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# v0.6.3 | ||
# v0.6.4 | ||
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## New Features | ||
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- New Activity model: Hard-constraint Neural Network for Consistent Activity Coefficient Prediction(`HANNA`). requires the loading of the auxiliary package `ClapeyronHANNA`. | ||
- New ideal model: PPDS correlations (`PPDSIdeal`) | ||
- New Function: `reference_chemical_potential`, to calculate the reference chemical potential used in activity coefficient calculations | ||
- New Functions: `activity` and `aqueous_activity`. both functions use the ability to change reference chemical potentials. | ||
- New Functions: `spinodal_pressure` and `spinodal_temperature`. | ||
- New function: `split_model_binaries`, that returns a list of all binary combinations of an n-component model. | ||
- New Saturation Method: `CritExtrapolation`, that calculates saturation volumes and pressures via extrapolation from the critical point. | ||
- `lb_volume` now has a three-arg version: `lb_volume(model,T,z)`. | ||
- `p_scale` is now defined in terms of `T_scale` and `lb_volume`. | ||
- Stability improvements for bubble/dew calculations. | ||
- Speed improvements for single and multicomponent equilibria. | ||
- Association solver is now faster for small association matrices. | ||
- New association mixing rule: Mie-15 (`:mie15`,`:dufal`) | ||
- Michelsen TP-Flash: in case of valid K values but single phase rachford-rice, the procedure will assume bubble or dew point as a first iteration. | ||
- Joback: new submodule: `JobackGC` that provides all available properties using the joback correlations. | ||
- SAFT-VR-Mie: speed improvements for calculation of association strengths. | ||
- Cubics: Better initial point for single component saturation calculations. | ||
- `split_model` now works for `ClapeyronParam`,`Symbol`,`Number`,`AbstractString`,`Tuple`,`Missing` and `Nothing`. before those could only be splitted if inside an `EoSModel`. | ||
- `StructGroupParam` is deprecated, `GroupParam` has all the functionality of `StructGroupParam`. | ||
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- New model: SAFT-VR-Mie with Gross-Vrabec quatrupolar contribution (`SAFTVRMieGV`) | ||
- New model: Co-Oriented Fluid Functional Equation for Electrostatic interactions (`COFFEE`) | ||
- Better support for evaluation of model properties at V == Inf (ideal gas limit) | ||
- New method: `adiabatic_index`, that calculates the ratio between the isobaric and isochoric heat capacities. | ||
- new API: `has_fast_crit_pure`, to indicate that models can calculate their pure critical point quickly. saturation initial guesses use the result of this function to decide if and when to call the `crit_pure` routine. | ||
- speed ups in some pressure routines | ||
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## Bug fixes | ||
- `SAFTgammaMie` fixes. | ||
- `SingleFluid` has improved initial points for liquid volume evaluation. | ||
- miscelaneous database improvements. | ||
- `second_virial_coefficient` for cubics was ignoring the translation. | ||
- improvements to the initial point of `SingleFluid`. | ||
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- `MultiFluid` and `SingleFluid` models did not use the correct gas constant. | ||
- Fix mixing rule in `SAFTVRMie`. | ||
- `VT_identify_phase` now returns `:unknown` for an unstable state input. | ||
- Typos in `TProperty` for pure models. |