Viskositas Liquid Viskositas Gas Kapasitas Panas Liquid Kapasitas Panas Gas

B. Daftar Konstanta Komponen 1.

Densitas Liquid Tabel 3.1 Konstanta Densitas Liquid Komponen Densitas Liquid kmolm 3          D C T L B A 1 1  , T dalam Kelvin A B C D Acetylene C 2 H 2 2,3948E+00 2,7091E-01 3,0832E+02 2,8571E-01 Formaldehyde CH 2 O 1,9400E+00 2,2240E-01 4,0800E+02 2,8570E-01 Butynediol C 4 H 6 O 2 9,1490E-01 2,3422E-01 6,9500E+02 2,8571E-01 Methanol CH 4 O 2,2880E+00 2,6850E-01 5,1264E+02 2,4530E-01 Propargyl Alcohol C 3 H 4 O 1,3541E+00 2,4900E-01 5,8000E+02 2,8570E-01 Hydrogen H 2 5,3840E+00 3,4730E-01 3,3180E+01 2,7560E-01 Nitrogen N 2 3,1724E+00 2,8479E-01 1,2610E+02 2,9250E-01 Air H 2 O 5,4590E+00 3,0542E-01 6,4713E+02 8,1000E-02 Sumber : Software ChemCAD 5.2

2. Viskositas Liquid

Tabel 3.2 Konstanta Viskositas Liquid Komponen Viskositas Liquid Pa.S           E L DT T C ln T B A EXP  , T dalam Kelvin A B C D E Acetylene C 2 H 2 6,2240E+00 -1,5180E+02 -2,6544E+00 Formaldehyde CH 2 O Butynediol C 4 H 6 O 2 Propargyl Alcohol C 3 H 4 O -1,2265E+01 2.1514e+03 -2,6367E-01 Methanol CH 4 O -2,5317E+01 1,7892E+03 2,0690E+00 Hydrogen H 2 -1,1986E+01 2,6260E+01 -1,7740E-01 -4,4000E-16 10 Nitrogen N 2 -3,2165E+01 4,9690E+02 3,9069E+00 -1,0800E-21 10 Air H 2 O -5,1964E+01 3,6706E+03 5,7331E+00 -5,3495E-29 10 Sumber : Software ChemCAD

3. Viskositas Gas

Tabel 3.3 Konstanta Viskositas Gas Komponen Viskositas Gas Pa.S 2 1 T D T C AT B g     , T dalam Kelvin A B C D Acetylene C 2 H 2 1,20E-06 4,95E-01 2,91E+02 Formaldehyde CH 2 O 8,31E-07 5,69E-01 2,40E+02 Butynediol C 4 H 6 O 2 1,05E-07 7,94E-01 1,11E+02 Methanol CH 4 O 3,06E-07 6,97E-01 2,05E+02 Propargyl Alcohol C 3 H 4 O 4,1863E-07 6,3060E-01 2,5589E+02 Hydrogen H 2 1,56E-07 7,06E-01 -5,87E+00 2,10E+02 Nitrogen N 2 7,63E-07 5,88E-01 6,78E+01 Air H 2 O 2,70E-06 4,98E-01 1,26E+03 -1,96E+04 Sumber : Software ChemCAD 5.2

4. Kapasitas Panas Liquid

Tabel 3.4 Konstanta Kapasitas Panas Liquid Komponen Kapasitas Panas Liquid JKmol K Cp L = A + BT + CT 2 + DT 3 + ET 4 , T dalam Kelvin A B C D E Acetylene C 2 H 2 Formaldehyde CH 2 O Butynediol C 4 H 6 O 2 4,3800E+04 4,7223E+02 Methanol CH 4 O 1,0580E+05 -3,6223E+02 9,3790E-01 Propargyl Alcohol C 3 H 4 O 1,0270E+05 1,7200E+02 Hydrogen H 2 2,2560E+04 -1,9859E+03 1,1547E+02 -1,2598E-01 Nitrogen N 2 -3,3400E+04 3,5070E+03 -4,6700E+01 2,1270E-01 Air H 2 O 2,7637E+05 -2,0901E+03 8,1250E+00 -1,4110E-02 9,3701E-06 Sumber : Software ChemCAD 5.2

5. Kapasitas Panas Gas

Tabel 3.5 Konstanta Kapasitas Panas Gas Komponen Kapasitas Panas Gas JKmol K Cp L = A + BT + CT 2 + DT 3 + ET 4 , T dalam Kelvin A B C D E Acetylene C 2 H 2 3,6760E+04 4,8290E+04 1,7965E+03 3,7220E+04 7,0807E+02 Formaldehyde CH 2 O 3,3270E+04 4,9542E+04 1,8666E+03 2,8075E+04 9,3490E+02 Butynediol C 4 H 6 O 2 4,6550E+04 1,7050E+05 1,6146E+03 1,1314E+05 -7,5018E+02 Methanol CH 4 O 3,9252E+04 8,7900E+04 1,9165E+03 5,3654E+04 8,9670E+02 Propargyl Alcohol C 3 H 4 O 9,3600E+04 7,0700E+04 1,2390E+03 -3,4400E+07 7,5800E+00 Hydrogen H 2 2,7617E+04 9,5600E+03 2,4600E+03 3,7600E+03 5,6760E+02 Nitrogen N 2 2,9105E+04 8,6149E+03 1,7016E+03 1,0347E+02 9,0979E+02 Air H 2 O 3,3359E+04 2,6798E+04 2,6093E+03 8,8880E+03 1,1676E+03 Sumber : Software ChemCAD 5.2

6. Konduktivitas Thermal Liquid