Documentation / ChemSep data
ChemSep data
Cheméo serves values from the ChemSep v8.3 pure component data, by Harry Kooijman and Ross Taylor (2021, 2022). The data are distributed under the Artistic License 2.0. Every value taken from them is cited as "ChemSep v8.3" on the compound pages, and the original data are at chemsep.org.
The values on Cheméo are Cheméo's conversion of the ChemSep files, a modified version: they are converted to Cheméo's units and correlation forms, some ranges are narrowed, and part of the files is left out. This page documents every difference, as the licence asks. Values found wrong at the source are listed on Corrected source values.
The files
DWSIM's copies of ChemSep's chemsep1.xml ("ChemSep v8.3 pure component data",
2021) and chemsep2.xml ("ChemSep v8.31 pure component data 2", 2022), from the
DWSIM repository at commit 1abf72d:
| file | sha256 |
|---|---|
chemsep1.xml |
31e72c40b2b3b084161314c3262e227fcdd773c0bf2070bacbae9c5da203533f |
chemsep2.xml |
3dfc57f4d5f0c9c0fb4dfb6caffe860e0dffe44618eb091a91f9ca5dd932cd2a |
They hold 558 compound records, 556 distinct CAS numbers. Benzoic acid and cumene
hydroperoxide appear in both files with different values: Cheméo uses the
chemsep1.xml record and leaves the other out.
A record is matched to a Cheméo compound by its structure (its SMILES). A record that cannot be matched is not shown. When two records (two CAS numbers) have the same structure, only one of them is shown.
Constants
Each constant is shown as a point from ChemSep, converted to Cheméo's unit:
| ChemSep | unit in the file | Cheméo property | conversion |
|---|---|---|---|
| Critical temperature | K | Tc | none |
| Critical pressure | Pa | Pc (kPa) | ÷ 1,000 |
| Critical volume | m³/kmol | Vc | none |
| Critical compressibility | Zc | none | |
| Acentric factor | ω | none | |
| Normal boiling point | K | Tboil | none |
| Melting point | K | Tfus | none |
| Triple point temperature | K | Ttriple | none |
| Triple point pressure | Pa | Ptriple (kPa) | ÷ 1,000 |
| Heat of formation (ideal gas, 298.15 K) | J/kmol | ΔfH°gas (kJ/mol) | ÷ 10⁶ |
| Gibbs energy of formation | J/kmol | ΔfG° (kJ/mol) | ÷ 10⁶ |
| Rackett parameter | Zra | none | |
| Dipole moment | C·m | debye | ÷ 3.33564 × 10⁻³⁰ |
| UNIQUAC r and q | UNIQUAC Ri, Qi | none |
Left out:
- zeros used as placeholders: a value of exactly 0 for the critical temperature, pressure or volume, or for a boiling, melting or triple point;
- a heat or Gibbs energy of formation of 0, except for an element. In the files: two heats and one Gibbs energy.
Temperature-dependent properties
Each is shown as a correlation, with ChemSep's validity range:
| ChemSep | unit in the file | Cheméo property | unit factor f |
|---|---|---|---|
| Vapour pressure | Pa | Pvap (kPa) | 10⁻³ |
| Ideal gas heat capacity | J/kmol/K | Cp,gas (J/mol×K) | 10⁻³ |
| Liquid heat capacity | J/kmol/K | Cp,liquid (J/mol×K) | 10⁻³ |
| Heat of vaporization | J/kmol | ΔvapH (kJ/mol) | 10⁻⁶ |
| Liquid density | kmol/m³ | ρl (kg/m³) | the record's molecular weight |
| Liquid viscosity | Pa·s | η | 1 |
| Liquid thermal conductivity | W/m/K | λ, liquid | 1 |
| Vapour thermal conductivity | W/m/K | λ, gas | 1 |
| Surface tension | N/m | γ | 1 |
Equation forms
ChemSep numbers its equations as DIPPR does. The unit factor f is folded into the coefficients, which is exact: no curve is refitted.
| ChemSep equation | Cheméo form | coefficients |
|---|---|---|
| 1 to 5, polynomials | dippr-100 |
equation n keeps its first n coefficients, each × f; the others are 0 |
| 100 | dippr-100 |
A to E × f |
| 101 | dippr-101 |
A + ln f; B to E unchanged |
| 10, ln Y = A − B/(T + C) | antoine, ln Y = A + B/(T + C) |
A + ln f, −B, C |
| 102 | dippr-102 |
A × f |
| 105 | dippr-105 |
A × f |
| 106 | dippr-106 |
A × f; Tc is the record's own critical temperature |
| 107 | dippr-107 |
A, B and D × f |
| 16, Y = A + exp(B/T + C + D·T + E·T²) | chemsep-16 |
A × f, C + ln f |
Equation 10 is read with the natural logarithm: it gives 1 atm at the normal boiling point. Four liquid heat capacities in equation 4 carry a fifth coefficient E. It is not part of the cubic equation and is dropped.
Left out:
- equations with no Cheméo form: 116 (41 surface tensions), 200 (5 vapour pressures), 118 (1 liquid viscosity);
- every other element of the files:
- properties: absolute entropy, heat of combustion, heat of fusion, vapour viscosity, the second liquid viscosity (RPS), the second (Antoine) vapour pressure, the RPP ideal gas heat capacity, second virial coefficient, solid heat capacity and density, relative permittivity, liquid volume at the normal boiling point, specific gravity, parachor, solubility parameter, radius of gyration, Lennard-Jones diameter and energy, van der Waals area and volume, Fuller and Wilson volumes, charge;
- model parameters: Mathias-Copeman, COSTALD, Chao-Seader, API-SRK, UNIQUAC q', and the group assignments (UNIFAC VLE and LLE, modified UNIFAC, ASOG, UMR, GC method);
- the molecular weight, which only converts the liquid density (Cheméo computes its own from the structure).
Ranges, narrowed and never extended
- Capped at the critical temperature. Every liquid-side curve whose range runs past the record's critical temperature ends there: 167 vapour pressures (15 of them then cut lower, at the critical pressure, below), 118 liquid densities, 52 heats of vaporization, 19 surface tensions, 3 liquid viscosities, 2 liquid heat capacities and 1 liquid thermal conductivity. Most pass it by less than 5%. Water's heat of vaporization, given to 647.28 K, ends at its critical temperature, 647.14 K. For a few records the critical temperature of the file lies 9 to 24 K below the range of its own curves (octanal to tridecanal, ethylacetylene, acetyl chloride, biphenyl), so their curves end that much earlier. The ideal-gas heat capacity and the vapour thermal conductivity keep their range: a gas has properties above the critical temperature.
- Cut where the vapour pressure exceeds the critical pressure. 71 vapour pressures rise more than 5% above the record's critical pressure below its critical temperature (styrene's to 83 times it). Their range ends where the curve first crosses the critical pressure: styrene's at 531.4 K instead of 636 K. A smaller excess, of at most 5% and found near the critical temperature, is left as it is.
- Cut before a negative tail. 187 surface tensions turn slightly negative (up to about −0.7 mN/m) as they approach the critical temperature. The range ends at the last temperature before the first negative value, on a grid of 1,001 temperatures.
- The original upper limit is kept in the comment. A curve capped at the critical temperature says "Range stopped at Tc; ChemSep gives it to … K."; one cut before a negative tail says "Range stopped where the equation turns negative; ChemSep gives it to … K."; one cut at the critical pressure says "Range stopped where the equation exceeds Pc; ChemSep gives it to … K.". A curve narrowed twice carries the comment of the last cut. An untouched curve has no comment.
- Refused curves, not shown:
- an empty range, or one starting at 0 K: 2 liquid heat capacities, 1 surface tension;
- a curve that cannot be evaluated over its range: 1 heat of vaporization (dimethylacetylene, undefined at the file's critical temperature);
- a curve that is negative at the start of its range: 1 vapour thermal conductivity;
- a vapour pressure that exceeds the critical pressure in the lower half of its range: none in v8.3.
What ChemSep does not say
ChemSep does not flag which of its values are measured and which are estimated. Cheméo shows them as ChemSep's values, cited to ChemSep, beside the other sources of each compound.
