Appendix B

Thermodynamic data

B.1 Thermochemistry

 MWΔHf (kcal/kmol) cp (kcal/kg K)a+bT+cT2+dT3 T[=]K
    abcd
N2280G0.26614833−0.000115942.28947E-07−9.97949E-11
O2320G0.21012261−2.7512E-081.30525E-077.96202E-11
H2O18−57,798G0.428535352.5569E-051.40284E-07−4.77937E-11
NO3021,600G0.23401116−7.4785E-067.77265E-08−3.33892E-11
NO2468091G0.126029750.0002515−1.0823E-071.52424E-12
NH317−10,960G0.384393470.000335362.40276E-07−1.6676E-10
H220G3.246770330.00110931−1.6519E-06−4.30144E-10
C2H226−24,861.244G−0.03886640.002818−1.4593E-062.95786E-10
CO28−26,464.1148G0.26374744−0.000109792.38312E-07−1.08681E-10
CO244−94,203.3493G0.107628320.00039928−3.0459E-079.32634E-11
SO264−71,064.5933G0.089159690.0001252−6.1815E-081.24112E-11
SO380−94,624.40191G0.048953350.00021817−1.1164E-072.42397E-11
FeS2120−42,464.11483S    
Fe2O3160−196,000S    
H2SO498−193,900L    
HNO363−41,650L    
HCl36.5−22,095.7G0.198538384.7198E-58.16674E-82.55489E-11
C3H844−24,861.244G−0.022966510.00166518−8.6233E-071.74783E-10
CH416−17,877.2G0.287561810.000778631.7886E-071.6909E-10
Cl2710G0.090737250.00011389−1.304E-075.22272E-11

Image

Aggregation state for ΔHf: G, Gas; L, Liquid; S, Solid.

B.2 Antoine Correlation and Phase Change

ln(Pv(mmHg))=ABC+T(°C)

image
 ABCλ (kcal/kmol)
H2O18.30363816.44227.029,723
CH3OH18.58753626.55238.868,431
C2H5OH18.91193803.98231.479,266
NH316.94812132.50240.175,583
H213.6333164.9276.34 
N214.9542588.72266.55 
Ar15.233700.51267.31 
CO14.3686530260 
CO222.58983103272.99 
O215.4075734.55266.71,632
N214.9542588.72266.551,335
HCl16.50401714.25258.73,866
FAME17.45305003122.1320,181
C3H8O317.23924487.94132.8014,623

Image

B.3 Heat of Solution (25°C)

In (Figure B.1) we see the heat of solution of various chemicals used along the book.

image
Figure B.1 Heat of solution.

B.4 Steam Properties

λ (kcal/kg)=−0.0000043722 · T(°C)3+0.00043484 · T(°C)2−0.58433 · T(°C)+597.48

Hsat vap (kcal/kg)=−0.0000030903 · T(°C)3+0.00022613 · T(°C)2+0.42436 · T(°C)+597.42

B.4.1 Compressed Liquid

H (kJ/kg)=4.2921 · (T(°C))+4.1269

S (kJ/(kg K))=1.1902×10−5 · (T(°C))3−3.7465×10−3 · (T(°C))2+4.5352 · (T(°C))+0.64547

B.4.2 Saturated Liquid

H (kJ/kg)=3.6082×10−12 · (T(°C))6−3.4120×10−9 · (T(°C))5+1.2303×10−6 · (T(°C))4−2.0306×10−4 · (T(°C))3+1.5552×10−2 · (T(°C))2+3.7216 · (T(°C))+3.0035

S (kJ/(kg K))=1.0372×10−12 · (T(°C))5 −8.6494×10−10 · (T(°C))4+2.8965×10−7 · (T(°C))3−5.6730×10−5 · (T(°C))2+1.6802×10−2 · (T(°C))−2.1997×10−2

B.4.3 Saturated Vapor

H (kJ/kg)=−6.5690×10−12 · (T(°C))6+6.3049×10−9 · (T(°C))5−2.3080×10−6 · (T(°C))4+3.8339×10−4 · (T(°C))3−3.0632×10−2 · (T(°C))2+2.7553 · (T(°C))+2.4957×103

S (kJ/(kg K))=−2.0373×10−12 · (T(°C))5+1.8589×10−9 · (T(°C))4−7.1901×10−7 · (T(°C))3+1.6112×10−4 · (T(°C))2−2.8904×10−2 · (T(°C))+9.1915

B.4.4 Overheated Steam (Up to 10 bar)

H (kJ/kg)=(−0.0000063293 · Pressure(bar)+0.00033179) · (T(°C))2+(0.0124 · Pressure(bar)+1.8039) · (T(°C))+(−6.0707 · Pressure(bar)+2504.6)

S (kJ/(kg K))=0.000000000942 · (T(°C))3−0.00000309 · (T(°C))2+0.00524 · (T(°C))+(6.8171 · (Pressure(bar))(−0.069455))

B.4.5 Overheated Steam (10 bar–150 bar)

H (kJ/kg)=(−0.00000000000011619 · Pressure(bar)2−0.0000000000087596 · Pressure(bar)−0.00000000022611) · (T(°C))4+(0.0000000004298 · Pressure(bar)2+0.00000003276 · Pressure(bar)+0.0000007313) · (T(°C))3+(−0.0000005801 · Pressure(bar)2−0.000046 · Pressure(bar)−0.0005009) · (T(°C))2+(0.0003383·Pressure(bar)2+0.02947·Pressure(bar)+2.195)·(T(°C))+(−0.072042 · Pressure(bar)2−7.7877 · Pressure(bar)+2440.8)

S (kJ/(kg K))=(0.000000000015719 · Pressure(bar)+0.00000000074013) · (T(°C))3+(−0.00000000010074 · Pressure(bar)2−0.000000030171 · Pressure(bar)−0.0000028872) · (T(°C))2+(0.000000094914 · Pressure(bar)2+0.000029097 · Pressure(bar)+0.0050938) · (T(°C))+(0.000041223 · Pressure(bar)2−0.028841 · Pressure(bar)+5.9537)

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