1*v1*t2/(t1*p2);
print "volume of oxygen = %f liters"%(v2)
import math
nCO2 = 2./44; #moles of CO2
nO2 = 4./32; #moles of O2
nCH4 = 1.5/16; #moles of CH4
total_moles = nCO2+nO2+nCH4;
yCO2 = nCO2/total_moles;
yO2 = nO2/total_moles;
yCH4 = nCH4/total_moles;
print " Composition of mixture = CH4 = %f O2 = %f CO2 = %f "%(yCH4,yO2,yCO2)
pCO2=nCO2*8.314*273/(6*10**-3);
pO2=nO2*8.314*273/(6*10**-3);
pCH4=nCH4*8.314*273/(6*10**-3);
print "pressure of CH4 = %f kPa pressure of O2 = %f kPa pressure of CO2 =%f kPa"%(pCH4*10**-3,pO2*10**-3,pCO2*10**-3)
total_pressure=pCO2+pCH4+pO2;
print "total pressure = %f Kpa"%(total_pressure*10**-3)
import math
P=104.3 #total pressure in KPa
pH2O=2.3 #in KPa
pH2=P-pH2O; #in KPa
VH2=209*pH2*273/(293*101.3)
print "volume of hydrogen obtained = %f ml"%(VH2)
m=350/196.08*11.2 #mass of metal in grams
print "mass of metal equivalent to 11.2 litre/mol of hydrogen = %f gm"%(m)
import math
w=2 #in gm
m=0.287 #in gm
mNaCl=58.5/143.4*m;
print "mass of NaCl = %f gm"%(mNaCl )
percentage_NaCl=mNaCl/w*100;
print "amount of NaCl = %f"%(percentage_NaCl)
import math
w=4.73 #in gm5
VCO2=5.30 #in liters
weight_CO2=44/22.4*VCO2;
carbon_content=12./44*weight_CO2;
percentage_content=(carbon_content/w)*100;
print "percentage amount of carbon in sample = %f"%(percentage_content)
import math
volume_H2=0.5 #in m3
volume_CH4=0.35 #in m3
volume_CO=0.08 #in m3
volume_C2H4=0.02 #in m3
volume_oxygen=0.21 #in m3 in air
H2=0.5*volume_H2;
CH4=2*volume_CH4;
CO=0.5*volume_CO;
C2H4=3*volume_C2H4;
total_O2=H2+CH4+CO+C2H4;
oxygen_required=total_O2/volume_oxygen;
print "amount of oxygen required = %f cubic meter"%(oxygen_required)
import math
density_H2SO4 = 1.10 #in g/ml
mass_1 = 100*density_H2SO4; #mass of 100ml of 15% solution
mass_H2SO4 = 0.15*mass_1;
density_std = 1.84 #density of 96% sulphuric acid
mass_std = 0.96*density_std; #mass of H2SO4 in 1ml 96% H2SO4
volume_std = mass_H2SO4/mass_std; #volume of 96%H2SO4
mass_water = mass_1 - mass_H2SO4;
print "volume of 0.96 H2SO4 required = %f ml"%(volume_std)
print "mass of water required = %f g"%(mass_water)
import math
w_H2SO4=0.15 #in gm/1gm solution
density=1.10 #in gm/ml
m=density*1000; #mass per liter
weight=m*w_H2SO4; #H2SO4 per liter solution
molar_mass=98;
Molarity=weight/molar_mass;
print "Molarity = %f mol/l"%(Molarity)
equivalent_mass=49;
normality=weight/equivalent_mass;
print "Normality = %f N"%(normality)
molality=176.5/molar_mass;
print "Molality = %f"%(molality)
import math
molar_mass_BaCl2=208.3; #in gm
equivalent_H2SO4=0.144;
normality=equivalent_H2SO4*1000/28.8;
print "Normality = %f N"%(normality)
import math
solubility_70=30.2 #in gm/100gm
w_solute=solubility_70*350/130.2; #in gm
w_water=350-w_solute;
solubility_30=10.1 #in gm/100gm
precipitate=(solubility_70-solubility_30)*w_water/100
print "amount precipitated = %f gm"%(precipitate)
import math
absorbtion_coefficient=1.71 #in liters
molar_mass=44;
solubility=absorbtion_coefficient*molar_mass/22.4; #in gm
pressure=8/solubility*101.3;
print "pressure required = %f kPa"%(pressure)
import math
w_water=540. #in gm
w_glucose=36. #in gm
m_water=18.; #molar mass of water
m_glucose=180.; #molar mass of glucose
x=(w_water/m_water)/(w_water/m_water+w_glucose/m_glucose);
p=8.2*x;
depression=8.2-p;
print "depression in vapor pressure = %f Pa"%(depression*1000)
import math
w_glucose=9. #in gm
w_water=100. #in gm
E=0.52;
m=90/180.; #moles/1000gm water
delta_t=E*m;
boiling_point=100+delta_t;
print "boiling_point of water = %f degreeC"%(boiling_point)
import math
K=1.86;
c=15 #concentration of alcohol
delta_t=10.26;
m=delta_t/K; #molality
M=c/(m*85); #molar mass
print "molar mass = %f gm"%(M*1000)
density=0.97 #g/ml
cm=c*density/(M*100);
print "molar concentration of alcohol = %f moles/l"%(cm)
p=cm*8.314*293 #osmotic pressure
print "osmotic pressure = %f Mpa"%(p/1000)
import math
u_in = 0.575 #from the graph
u_s = 0.295 #in mPa-s
M_v = (u_in/(5.80*10**-5))**(1/0.72);
u_red = 0.628; #in dl/g
c = 0.40 #in g/dl
k = (u_red-u_in)/((u_in**2)*c);
print "k = %f Mv = %fu_in = %f dl/gm"%(k,M_v,u_in)
import math
C=54.5 #% of carbon
H2=9.1 #% of hydrogen
O2=36.4 #% of oxygen
x=C/12.; #number of carbon molecules
y=O2/16.; #number of oxygen molecules
z=H2/2. #number of hydrogen molecules
molar_mass=88.;
density=44.;
ratio=molar_mass/density;
x=ratio*2;
y=ratio*1;
z=ratio*4;
print "x = %f y = %f z = %f"%(x,y,z)
print "formula of butyric acid is = C4H8O2"
import math
C=93.75 #% of carbon
H2=6.25 #% of hydrogen
x=C/12 #number of carbon atoms
y=H2/2 #number of hydrogen atoms
molar_mass=64
density=4.41*29;
ratio=density/molar_mass;
x=round(ratio*5);
y=round(ratio*4);
print "x = %f y = %f"%(x,y)
print "formula of butyric acid is = C10H8"
import math
C=50.69 #% of carbon
H2=4.23 #% of hydrogen
O2=45.08 #% of oxygen
a=C/12; #number of carbon molecules
c=O2/16; #number of oxygen molecules
b=H2/2; #number of hydrogen molecules
molar_mass=71;
def f(m):
return (2.09*1000)/(60*m);
M=f((1.25/5.1));
print "actual molecular mass = %f"%(M)
ratio=M/molar_mass;
a=round(ratio*3);
b=round(ratio*3);
c=round(ratio*2);
print "a = %d, b = %d, c = %d"%(a,b,c)
print "M = %.1f g/mol"%M
print "formula of butyric acid is = C6H6O4"
import math
C=64.6 #% of carbon
H2=5.2 #% of hydrogen
O2=12.6 #% of oxygen
N2=8.8 #% of nitrogen
Fe=8.8 #% of iron
a=C/12; #number of carbon molecules
c=8.8/14; #number of nitrogen molecules
b=H2; #number of hydrogen molecules
d=O2/16; #number of oxygen molecules
e=Fe/56 #number of iron atoms
cm=243.4/(8.31*293) #concentration
molar_mass=63.3/cm;
print "a = %d, b = %d, c = %d, d = %d, e = %d"%(a*6.5,b*6.5,c*6.5,d*6.5,e*6.5)
print "formula of butyric acid is = C34H33N4O5Fe"
import math
E1=-0.25;
E2=0.80;
E3=0.34;
a=[E1,E2,E3];
sorted(a)
print "sorted potential in volts ="
print (a)
print ("E2>E3>E1")
print ("silver>copper>nickel")
import math
E0_Zn=-0.76;
E0_Pb=-0.13;
c_Zn=0.1;
c_Pb=0.02;
E_Zn=E0_Zn+(0.059/2)*math.log10(c_Zn);
E_Pb=E0_Pb+(0.059/2)*math.log10(c_Pb);
E=E_Pb-E_Zn;
print "emf of cell = %f V"%(E)
print "Since potential of lead is greater than that of zinc thus reduction will occur at\
lead electrode and oxidation will occur at zinc electrode"
import math
E0_Ag=0.80;
E0_AgNO3=0.80;
c_Ag=0.001;
c_AgNO3=0.1;
E_Ag=E0_Ag+(0.059)*math.log10(c_Ag);
E_AgNO3=E0_AgNO3+(0.059)*math.log10(c_AgNO3);
E=E_AgNO3-E_Ag;
print "emf of cell = %f V" %(E)
print "since E is positive, the left hand electrode will be anode and\
the electron will travel in the external circuit from the left hand to the right hand electrode"
import math
pH=12; #pH of solution
E_H2=0;
E2=-0.059*pH;
E=E_H2-E2;
print "EMF of cell = %f V"%(E)
import math
I=3 #in Ampere
t=900 #in s
m_eq=107.9 #in gm/mol
F=96500;
m=(I*t*m_eq)/F;
print "mass = %f gm"%(m)
import math
volume=10*10*0.005; #in cm3
mass=volume*8.9;
F=96500;
atomic_mass=58.7 #in amu
current=2.5 #in Ampere
charge=(8.9*F*2)/atomic_mass;
yield_=0.95;
actual_charge=charge/(yield_*3600);
t=actual_charge/current;
print "time required = %f hours"%(t)
m_MgSO4=90. #in ppm
MgSO4_parts=120.;
CaCO3_parts=100.;
hardness=(CaCO3_parts/MgSO4_parts)*m_MgSO4;
print "hardness of water = %f mg/l"%(hardness)
'''
calculate
i) the temporary and total hardness of the sample
ii) the amounts of lime and soda needed for softening of 1 l of the sample
'''
import math
m1 = 162. #mass of calcium bi carbonate in mg
m2 = 73. #mass of magnesium bi carbonate in mg
m3 = 136. # mass of calsium sulfate in mg
m4 = 95. # mass of magnesium cloride
m5 = 500. #mass of sodium cloride in mg
m6 = 50. # mass of potassium cloride in mg
content_1 = m1*100/m1; #content of calcium bi carbonate in mg
content_2 = m2*100/(2*m2); #content of magnesium bi carbonate in mg
content_3 = m3*100/m3; # content of calsium sufate in mg
content_4 = m4*100/m4; # content of magnesium cloride
temp_hardness = content_1 + content_2; #depends on bicarbonate only
total_hardness = content_1+content_2+content_3+content_4;
print "total hardness = %.0f mg/l temporary hardness = %.0f mg/l"%(temp_hardness,total_hardness)
wt_lime = (74./100)*(content_1+2*content_2+content_4);
actual_lime = wt_lime/0.85;
print "amount of lime required = %.1f mg/l"%(actual_lime)
soda_required = (106./100)*(content_1+content_4);
actual_soda = soda_required/0.98;
print "amount of soda required = %.1f mg/l"%(actual_soda)
volume_NaCl=50. #in l
c_NaCl=5000. #in mg/l
m=volume_NaCl*c_NaCl;
equivalent_NaCl=50/58.5;
hardness=equivalent_NaCl*m;
print "hardness of water = %f mg/l"%(hardness/1000.)
import math
m_benzene = 55. #in kg
m_toluene = 28. #in kg
m_xylene = 17. # in kg
mole_benzene = m_benzene/78.;
mole_toluene = m_toluene/92.;
mole_xylene = m_xylene/106.;
mole_total = mole_benzene+mole_toluene+mole_xylene;
x_benzene = mole_benzene/mole_total;
x_toluene = mole_toluene/mole_total;
x_xylene = mole_xylene/mole_total;
P = x_benzene*178.6+x_toluene*74.6+x_xylene*28;
print "total pressure = %f kPa"%(P)
benzene = (x_benzene*178.6*100)/P;
toluene = (x_toluene*74.6*100)/P;
xylene = (x_xylene*28*100)/P;
print "xylene = %f toluene = %f benzene = %f"%(xylene,toluene,benzene)
import math
vapor_pressure=8. #in kPa
pressure=100. #in kPa
volume=1 #in m3
volume_ethanol=volume*(vapor_pressure/pressure);
volume_air=1-volume_ethanol;
print "volumetric composition:- air composition = %f ethanol compostion = %f"%(volume_air*100,volume_ethanol*100)
molar_mass_ethanol=46;
molar_mass_air=28.9;
mass_ethanol=0.08*molar_mass_ethanol; #in kg
mass_air=0.92*molar_mass_air; #in kg
fraction_ethanol=(mass_ethanol*100)/(mass_air+mass_ethanol);
fraction_air=(mass_air*100)/(mass_air+mass_ethanol);
print "composition by weight:-Air = %f Ethanol vapor = %f"%(fraction_air,fraction_ethanol)
mixture_volume=22.3*(101.3/100)*(299./273); #in m3
weight_ethanol=mass_ethanol/mixture_volume;
print "weight of ethanol/cubic meter = %f Kg"%(weight_ethanol)
w_ethanol=mass_ethanol/mass_air;
print "weight of ethanol/kg vapor free air = %f Kg"%(w_ethanol)
moles_ethanol=0.08/0.92;
print "kmol of ethanol per kmol of vapor free air = %f"%(moles_ethanol)
import math
vapor_pressure=8. #in kPa
volume_ethanol=0.05;
partial_pressure=volume_ethanol*100;
relative_saturation=partial_pressure/vapor_pressure;
mole_ratio=volume_ethanol/(1-volume_ethanol);
print "mole ratio = %f \nrelative saturation = %f %%"%(mole_ratio,relative_saturation*100)
volume_vapor=(8./100)*100;
ethanol_vapor=volume_vapor/100.;
air_vapor=1-ethanol_vapor;
saturation_ratio=ethanol_vapor/air_vapor;
percentage_saturation=mole_ratio/saturation_ratio;
print "percentage saturation = %f %%"%(percentage_saturation*100)
print "corresponding to partial pressure of 5kPa we get a dew point of 17.3 degree celcius"
import math
p = 4.24 #in kPa
H_rel = 0.8;
p_partial = p*H_rel;
molal_H = p_partial/(100-p_partial);
print "initial molal humidity = %.3f"%(molal_H)
P = 200. #in kPa
p_partial = 1.70 #in kPa
final_H = p_partial/(P-p_partial);
print "final molal humidity = %.4f"%(final_H)
p_dryair = 100 - 3.39;
v = 100*(p_dryair/101.3)*(273./303);
moles_dryair = v/22.4;
vapor_initial = molal_H*moles_dryair;
vapor_final = final_H*moles_dryair;
water_condensed = (vapor_initial-vapor_final)*18;
print "amount of water condensed = %f kg"%(water_condensed)
total_air = moles_dryair+vapor_final;
final_v = 22.4*(101.3/200)*(288./273)*total_air;
print "final volume of wety air = %f m**3"%(final_v)