- The new minimum supported julia version is v1.10.
- Support for
ForwardDiffv1.0. - the following EoS now support parametric parameters:
SAFTgammaMie(includingstructSAFTgammaMie)PCPSAFT(includingHeterogcPCPSAFTandHomogcPCPSAFT)CPPCSAFTsPCSAFT(includinggcsPCSAFT)pharmaPCSAFT
Given a model with parametric parameters, one can now build another model with a different number type using the function Clapeyron.promote_model(::Type{T},model) where T <: Number.
SAFTgammaMie: mixed segment paramters are now stored in the model parameters instead of inside the groups.- Faster
split_model - Faster parameter instantiation, as now the
sourcesandsourcescsvcan be optionallynothing,and there is less copying of vectors. - New Function:
USCT_temperature.USCT_mixwas renamed toUSCT_pressure(The alias is still available, but it could be removed in future Clapeyron versions.) - Estimation Framework: initial support for gradient optimization (using
ForwardDiff) with parametric models.
- fixed
CPAinitialization with custom parameters. - fixed
CPAdefault locations. - fixed
ePCSAFTinitialization with custom ideal models. - general flash: support for pure supercritical states.
- fix bugs in noncondensable/nonvolatiles Fugacity solver.
-
Experimental: support for using ForwardDiff through some equilibria procedures in some restricted cases:
saturation_temperaturesaturation_pressurebubble_pressure(only helmholtz EoS, without non-volatiles)bubble_temperature(only helmholtz EoS, without non-volatiles)dew_pressure(only helmholtz EoS, without non-condensables)dew_temperature(only helmholtz EoS, without non-condensables)tp_flash(only helmholtz EoS, without non-condensables nor non-volatiles)PpropertyTPropertyX-Yflashes (single component helmholtz EoS)
For example, this function now works without the need to propagate dual information through any iterative solvers:
function ad_function(model,Q) z = Clapeyron.SA[1.0] p = 1e5 T = 350.0 k = 10 h1 = 6200.0 T1 = PH.temperature(model,p,h1,z) h2 = h1 + Q T2 = PH.temperature(model,p,h2,z) return -Q + (T - (T1+T2)/2) * k end model = PR("air") ForwardDiff.derivative(Base.Fix1(ad_function,model),500.0)
- Fix typo in composition return
ChemPotDewTemperature - incorrect scaling for second virial coefficient in the case of cubics
- fixing support for second order properties in activity + puremodel EoS calculation
pharmaPCSAFTnow considerswaterandwater08for it's T-dependend hard-sphere diameter. Before, onlywater08used the specialized behaviour, andwaterreturned the stock PCSAFT parameters.- speed improvements in
MichelsenTPFlashand fugacity-based bubble/dew calculations
- Fix errors with the use of
EoSSuperancillariesalong withpharmaPCSAFT - rachford-rice: Fix errors when there are NaN K-values corresponding to non-condensables or non-volatiles.
tp_flash: Fix errors when there are NaN K-values corresponding to non-condensables or non-volatiles.- typo in
x0_sat_pure_spinodal
- New function:
partial_property, for calculating partial properties at constant pressure and temperature. - New functions:
widom_pressure,widom_temperature,ciic_pressure,ciic_temperature, that calculate the maxima of isobaric heat capacity at constant pressure (widom) or constant temperature (CIIC). - New models: original UNIFAC 2.0 (
ogUNIFAC2, from doi.org/10.1016/j.cej.2024.158667) and modified (Dortmund) UNIFAC 2.0 (UNIFAC2, from doi.org/10.48550/arXiv.2412.12962). - Ideal models: now all ideal models (with the exception of
BasicIdeal) support optionally setting molecular weights. - Database: the behaviour of
getparams(;return_sites)was changed. Now, all single parameters used when building theSiteParamwill be removed from the result (if sites are built.). The removed parameters will also not be checked for complete specification (non-existing sites are made equivalent to zero sites). - Estimation: more flexibility in setting indices.
- ReidIdeal: Parameters for
a,b,c,d,eare now included inReidIdealParam.
- Stability improvements in
xy_flash. - Stability improvements in bubble and dew points
- Fix K-value initialization when components are over JT temperature.
- Stability improvements for spinodal initialization, used for pure saturation pressure calculations.
- Fixed bugs on the PH and PS modules.
Symbolics.jlextension now compiles correctly.- Stability improvements in
xy_flash
- New general formulation for flashes. the formulation supports any combination of P,T,H,U,S,V,vapour fraction (q),given that initial values are provided. the formulation can be accessed via calling the function
Clapeyron.xy_flash(model,spec::FlashSpecifications,z,components0,fractions0,volumes0,T0) - New methods: flashes based on the general formulation, with automatic initialization:
- p-H flash: (
ph_flash) - p-S flash: (
ps_flash) - V-T flash: (
vt_flash) - T-S flash: (
ts_flash) - vapour fraction - T flash: (
qt_flash) - vapour fraction - P flash: (
qp_flash)
- p-H flash: (
- New Flash method:
GeneralizedXYFlash, the only available method for other flashes that are not P-T formulations. - New method:
Clapeyron.set_reference_state!(model::EoSModel,state::ReferenceState;verbose = false), that allows setting reference states for any model that supports it. - flashes (with the exception of
tp_flash) now return aFlashResultobject.Clapeyron.tp_flash2returns aFlashResultthat is converted to the old format internally. - New function:
PProperty(model,T,prop,z,property), that calculates the pressure in T-X coordinates. - Activity models and Composite-γ-ϕ Models can now be used to calculate caloric properties.
- Activity models and Composite-γ-ϕ Models have support for setting reference states.
- Better
Base.showmethods for some Clapeyron.jl structs - Reference states are now shown for models.
- the default method for
tp_flashwas changed toMichelsenTPFlash
TPropertyfixes and stability improvements.- stability improvements in calculation of bubble/dew initial points
- stability improvements when calculating Rachford-Rice iterations.
- fixes for setting reference states with cubic EoS, SAFT-γ-Mie and other custom EoS not created via
@newmodelmacros. - fixes for some component names not being used in empiric EoS
- fixes for
crit_mix
-
Experimental: Bulk properties for Pressure-Enthalpy and Pressure-Entropy, the syntax is the following:
using Clapeyron: PH PH.entropy(model,p,h,z) PH.adiabatic_index(model,p,h,z,T0 = T0) #suplying an initial point for the temperature
The calculation is done via
Clapeyron.Tproperty. there are alsoPTandVTfunctions for parity.
- fixes in calculation of spinodal with cubics.
MultiFluidandSingleFluiderrors when T_reducing != Tc.- fix
VT_identify_phase. - fix GC-to-component asssociation mix when there are non-symmetric values.
- 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 thecrit_pureroutine. - speed ups in some pressure routines
MultiFluidandSingleFluidmodels did not use the correct gas constant.- Fix mixing rule in
SAFTVRMie. VT_identify_phasenow returns:unknownfor an unstable state input.- Typos in
TPropertyfor pure models.
- New Activity model: Hard-constraint Neural Network for Consistent Activity Coefficient Prediction(
HANNA). requires the loading of the auxiliary packageClapeyronHANNA. - New ideal model: PPDS correlations (
PPDSIdeal) - New Function:
reference_chemical_potential, to calculate the reference chemical potential used in activity coefficient calculations - New Functions:
activityandaqueous_activity. both functions use the ability to change reference chemical potentials. - New Functions:
spinodal_pressureandspinodal_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_volumenow has a three-arg version:lb_volume(model,T,z).p_scaleis now defined in terms ofT_scaleandlb_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:
JobackGCthat 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_modelnow works forClapeyronParam,Symbol,Number,AbstractString,Tuple,MissingandNothing. before those could only be splitted if inside anEoSModel.StructGroupParamis deprecated,GroupParamhas all the functionality ofStructGroupParam.
SAFTgammaMiefixes.SingleFluidhas improved initial points for liquid volume evaluation.- miscelaneous database improvements.
second_virial_coefficientfor cubics was ignoring the translation.- improvements to the initial point of
SingleFluid.
SAFTgammaMiefixes.
tpdfixes.MultiPhaseTPFlashfixes.- Association: all temporary storage is now initialized
- New models: Electrolyte models are now supported! We have introduced the
ESElectrolyteframework which will let users combine any electrostatic model (DH,MSAandBorn) and relative static permittivity model with any of our supported equations of state. Due to this flexibility, we now support four existing SAFT-type electrolyte equations (with planned support for more):ePCSAFTSAFTVREMieeSAFTVRMieSAFTgammaEMie
- New method: Two new methods specific to electrolytes have been added:
mean_ionic_activity_coefficientandosmotic_coefficient, along with their saturated variants. - New method:
MultiPhaseTPFlash, that solves multiphase,multicomponent TP-flash with automatic phase detection. this method is now the default when callingtp_flashwith more than two components and helmholtz-based models. - New method:
Tproperty(model,p,prob,z,property)to calculate temperatures, given pressure and another property. - New model: To model solubility of salts,
SolidKshas been added in order to obtain the solubility of salts using the infinite-dilution approach as opposed to the pure-fluid approach usingSolidHfus. - additional method:
x0_volume_liquid(model,p,T,z)andx0_volume_solid(model,p,T,z)can be overloaded to calculate liquid an solid volumes, using the pressure as information. They are defined asx0_volume_liquid(model,p,T,z) = x0_volume_liquid(model,T,z)andx0_volume_solid(model,p,T,z) = x0_volume_solid(model,T,z) - tangent plane distance (
tpd) calculations are now faster. VT_diffusive_stabilitynow useseigmininstead of the full eigen calculation.isstablenow works on (P,T,z) space, for the (V,T,z) space, useVT_isstable. there are now (P,T,z) versions of each stability function.- calculation of volumes,saturation pressures and critical points of CPA models now defaults to the inner cubic model when there is no association present.
- The default association implementation now uses a combination of accelerated successive substitution and newton optimization. While increasing allocations, the method is faster.
- the default
volumeimplementation now uses implicit AD to support derivatives. instead of propagating derivative information through the iterative procedure. This allows workloads of the type:ForwardDiff.derivative(_p -> property(model,_p,T,z,phase = :l,vol0 = v0),p)to be efficiently calculated. Clapeyron.tpdcode has been optimized.tpdhas new keywords:break_first, that tries to return a negative tpd as early as possible,llefor only calculating TPD in liquid phases,strategy, that changes the search strategy between a K-value search (:wilson), a pure component search (:pure) or both strategies (default).Clapeyron.tpdnow supports activity models (if the keywordlleis set totrue)MichelsenTPFlashwill now try LLE if the initial equilibrium type is not set and VLE fails.- New EoS: modified Lee-Kesler-Plöcker with consistent parameters (
LKPmod) - New EoS: Lee-Kesler-Plöker-equation of state, Sabozin-Jäger-Thol enhancement (
LKPSJT,enhancedLKP)
- PCPSAFT: typo in unlike asssociation parameters
- Support for reference states. A reference state is a point in V-T space where H = H₀ and S = S₀. Setting those have uses in Reaction equilibria and when comparing between different models.In particular, Reference states are stored in a
ReferenceState <: ClapeyronParamin the ideal model parameters. TheBasicIdealmodel is, intentionally, the only ideal model in Clapeyron that does not have this struct and, as a consequence, it is not able to set reference states. - Support for superancillaries via
EoSSuperancillaries.jl. When the package is loaded, initial saturation points for cubics and PCSAFT are overloaded to use superancillary evaluations instead of the generalx0_sat_purefunction. in the case ofPCSAFTmodels, it also speeds up the evaluation ofcrit_pure. - New EoS: EOS-CG (2021) (
EOS_CG), a reference model for humid gases and CCS mixtures. - New EoS: Lee-Kesler-Plöcker (
LKP) - New EoS: Shomate ideal model (
ShomateIdeal) - database: PCPSAFT,gcPCSAFT and gcPCPSAFT are updated to use the values of Rehner (2023).
- new functions:
helmholtz_free_energy_res,gibbs_free_energy_res,internal_energy_res,enthalpy_res - database:
ReidIdealnow uses the poling coefficients by default. - database:
JobackIdealhas support for more common group fragments used in gcPCSAFT. melting_temperature,sublimation_temperaturedoes not allocate anymore. Note that the function can still allocate if the EoS model itself allocates.
- Incorrect value for CPA with water (#256)
- Bug in SAFT-VR-SW (#165)
- Bug in CP-PC-SAFT
- Association models don't allocate anymore in the case of a single association site pair.
saturation_pressure(model,T)(ChemPotVSaturation,IsoFugacitySaturation) does not allocate if the calculation does not require a critical point calculation. Note that the function can still allocate if the EoS model itself allocates. the same optimizations were applied tosaturation_temperature(AntoineSaturation,ClapeyronSaturation),sublimation_pressureandmelting_pressure.- Bulk properties now accept a
vol0initial point for the volume solver. - SAFT-VR-Mie uses a divided approach for calculating
d: if θ = ℂ*ϵᵢ/T > 1, then it uses a 10-point gauss-laguerre integrator. Otherwise, the Assen method of finding a cut point and integrating the rest is used. A description of the method is found here: https://teqp.readthedocs.io/en/latest/models/SAFT-VR-Mie.html. the cut allows for better accuracy at higher reduced temperatures.
- Peng-Robinson now uses more accurate
ΩaandΩbvalues - CPA/sCPA now uses SI units as input.
- New EoS: Solid SAFT-VR Mie (
SAFTVRSMie) - New EoS: Solid soft-SAFT (
solidsoftSAFT) - New property: sublimation pressure.
sublimation_pressure(model::CompositeModel,T) - New property: melting pressure.
melting_pressure(model::CompositeModel,T) - New property: sublimation temperature.
sublimation_temperature(model::CompositeModel,p) - New property: melting temperature.
melting_temperature(model::CompositeModel,p) - New property: triple point.
triple_point(model::CompositeModel) CompositeModelwas revamped to support more general equilibria. in particular it will be used to represent equilibria with Activity Models along with with Real Gases. As a result of these enhancements,CompositeModelnow supportsbubble_pressure,bubble_temperature,dew_pressure, anddew_temperature.DETPFlashsupports LLE equilibria with activity models- Bulk properties now accept a
vol0initial point for the volume solver.
SAFTVRMiewas allocating excesively because of unbound type parameter.- typos in
pharmaPCSAFT SanchezLacombedidn't setkcorrectly when passed asuserlocationsCPA, SAFT equation of state and other EoS that implement association,don't need to specifybondvolandepsilon_assoc, when using non-associating species.- correct implementation of
lb_volumeforCPPCSAFT - better implementation of
lb_volumeforpharmaPCSAFT
Base.getindexandBase.setindexwithSingleParam,PairParamandAssocParamnow works with strings. the strings are compared with the components (or groups) stored in each param. in particularAssocParamallows set/get index methods if you pass aTuple{String,String}:
julia> model = PPCSAFT(["water","ethanol"],assoc_options = AssocOptions(combining = :esd))
PPCSAFT{BasicIdeal} with 2 components:
"water"
"ethanol"
Contains parameters: Mw, segment, sigma, epsilon, dipole, dipole2, epsilon_assoc, bondvol
julia> model.params.bondvol[("water","a"),("water","b")]
0.35319
julia> model.params.bondvol[("water","a"),("water","b")] = 0.36
0.36
julia> model.params.bondvol[("water","a"),("water","b")]
0.36PCPSAFTis defined (alias forPPCSAFT)- New EOS: Critical-point based PC-SAFT
CPPCSAFT(https://doi.org/10.1021/ie502633e) - Experimental: new
get_k/get_l/set_k!/set_l!defined for cubics
- bug in ether and aldehyde parameters in UNIFAC (ClapeyronThermo#225)
- more strict checks for saturation temperature and better initial point.
- New EoS: Polar PCSAFT with Quadrupolar interactions (
QPPCSAFT) - New EoS: Group-Contribution simplified PC-SAFT (
gcsPCSAFT) - New EoS: Group-Contribution homosegmented polar PC-SAFT (
gcPPCSAFT) Unitful.jlsupport has been moved into an extension.MultiComponentFlash.jlsupport via extension: you can passmodel::EoSModeltoMultiComponentFlash.flash_2ph. there is also a newMCFlashJLmethod that callsflash_2phusing theClapeyron.tp_flashinterface.- custom types can be passed to the
userlocationskeyword argument, definingClapeyron.can_nt(::datatype) = trueandClapeyron.to_nt(x::datatype)::Union{AbstractDict,NamedTuple}
- bug in
pharmaPCSAFTmixing rules
Clapeyron.diagvaluesnow acceptsx::Number(returning the same number)
- more flexible sites parser (#214). Before, some site names where hardcoded.
- Polar PC-SAFT now uses the Esper et al. (2023) parameters.
- added promotion of types for solid solvers and
pharmaPCSAFT(#212)
- New Function:
export_model, that allows exporting a current clapeyron model into a series of csv files. - Metaheuristics.jl extension to allow passing a
Clapeyron.EstimatortoMetaheuristics.optimize(optimize(f,estimator,method)) Clapeyron.Estimatornow has aobjective_formfield.
- Databases were standardized according to CAS. almost all components present in Clapeyron.jl databases are present in
@DB/properties/identifiers.csv. - COSMOSAC-2002 (
COSMOSAC02),COSMOSAC-2010 (COSMOSAC10) and COSMOSAC-dispersion (COSMOSACdsp) can now read files from the NIST database found at https://github.com/usnistgov/COSMOSAC . to use those parameters, pass the keyworduse_nist_database = true - New model: doubly association perturbation theory (
DAPT) - New model: PCSAFT with association dependent hard sphere diameter (
ADPCSAFT) - New model: translated-and-consistent Peng-Robinson (
tcPR) - New model: translated-and-consistent Peng-Robinson, with Wilson and gE-res mixing rule (
tcPRW) - New model: translated-and-consistent Redlich-Kwong (
tcRK) - New Mixing Rule: residual (excess) gibbs energy mixing rule (
gErRule) - New model: consistent PR - Twu (
cPR) - New alpha function: Twu-88 (
Twu88Alpha) - New alpha function: soave-2019 (
Soave2019Alpha) DETPFlashnow supports theequilibrium = :lleoption, to only find liquid phases.
- Support for solid models (
Clapeyron.sle_solubility,Clapeyron.slle_solubilityandClapeyron.eutectic_point).
eltype(::SAFTVRMieParam)is defined.
- Experimental support models with diferent types of parameters (that aren't
Float64). This allows, among other things, creating models that have uncertainty in their parameters, and track that uncertainty across property calculations.PCSAFTandSAFTVRMiesupport this. (uncertainty support viaMeasurements.jl+ForwardDiffOverMeasurements.jlfor autodiff rules) - Models built automatically via the
@newmodel,@newmodelgcandnewmodelsinglemacros now allow to pass single components as a string (PR("water")). There is also more compatibility with Group Contribution modelsPCSAFT(["water" => ["H2O"=>1]],idealmodel = WalkerIdeal). - minor inprovement on
x0_sat_purewhen the model cannot provide a virial coefficient.
- rework of
@newmodel,@newmodelgcandnewmodelsinglemacros. Now they also define the outer constructor. for a simple EoS that does not require transformation of parameters, you can now do:
@newmodel MyModel EoSModel MyModelParam
#define locations for your model, relative to the current database location
Clapeyron.default_locations(::Type{MyModel}) = ["models/mymodel"]
#define references
Clapeyron.default_references(::Type{MyModel}) = ["TODO"]- new macro
@newmodelsingleton, that defines "singleton" EoSModels. - Rework of MultiParameter EoS. there are two new
EoSModelsthat represent Empiric, Multiparameter EoS:SingleFluid: for single component fluidsMultiFluid: for multicomponent fluids, with specific mixing and departure rulesSingleFluidandMultiFluidconstructors are capable of parsingCoolPropJSON single component files. furthermore, you can use the availableCoolPropsingle fluid library by just importingCoolPropinto the current working enviroment (using CoolProp).
- Cubic models that have an alpha dependent of the acentric factor, can be built by passing
acentricfactordirectly touserlocations, instead ofalpha_userlocations(#188) - New Function:
RGas(model)andRgas(), that gives the value of the gas constant used by the model. defaults toClapeyron.R̄ = 8.31446261815324 - New model:
HelmAct, to use multiparameter EoS + activity coefficient models as the departure. - New model:
XiangDeiters - New model:
TholLJ(used inLJRef) - New model:
EmpiricIdeal, the ideal part of a multiparameter model, to be used in conjuction with other EoS - New model:
AlyLeeIdeal - New model:
CPLNGEstIdeal(http://dx.doi.org/10.1016/j.jngse.2014.04.011) - CSVs allow defining a
sepkeyword in the inline CSV options:
Clapeyron Database File
my parameters [csvtype = like, sep = ;]
species,Mw
1,3,5,7-CYCLOOCTATETRAENE;156.22368
IAPWS95,PropaneRef,Ammonia2023are now of typeSingleFluid{EmpiricAncillary}.GERG2008,EOS-LNGare now of typeMultiFluid{EmpiricAncillary,AsymmetricMixing,EmpiricDeparture}@newmodelmacros don't require defining external constructors anymore.SpecialComp(used bypharmaPCSAFT) is now aClapeyronParaminstead of anEoSModel
- (Experimental) Initial
Symbolics.jlsupport for bulk properties onEoSModel. In particular, all Activity models, cubic models, SAFT models without association, and empiric models are supported. for example, this is now supported:
@variables y(..)[1:4], n(..)[1:4]
mixture = UNIFAC(["water","ethanol","methanol","1-propanol"])
moles = [n(t)[i] for i in 1:4] #Clapeyron accepts mole amounts, so it is not necessary to perform transformations to mole fractions
bc_l = y(t, 0.0) .~ activity_coefficient(mixture, 1.0, 298.15, moles)- automatic precompile is disabled in this version.
-
@registermodelmacro is now a no-op. custom models that have acomponents::Vector{String}automatically support the printing interface and if they havemodel.params.Mw, they support molecular weight calculations. -
Cubic roots now use a real solver. this allows more stability and correctness in challenging EoS
- The package now performs precompilation (via
PrecompileTools.jl) of some commonly used functions and EoSModels. this will add more time at the installation of the package, in exchange with decreased loading times each timeClapeyronis loaded in a new julia session. you can turn on/off the feature withClapeyron.precompile_clapeyron!(setting::Bool)(recomended in the case of developing the library). due to how precompilation is done, it is only done from julia 1.9 onwards. - New EoS: NRTL with aspen paranetrization of τᵢⱼ :
aspenNRTL split_modelshould be a little bit faster, and will perform correct splitting of group association models that useget_group_idx.
- Combining rule for epsilon in
SAFTgammaMieupdated from√(ϵᵢ*ϵⱼ)*(σᵢ^3 * σⱼ^3)/σᵢⱼ^6to√(ϵᵢ*ϵⱼ*(σᵢ^3 * σⱼ^3))/σᵢⱼ^3. the old behaviour can be obtained by passing the argumentepsilon_mixing::Symbolto the model constructor. (#179)
MichelsenTPFlashnow supports activity models, it also supportsCompositeModelif they don't reach the multidimensional optimizer. with that, all combinations of 2-phase TP-Flash are supported in the following way:- Raoult:
CompositeModel - Raoult with gas fugacity:
CompositeModel(components, gas = EoSModel) - fugacity: any Helmholtz model
- Activity + ideal gas:
Activity(components, puremodel = IdealModel) - Activity + real gas:
Activity(components, puremodel = EosModel)(ActivityModel(components)normally callsActivityModel(components,puremodel = PR))
- Raoult:
RRTPFlashnow supports acceleration, non-condensables, non-volatiles, activity models andCompositeModel. (the same operations thatMichelsenTPFlashsupports.)MichelsenTPFlashandRRTPFlashprovide initial guesses for LLE equilibria.tp_flash(model,p,T,z,MichelsenTPFlash(equilibrium = :lle))should suffice to calculate LLE flashes.UNIFACmodels should be faster.
-
ideal_consistency(model,V,T,z)that checks ifda0/dV + sum(z)/Vis zero (or as close to zero as the Floating Point Format allows it.) -
broadcasting on
AssocParamis defined (bondvol .= 1e-10 .* bondvol .^3) -
you can pass functions that build models instead of EoSModel types. for example, now you can do:
function myvdW(components;userlocations = String[],verbose = false) return vdW(components;userlocations = userlocations,verbose = verbose,alpha = SoaveAlpha) end model = Wilson(["water","ethanol"];puremodel=myvdW)
- proper namespaces in
@registermodel(#161) - fixed bug in
MichelsenTPFlashwhen using non-volatiles andsecond_order = false - fixed bug when building
UNIFACFVPoly
- you can pass a named tuple to
userlocationsand its variants to build a model directly from those parameters (#156). for example, with PCSAFT:
julia> model = PCSAFT(["a1"],userlocations = (;
Mw = [1.],
epsilon = [2.],
sigma = [3.],
segment = [4.],
k = [0.0;;], #matrix
n_H = [1],
n_e = [1],
epsilon_assoc = Dict((("a1","e"),("a1","H")) => 1000.),
bondvol = Dict((("a1","e"),("a1","H")) => 0.001)))
PCSAFT{BasicIdeal} with 1 component:
"a1"
Contains parameters: Mw, segment, sigma, epsilon, epsilon_assoc, bondvol
- The
denseoption inAssocOptionsis deprecated and it will be removed on 0.5.0. the sparse solver is not used anymore, the dense solver has performance advantages in all cases.
- bug in
@registermodel(#157)
@newmodel,@newmodelsimpleand@newmodelgcmacros had a bug where some structs and types didn't have the proper namespace (#154)
fixed bug on Michelsen TP flash introduced in the last release.
DETPFlash now returns results sorted by increasing molar volume (heavy liquid ->light liquid -> vapour) (fixes #151)
- New EoS: Ammonia2023, an Empiric EoS with a new term (https://doi.org/10.1063/5.0128269)
- Speed improvements on some Empiric EoS
- Estimation Framework: the method is now specified as a csv option instead of just the title.
- Estimation Framework: support for setting species to be estimated.
- some references in the
SAFTVRMie's csv were incorrect. recombine!now works withStructGroupParam.
- incorrect indexing of sites when doing group-to-component transformation (e.g SAFTgammaMie) with more than one association site per molecule.
- better error handling when incorrect group types are assigned.
- Typo in
assoc_translatorfield when creating assoc sites with groups that have multiple association groups. - Correct initialization of
βinrachfordrice
- New Clapeyron Parameter
StructGroupParam, that stores groups, as well as it's bonds between them, used in heteronuclear GC approaches - New EOS: structural SAFT-γ-Mie (
structSAFTgammaMie) - New EOS: heteronuclear GC-PC-SAFT (
gcPCSAFT) - in some limited cases,
split_modelcan now differenciate between group and component parameters inside a model
-
New estimation framework, to fit new model parameters from known data. at the moment of this release, it should support all SAFTs, Cubics, Activity models and models that don't require any special pre-computed cache.
-
Base.transpose(model::EoSModel)is defined. now this is valid code:
T = 300:350
comp = ["water"]
models = [m(comp) for m in (PR,PCSAFT,SAFTVRMie)]
saturation_pressure.(transpose(models),T) #produces a 51×3 Matrix{Tuple{Float64, Float64, Float64}}:x0_sat_purenow returnsVlandVv(in[m^3]) instead oflog10(Vl)andlog10(Vv).- in databases,
segmentis used instead ofm - in databases,
Vcis used instead ofvc - in databases,
Pcis used instead ofpc - in databases,
acentricfactoris used instead ofw
- new EoS: RKPR (
RKPR) - new functions:
cross_second_virialandequivol_cross_second_virial, to calculate B12, at specified z conditions, or by setting equivolumetric mixing. - cubic EoS now support
recombine! PenelouxTranslationandRackettTranslationnow cache their results, resulting in a speed up when using volume translated EoS.Clapeyron.citenow accepts the optional argumentout, that can bedoi(current default, DOI) or:bib(for BibTeX)
- various bug fixes in SAFT-VRQ-Mie. the Hard sphere term now performs the non-additive mixing rule for the multicomponent case. initializations with integer values are fixed.
- new EoS: PCSAFT with activity mixing rules (
GEPCSAFT(components; activity)) (https://doi.org/10.1021/acs.iecr.2c03464) - new EoS: UNIFAC-FV (
UNIFACFV) - new EoS UNIFAC-FV-poly (
UNIFACFVPoly) getparamsnow supports inline csvs, custom locations and the ability to replace or swap out certain parameters, checkgetparamsdocs for more information- new function:
recombine!to recalculate combining and mixing rules after one parameter is modified. at the moment, SAFT and activity models have this defined. - all quadratic mixing rules have an implace version (
sigma_LorentzBerthelot(sigma,zeta)->sigma_LorentzBerthelot!(sigma,zeta)) AssocParamhasgetindex/setindex!methods defined.GroupParamhas a new field,grouptype, to differenciate group parametrizations
icomponentswas removed, useClapeyron.@compsor1:length(model)insteadPairParam.diagvalueswas removed, useClapeyron.diagvalues(param)instead
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dew_pressureanddew_temperaturecan now by calculated withActivityModels. options available can be passed via the new methodsActivityBubblePressure,ActivityBubblwTemperature,ActivityDewPressure,ActivityDewTemperature. helmholtz-based models also support solvingbubble_pressureanddew_pressureusing those methods (http://dx.doi.org/10.1021/acs.iecr.1c03800). -
There is support for γ-ϕ equilibria on
bubble_pressureanddew_pressurewith activity models, that is:, solvingyᵢϕᵢp = γᵢp₀ᵢϕ₀ᵢ𝒫ᵢ -
New Correlation models:
LeeKeslerSat,DIPPR101Satfor saturation pressure and temperature,COSTALD,RackettLiquid,DIPPR105Liquid, for saturated liquid volume. -
New models: Second Virial models (
AbbottVirial,TsonopoulosVirialandEoSVirial2) -
New model:
CompositeModel, used to hold saturation, liquid and vapor correlations. For example, instantiating an Activity Model, that uses Peng-Robinson for a gas model, DIPPR 101 for saturation and COSTALD for liquid volume, with a wilson activity coefficient, can be written as:julia> com = CompositeModel(["water","methanol"],liquid = COSTALD,saturation = DIPPR101Sat,gas = PR) Composite Model: Gas Model: PR{BasicIdeal, PRAlpha, NoTranslation, vdW1fRule}("water", "methanol") Liquid Model: COSTALD("water", "methanol") Saturation Model: DIPPR101Sat("water", "methanol") # Wilson activity model, using the composite model as the pure model julia> model = Wilson(["water","methanol"],puremodel = com) Wilson{CompositeModel{PR{BasicIdeal, PRAlpha, NoTranslation, vdW1fRule}, COSTALD, Nothing, DIPPR101Sat, Nothing}} with 2 components: "water" "methanol" Contains parameters: g, Tc, Pc, ZRA, Mw -
Improved initial points for
bubble_temperatureanddew_temperature. -
MichelsenTPFlashno uses an accelerated successive substitution method.
- cross-association weren't counted in some cases.
- incorrect initialization on
FugBubbleTemperature Clapeyron.lnϕuses the specialized algorithm for volume instead of the general one.
- New combining rules that are done at model creation time instead of runtime:
:cr1and:esd/elliott. the oldelliottcombining rule was renamed toelliott_runtime(it is only used onPharmaPCSAFT, where is required)
crit_pureon CPA was failing (#112, #113)- error on bubble/dew pressure/temperature when using the
v0starting point (#113) crit_purewas slower than expected on julia 1.8- add error path on
SingleParamwhen all data is missing
-
bubble_pressure,bubble_temperature,dew_pressure, anddew_temperaturecan now support custom methods. (subtypingBubblePointMethodorDewPointMethod). the default methods are now namedChemPotBubblePressure,ChemPotBubbleTemperature,ChemPotDewPressure,ChemPotDewTemperature. you can provide some or all necessary initial conditions to those new methods:res = bubble_pressure(model,T,x,ChemPotBubblePressure(;y0;p0;vol0)) -
New bubble/dew methods based on isofugacity conditions:
FugtBubblePressure,FugBubbleTemperature,FugDewPressure,FugtDewTemperature. -
All bubble methods now support leaving some components out of the bubble phase,via the
nonvolatileskeyword, supported by all available bubble solvers. similarly, all dew methods support thenoncondensableskeyword to leave some components out of the dew phase. -
MichelsenTPFlashcan support bothnonvolatilesandnoncondensables. -
SingleParamandPairParamsupport indexing and broadcasting.PairParamhas a modified indexing scheme, whereparam[i]will return the diagonal elements,param[i,j]will return off-diagonal elements.setindex!onPairParamis symmetric by default, that is,param[i,j] = kwill also setparam[j,i]. you can opt out of this by doingparam[i,j,false] = k -
New function:
diagvalues, for obtaining a vector view of the diagonal elements of a Pair or Single Parameter. -
New functions:
VT_gibbs_free_energy_resandVT_helmholtz_free_energy_res -
New saturation method:
saturation_temperature(model,p,::SuperAncSaturation) -
index_reduction(model,x::AbstractVector{Bool})will return a reduced model, according to the true values of the vectorx. Passing another vector will perform the index reduction based on non-empty values, as usual. -
Initial (and optional) support for solid phase volume solving, via
x0_volume_solid -
New EoS (experimental):
AnalyticalSLV, that supports solid, liquid and vapour phases in one continous helmholtz functional. -
the database parser is faster and has better verbose reporting.
-
SAFTVRMieandSAFTGammaMieshould be a little faster on single component evaluations
activity_coefficientandfugacity_coefficientnow works withSVector#104- there was a bug on calculating the length of GC models that went under
split_model
-
model.params.param.diagvaluesis not longer used in the codebase and it will be removed at the next breaking version. usediagvalues(model.params.param)ormodel.params.param[i]instead. -
model.icomponentsis not longer used in the codebase and it will be removed at the next breaking version.1:length(model)orClapeyron.@compsinstead.
- You can now define custom saturation (temperature or pressure) solvers, via subtyping
SaturationMethod. The default solver is now namedChemPotVSaturation. - New methods for saturation pressure:
IsoFugacitySaturation,ChemPotDensitySaturation,SuperAncSaturation(for cubics) - All saturation methods support passing the
critkeyword, to allow using precomputed critical points. - All saturation methods that use a non linear solver support passing convergence options.
- The default solver for
saturation_temperaturewas changed (now namedAntoineSaturation). The new model is much faster and with a similar reliability. the old one is available viaClapeyronSaturation. - New method for TP-Flash:
MichelsenTPFlash - New function:
tpd, that tries to find all negative tangent plane distances - New function:
lle_init, that tries to find good LLE starting points, viatpd - New function:
x0_saturation_temperature(model,p), that returns starting points forsaturation_temperature. - New function:
x0_psat(model,p), that returns starting points forIsoFugacitySaturation. - New function:
antoine_coeffor reduced antoine coefficients. used to accelerate initial points, if available. - New function:
cite(model)returns all references used in the evaluation of a model. bubble_temperature,dew_temperature,lle_temperature,azeotrope_temperatureandvlle_temperaturemethods now iterate directly over the extended-with-temperature non linear system that their pressure cointerparts.- Cubics were revamped and generalized even more. those changes opened the way to introduce more non-standard cubics, all while being compatible with the initial guess procedures, advanced mixing rules and other Clapeyron optimizations for cubics.
- New cubic EoS:
Clausius - New cubic EoS:
Berthelot - New cubic EoS: Patel-Teja (
PatelTeja) - New cubic EoS: Patel-Teja-Valderrama (
PatelTeja) - New cubic EoS: Kumar-Upadhyay two parameter EoS (
KU) - New mixing rule: Modified Wong-Sandler (
ModWS) SoaveAlphanow works withvdWandPR(returning the same value ofPRAlpha)- New EoS: Perturbed, truncated and shifted LJ EoS (
PeTS) - SPUNG is now a constructor for the new
ECSmodel. volumenow accepts avol0initial point.PCSAFTshould be a little bit faster for single component cases
ZeroResidualmodel (a_res = 0)
HVRuleuses the original rule instead of the modified one.ismissingvaluesis preserved when a combining rule is applied. this allows us to track inputed parameters vs calculated ones.
In particular, this release is the one used in the Clapeyron.jl paper. and it's results should be reproducible by locking the version to v0.3.6.
- new functions:
VT_mass_density,VT_mol_density vdW,RKandPRmodels and variants use nowABCubicParam.vdWParam,RKParamandPRParamare now just aliases toABCubicParam.- Roots.jl updated to 2.0
- fixes to UNIFAC models
- fixes to
split_modelon groups
- New EoS: Enhanced Predictive Peng Robinson 1978 (2022) (
EPPR78) - New EoS: Quantum Corrected Peng Robinson (2022) (
QCPR) - New EoS: Modified PCSAFT with T-dependent σ for water (passing
water08) and k0 + k1T mixing rule (pharmaPCSAFT). - New function:
index_reduction(model,z)that removes components with compositions near zero. useful to reduce the dimensionality on multicomponent solvers. - New function:
isstable(model,V,T,z)to check for stability at the input conditions. - New function:
gibbs_duhem(model,V,T,z)to check if the Gibbs-Duhem relations holds for the input model at the specified conditions. - New function:
kij_mixandpair_mixfor arbitrary pair combining rules - volume solver can now perform aditional stability checks by passing
phase = :stable, before only mechanical stability checks were done. - association solver supports Elliot rule for combining rules, passed via
assoc_options(combining = :elliott) - association solver supports dense association matrix, passed via
assoc_options(combining = :dense_nocombining) - Faster
crit_pure,saturation_pressure - Faster
GERG2008andEOS_LNG - some cubic α-functions are faster for single component models
- improved initial saturation point for cubics
CPAandsCPAnow acceptAssocOptions- new mixing
SLKRuleforSanchesLacombe - easier constructors for some empty models:
NoTranslation()instead ofNoTranslation(NoTranslationParam())
- GC models can now be splitted in arbitrary component subsets
absolutetolerancefields removed from almost all EoS (except COSMO models)second_virial_coefficientnow works withSanchezLacombe- some starting points for
softSAFT(original) andBACKSAFTwere wrong. ``softSAFT2016` was not affected. volume_compressnow accepts integer pressures, they are converted internally.volumefor cubics now propagates the pressure type
gibbs_solvation(model,T): For calculation of the solvation energy in a binary model- speed up for activity coefficients and excess gibbs free energies for
NRTL,Wilson,UNIQUACandUNIFAC - new EoS model:
softSAFT2016, that uses the LJ helmholtz energy from thol et al. (2016) - new utility function:
correct_composition_derivative, that returns∑xᵢμᵢ - G. it should be zero or near zero for correctly written models.
- fix error in parameters for
softSAFT - fix errors in use of units. tests added.
- fix error on isobaric expansivity.
- fixes in volume solver
- fixes in initial guesses for
MultiFuidModelandCPA - all multicomponent solvers now accept an initial guess
Model fixes;
WSRuleMonomerIdealnew functions:assoc_site_matrix(model::Union{SAFTModel,CPAModel},V,T,z)to instantiate the association matrixReidIdeal(model::JacobianIdeal)to obtain a Reid ideal model from a Joback Ideal model fastercrit_pureon cubics
- Differential Evolution and Rachford-Rice Tp-flash algorithms have been implemented
- AssocOptions has been added to all SAFT equations
- Further speed-up to cubics
- sat_pure has been renamed saturation_pressure
- Numerous new multi-component VLE functions have been added (dew_pressure, bubble_temperature, VLLE_temperature etc.)
- New models: Full CPA, sCPA and ogUNIFAC