- The Catalyst release process is changing; certain core dependencies of Catalyst will now be capped to ensure Catalyst releases are only installed with versions of dependencies for which Catalyst CI and doc build tests pass (at the time the release is made). If you need a dependency version increased, please open an issue and we can update it and make a new Catalyst release once testing against the newer dependency version is complete.
- Array symbolics support is more consistent with ModelingToolkit v9. Parameter
arrays are no longer scalarized by Catalyst, while species and variables
arrays still are (as in ModelingToolkit). As such, parameter arrays should now
be specified as arrays in value mappings, i.e.
While one can still manually scalarize a parameter array, it is recommended not to do this as it has signifcant performance costs with ModelingToolkit v9. Note, scalarized parameter arrays passed to the two-argument
@parameters k[1:4] pmap = [k => rand(4)]
ReactionSystem
constructor may become unscalarized. - Scoped species/variables/parameters are now treated similar to the latest MTK releases (≥ 9.49).
- The structural identifiability extension is currently disabled due to issues StructuralIdentifiability has with Julia 1.10.5 and 1.11.
- A tutorial on making interactive plot displays using Makie has been added.
- The BifurcationKit extension has been updated to v.4.
- There is a new DSL option
@require_declaration
that will turn off automatic inferring for species, parameters, and variables in the DSL. For example, the following will now error:When this flag is set, all symbolics must be explicitly declared.rn = @reaction_network begin @require_declaration (k1, k2), A <--> B end
rn = @reaction_network begin @species A(t) B(t) @parameters k1 k2 @require_declaration (k1, k2), A <--> B end
- Support for user-defined functions on the RHS when providing coupled equations
for CRNs using the @equations macro. For example, the following now works:
Note that user-defined functions will not work on the LHS of equations.
using Catalyst f(A, t) = 2*A*t rn = @reaction_network begin @equations D(A) ~ f(A,t) end
- Symbolics 6 support.
- Support for simulating stochastic chemical kinetics models with explicitly
time-dependent propensities (i.e. where the resulting
JumpSystem
containsVariableRateJump
s). As suchJumpProblem
s need to be defined overODEProblem
s orSDEProblem
s instead ofDiscreteProblem
s we have introduced a new input struct,JumpInputs
, that handles selecting via analysis of the generatedJumpSystem
, i.e. one can now sayWhen calling solve for problems with explicit time-dependent propensities, i.e. whereusing Catalyst, OrdinaryDiffEq, JumpProcesses, Plots rn = @reaction_network begin k*(1 + sin(t)), 0 --> A end jinput = JumpInputs(rn, [:A => 0], (0.0, 10.0), [:k => .5]) # note that jinput.prob isa ODEProblem jprob = JumpProblem(jinput) sol = solve(jprob, Tsit5()) plot(sol, idxs = :A) rn = @reaction_network begin k, 0 --> A end jinput = JumpInputs(rn, [:A => 0], (0.0, 10.0), [:k => .5]) # note that jinput.prob isa DiscreteProblem jprob = JumpProblem(jinput) sol = solve(jprob) plot(sol, idxs = :A)
jinput.prob isa ODEProblem
, note that one must currently explicitly select an ODE solver to handle time-stepping and integrating the time-dependent propensities. - Note that solutions to jump problems with explicit time-dependent
propensities, i.e. a
JumpProblem
over anODEProblem
, require manual selection of the variables to plot. That is, currentlyplot(sol)
will error in this case due to limitations in the SciMLBase plot recipe.
- Support for auto-algorithm selection in
JumpProblem
s. For systems with only propensities that do not have an explicit time-dependence (i.e. that are notVariableRateJump
s in JumpProcesses), one can now run model simulations viaFor small systems this will just use Gillespie'susing Catalyst, JumpProcesses model = @reaction_network begin kB, S + E --> SE kD, SE --> S + E kP, SE --> P + E end u0 = [:S => 50, :E => 10, :SE => 0, :P => 0] tspan = (0., 200.) ps = [:kB => 0.01, :kD => 0.1, :kP => 0.1] dprob = DiscreteProblem(model, u0, tspan, ps) jprob = JumpProblem(model, dprob) sol = solve(jprob)
Direct
method, transitioning to usingRSSA
andRSSACR
as system size increase. Once can still manually select a given SSA, but no longer needs to specifySSAStepper
when callingsolve
, i.e.# use the SortingDirect method instead jprob = JumpProblem(model, dprob, SortingDirect()) sol = solve(jprob)
- Latexify recipe improvements including display fixes for array symbolics.
- Deficiency one and concentration robustness checks.
The expansion of ReactionSystem
models to spatial lattices has been enabled. Here follows a
simple example where a Brusselator model is expanded to a 20x20 grid of compartments, with diffusion
for species X, and then simulated using ODEs. Finally, an animation of the simulation is created.
using Catalyst, CairoMakie, OrdinaryDiffEq
# Create `LatticeReactionSystem` model.
brusselator = @reaction_network begin
A, ∅ --> X
1, 2X + Y --> 3X
B, X --> Y
1, X --> ∅
end
diffusion_rx = @transport_reaction D X
lattice = CartesianGrid((20,20))
lrs = LatticeReactionSystem(brusselator, [diffusion_rx], lattice)
# Create a spatial `ODEProblem`.
u0 = [:X => rand(20, 20), :Y => 10.0]
tspan = (0.0, 40.0)
ps = [:A => 1.0, :B => 4.0, :D => 0.2]
oprob = ODEProblem(lrs, u0, tspan, ps)
# Simulate the ODE and plot the results.
sol = solve(oprob, FBDF())
lattice_animation(sol, :X, lrs, "brusselator.mp4")
The addition of spatial modelling in Catalyst contains a large number of new features, all of which are described in the corresponding documentation.
Bug fix to address that independent variables, like time, should now be @parameters
according to MTKv9. Converted internal time variables to consistently use default_t()
to hopefully avoid such issues going forward.
Catalyst v14 was prompted by the (breaking) release of ModelingToolkit v9, which introduced several breaking changes to Catalyst. A summary of these (and how to handle them) can be found here. These are briefly summarised in the following bullet points:
ReactionSystem
s must now be marked complete before they are exposed to most forms of simulation and analysis. With the exception ofReactionSystem
s created through the@reaction_network
macro, allReactionSystem
s are not marked complete upon construction. Thecomplete
function can be used to markReactionSystem
s as complete. To construct aReactionSystem
that is not marked complete via the DSL the new@network_component
macro can be used.- The
states
function has been replaced withunknowns
. Theget_states
function has been replaced withget_unknowns
. - Support for most units (with the exception of
s
,m
,kg
,A
,K
,mol
, andcd
) has currently been dropped by ModelingToolkit, and hence they are unavailable via Catalyst too. Its is expected that eventually support for relevant chemical units such as molar will return to ModelingToolkit (and should then immediately work in Catalyst too). - Problem parameter values are now accessed through
prob.ps[p]
(rather thanprob[p]
). - ModelingToolkit currently does not support the safe application of the
remake
function, or safe direct mutation, for problems for whichremove_conserved = true
was used when updating the values of initial conditions. Instead, the values of each conserved constant must be directly specified. - The
reactionparams
,numreactionparams
, andreactionparamsmap
functions have been deprecated and removed. - To be more consistent with ModelingToolkit's immutability requirement for
systems, we have removed API functions that mutate
ReactionSystem
s such asaddparam!
,addreaction!
,addspecies
,@add_reactions
, andmerge!
. Please useModelingToolkit.extend
andModelingToolkit.compose
to generate new merged and/or composedReactionSystem
s from multiple component systems.
-
default_t()
anddefault_time_deriv()
functions should be used for creating the default time independent variable and its differential. i.e.# do t = default_t() @species A(t) # avoid @variables t @species A(t)
- It is now possible to add metadata to individual reactions, e.g. using:
a more detailed description can be found here.
rn = @reaction_network begin @parameters η k, 2X --> X2, [description="Dimerisation"] end getdescription(rn)
-
SDEProblem
no longer takes thenoise_scaling
argument. Noise scaling is now handled through thenoise_scaling
metadata (described in more detail here) - Fields of the internal
Reaction
structure have been changed.ReactionSystems
s saved usingserialize
on previous Catalyst versions cannot be loaded using this (or later) versions. - A new function,
save_reactionsystem
, which permits the writing ofReactionSystem
models to files, has been created. A thorough description of this function can be found here - Updated how compounds are created. E.g. use
to create a compound species
@variables t C(t) O(t) @compound CO2 ~ C + 2O
CO2
that consists ofC
and twoO
. - Added documentation for chemistry-related functionality (compound creation and reaction balancing).
- Added function
isautonomous
to check if aReactionSystem
is autonomous. - Added function
steady_state_stability
to compute stability for steady states. Example:Here,# Creates model. rn = @reaction_network begin (p,d), 0 <--> X end p = [:p => 1.0, :d => 0.5] # Finds (the trivial) steady state, and computes stability. steady_state = [2.0] steady_state_stability(steady_state, rn, p)
steady_state_stability
takes an optional keyword argumenttol = 10*sqrt(eps())
, which is used to check that the real part of all eigenvalues are at leasttol
away from zero. Eigenvalues withintol
of zero indicate that stability may not be reliably calculated. - Added a DSL option,
@combinatoric_ratelaws
, which can be used to toggle whether to use combinatorial rate laws within the DSL (this feature was already supported for programmatic modelling). Example:# Creates model. rn = @reaction_network begin @combinatoric_ratelaws false (kB,kD), 2X <--> X2 end
- Added a DSL option,
@observables
for creating observables (this feature was already supported for programmatic modelling). - Added DSL options
@continuous_events
and@discrete_events
to add events to a model as part of its creation (this feature was already supported for programmatic modelling). Example:rn = @reaction_network begin @continuous_events begin [X ~ 1.0] => [X ~ X + 1.0] end d, X --> 0 end
- Added DSL option
@equations
to add (algebraic or differential) equations to a model as part of its creation (this feature was already supported for programmatic modelling). Example:couples the ODErn = @reaction_network begin @equations begin D(V) ~ 1 - V end (p/V,d/V), 0 <--> X end
$dV/dt = 1 - V$ to the reaction system. - Coupled reaction networks and differential equation (or algebraic differential
equation) systems can now be converted to
SDESystem
s andNonlinearSystem
s.
- Added CatalystStructuralIdentifiabilityExtension, which permits
StructuralIdentifiability.jl to be applied directly to Catalyst systems. E.g.
use
to assess (global) structural identifiability for all parameters and variables of the
using Catalyst, StructuralIdentifiability goodwind_oscillator = @reaction_network begin (mmr(P,pₘ,1), dₘ), 0 <--> M (pₑ*M,dₑ), 0 <--> E (pₚ*E,dₚ), 0 <--> P end assess_identifiability(goodwind_oscillator; measured_quantities=[:M])
goodwind_oscillator
model (under the presumption that we can measureM
only). - Automatically handles conservation laws for structural identifiability problems (eliminates these internally to speed up computations).
- A more detailed of how this extension works can be found here.
- Add a CatalystBifurcationKitExtension, permitting BifurcationKit's
BifurcationProblem
s to be created from Catalyst reaction networks. Example usage:using Catalyst wilhelm_2009_model = @reaction_network begin k1, Y --> 2X k2, 2X --> X + Y k3, X + Y --> Y k4, X --> 0 k5, 0 --> X end using BifurcationKit bif_par = :k1 u_guess = [:X => 5.0, :Y => 2.0] p_start = [:k1 => 4.0, :k2 => 1.0, :k3 => 1.0, :k4 => 1.5, :k5 => 1.25] plot_var = :X bprob = BifurcationProblem(wilhelm_2009_model, u_guess, p_start, bif_par; plot_var = plot_var) p_span = (2.0, 20.0) opts_br = ContinuationPar(p_min = p_span[1], p_max = p_span[2], max_steps = 1000) bif_dia = bifurcationdiagram(bprob, PALC(), 2, (args...) -> opts_br; bothside = true) using Plots plot(bif_dia; xguide = "k1", guide = "X")
- Automatically handles elimination of conservation laws for computing bifurcation diagrams.
- Updated Bifurcation documentation with respect to this new feature.
- Added a CatalystHomotopyContinuationExtension extension, which exports the
hc_steady_state
function if HomotopyContinuation is exported.hc_steady_state
finds the steady states of a reaction system using the homotopy continuation method. This feature is only available for julia versions 1.9+. Example:
wilhelm_2009_model = @reaction_network begin
k1, Y --> 2X
k2, 2X --> X + Y
k3, X + Y --> Y
k4, X --> 0
end
ps = [:k1 => 8.0, :k2 => 2.0, :k3 => 1.0, :k4 => 1.5]
hc_steady_states(wilhelm_2009_model, ps)
- Added the ability to create species that represent chemical compounds and know
their constituents. For example, water can be created and queried as
@variables t @species H(t) O(t) @compound H2O(t) 2*H O iscompound(H2O) == true isspecies(H2O) == true # compounds are also species, so can be used in reactions isequal(components(H2O), [H, O]) coefficients(H2O) == [2, 1]
- Added reaction balancing via the
balance_reaction
command, which returns a vector of balanced reaction versions, i.e.@variables t @species H(t) O(t) C(t) @compound CH4(t) C 4H @compound O2(t) 2O @compound CO2(t) C 2O @compound H2O(t) 2H O # unbalanced reaction to balance rx = Reaction(1.0, [CH4, O2], [CO2, H2O]) # calculate a balanced version, this returns a vector # storing a single balanced version of the reaction in this case brxs = balance_reaction(rx) # what one would calculate by hand balanced_rx = Reaction(1.0, [CH4, O2], [CO2, H2O], [1, 2], [1, 2]) # testing equality @test isequal(balanced_rx, first(brxs))
- Note that balancing works via calculating the nullspace of an associated
integer matrix that stores in entry
(i,j)
a signed integer representing the number of times thei
'th atom appears within thej
th compound. The entry is positive for a substrate and negative for a product. One cannot balance a reaction involving compounds of compounds currently. A non-empty solution vector is returned if the reaction can be balanced in exactly one way with minimal coefficients while preserving the set of substrates and products, i.e. if the dimension of the nullspace is one. If the dimension is greater than one we return aReaction
for each nullspace basis vector, but note that they may currently interchange substrates and products (i.e. we do not solve for if there is a linear combination of them that preserves the set of substrates and products). An emptyReaction
vector indicates it is not possible to balance the reaction.
- Array parameters, species, and variables can be use in the DSL if explicitly
declared with
@parameters
,@species
, or@variables
respectively, i.e.rn = @reaction_network begin @parameters k[1:2] a @variables (V(t))[1:2] W(t) @species (X(t))[1:2] Y(t) k[1]*a+k[2], X[1] + V[1]*X[2] --> V[2]*W*Y + B*C end
- Non-species states can be declared in the DSL using
@variables
, and custom independent variables (instead of justt
) using@ivs
. For the latter, the first independent variable is always interpreted as the time variable, and all discovered species are created to be functions of all theivs
. For example inrn = @reaction_network begin @ivs s x @variables A(s) B(x) C(s,x) @species D(s) E(x) F(s,x) k*C, A*D + B*E --> F + H end
s
will be the time variable,H = H(s,x)
will be made a function ofs
andx
, andA(s)
,B(x)
, andC(s,x)
will be non-species state variables. Catalyst.isequal_ignore_names
has been deprecated forisequivalent(rn1, rn2)
to test equality of two networks and ignore their name. To include names in the equality check continue to usern1 == rn2
or useisequivalent(rn1, rn2; ignorenames = false)
.
-
BREAKING: Parameters should no longer be listed at the end of the DSL macro, but are instead inferred from their position in the reaction statements or via explicit declarations in the DSL macro. By default, any symbol that appears as a substrate or product is a species, while any other is a parameter. That is, parameters are those that only appear within a rate expression and/or as a stoichiometric coefficient. E.g. what previously was
using Catalyst rn = @reaction_network begin p, 0 --> X d, X --> 0 end p d
is now
using Catalyst rn = @reaction_network begin p, 0 --> X d, X --> 0 end
More generally, in the reaction system
rn = @reaction_network begin k*k1*A, A --> B k2, k1 + k*A --> B end
k
andk2
are inferred as parameters by the preceding convention, whileA
,B
andk1
are species. -
Explicit control over which symbols are treated as parameters vs. species is available through the new DSL macros,
@species
and@parameters
. These can be used to designate when something should be a species or parameter, overriding the default DSL assignments. This allows setting that a symbol which would by default be interpreted as a parameter should actually be a species (or vice-versa). E.g. in:using Catalyst rn = @reaction_network begin @species X(t) k*X, 0 --> Y end
X
andY
will be considered species, whilek
will be considered a parameter. These options take the same arguments as standalone the@species
(i.e.ModelingToolkit.@variables
) andModelingToolkit.@parameters
macros, and support default values and setting metadata. E.g you can set default values using:using Catalyst rn = @reaction_network begin @species X(t)=1.0 @parameters p=1.0 d=0.1 p, 0 --> X d, X --> 0 end
or designate a parameter as representing a constant species using metadata:
using Catalyst rn = @reaction_network begin @parameters Y [isconstantspecies=true] k, X + Y --> 0 end
-
BREAKING: A standalone
@species
macro was added and should be used in place of@variables
when declaring symbolic chemical species, i.e.@parameters k @variables t @species A(t) B(t) rx = Reaction(k, [A], [B]) @named rs = ReactionSystem([rx], t)
This will no longer work as substrates and products must be species
@parameters k @variables t A(t) B(t) rx = Reaction(k, [A], [B]) # errors as neither A or B are species rx = Reaction(k, [A], nothing) # errors as A is not a species rx = Reaction(k, nothing, [B]) # errors as B is not a species # this works as the rate or stoichiometry can be non-species @species C(t) D(t) rx = Reaction(k*A, [C], [D], [2], [B]) @named rs = ReactionSystem([rx], t)
@variables
is now reserved for non-chemical species state variables (for example, arising from constraint equations). Internally, species are normal symbolic variables, but with added metadata to indicate they represent chemical species. -
To check if a symbolic variable is a species one can use
isspecies
:@variables t @species A(t) @variables B(t) isspecies(A) == true isspecies(B) == false
-
BREAKING: Constraint subsystems and the associated keyword argument to
ReactionSystem
have been removed. Instead, one can simply add ODE or algebraic equations into the list ofReaction
s passed to aReactionSystem
. i.e. this should now work@parameters k α @variables t V(t) @species A(t) rx = Reaction(k*V, nothing, [A]) D = Differential(t) eq = D(V) ~ α @named rs = ReactionSystem([rx, eq], t) osys = convert(ODESystem, rs)
which gives the ODE model
julia> equations(osys) 2-element Vector{Equation}: Differential(t)(A(t)) ~ k*V(t) Differential(t)(V(t)) ~ α
Mixing ODEs and algebraic equations is allowed and should work when converting to an
ODESystem
orNonlinearSystem
(if only algebraic equations are included), but is not currently supported when converting toJumpSystem
s orSDESystem
s. -
API functions applied to a
ReactionSystem
,rs
, now have:species(rs)
give the chemical species of a system.states(rs)
give all the variables, both chemical species and non-chemical species of a system.
Catalyst now orders species before non-species in
states(rs)
such thatstates(rs)[1:length(species(rs))]
andspecies(rs)
should be the same. Similarly:equations(rs)
gives the set ofReaction
s andEquation
s of a system.reactions(rs)
gives theReaction
s of a system.
As with species,
Reaction
s are always ordered beforeEquation
s so thatequations(rs)[1:length(reactions(rs))]
should be the same ordered list ofReaction
s as given byreactions(rs)
. -
Catalyst has been updated for Symbolics v5, and requires Symbolics v5.0.3 or greater and ModelingToolkit v8.47.0 or greater.
-
The accessors for a given system,
rs
, that return the internal arrays at the top-level (i.e. ignoring sub-systems) now haveModelingToolkit.get_states(rs)
to get the list of all species and non-species variables.Catalyst.get_species(rs)
to get the list of all species variables. Note thatget_states(rs)[1:length(get_species(rs))]
should be the same ordered list of species asget_species(rs)
.ModelingToolkit.get_eqs(rs)
gives the list of allReaction
s and thenEquation
s in the system.Catalyst.get_rxs(rs)
gives the list of allReaction
s, such thatget_eqs(rs)[1:length(get_rx(rs))]
is the same ordered list ofReaction
s as returned byget_rxs(rs)
.
-
BREAKING: Chemical species specified or inferred via the DSL are now created via the same mechanism as
@species
, and therefore have the associated metadata that is missing from a normal symbolic variable. -
Deprecated functions
params
andmerge
have been removed. -
BREAKING: The old notation for the constants representing conserved quantities,
_Conlaw
, has been replaced with uppercase unicode gamma, "Γ". This can be entered in notebooks, the REPL, or many editors by typing the corresponding Latex command, "\Gamma", and hitting tab. This leads to much cleaner equations when Latexifying systems where conservation laws have been applied. The underlying symbol can also be accessed viaCatalyst.CONSERVED_CONSTANT_SYMBOL
. -
Modelingtoolkit symbolic continuous and discrete events are now supported when creating
ReactionSystem
s via thecontinuous_events
anddiscrete_events
keyword arguments. As in ModelingToolkit, species, states, and parameters that appear only within events are not detected automatically, and hence the four-argumentReactionSystem
constructor, where states and parameters are explicitly passed, must be used unless every variable, state, or parameter in the events appears within aReaction
orEquation
too. See the ModelingToolkit docs for more information on using events. Note thatJumpSystem
s only support discrete events at this time.
- Support for states/species that are functions of multiple variables. This
enables (symbolically) building PDEs to solve with
MethodOfLines. To use multiple
independent variables one can say:
The
using Catalyst using ModelingToolkit: scalarize @parameters k[1:7] @variables t x y U(x,y,t) V(x,y,t) W(x,y,t) rxs = [Reaction(k[1], [U, W], [V, W]), Reaction(k[2], [V], [W], [2], [1]), Reaction(k[3], [W], [V], [1], [2]), Reaction(k[4], [U], nothing), Reaction(k[5], nothing, [U]), Reaction(k[6], [V], nothing), Reaction(k[7], nothing, [V])] pars = scalarize(k) @named rn = ReactionSystem(rxs, t, [U, V, W], pars; spatial_ivs = [x, y])
spatial_ivs
keyword lets Catalyst know which independent variables correspond to spatial variables. Note that rate expressions can depend onx
andy
too, i.e.k[1] * x + y*t
would be valid. See the work in progress PDE tutorial to solve the resulting system and add spatial transport.
- API functions to generate substrate, product, and net stoichiometry matrices should now work with floating point stoichiometric coefficients. Note, symbolic coefficients are still not supported by such functions.
- BREAKING: Modified how constant and boundary condition species (in the
SBML sense) work. Constant species should now be specified as ModelingToolkit
@parameters
with theisconstantspecies=true
metadata, while non-constant boundary condition species should be specified as ModelingToolkit@variables
with theisbcspecies=true
metadata. As before, boundary condition species are treated as constant with respect to reactions, but since they are considered variables their dynamics should be defined in a constraint system. Moreover, it is required that BC species appear in a balanced manner (i.e. in each reaction for which a BC species is a reactant it must appear as a substrate and a product with the same stoichiometry). Right now only conversion ofReactionSystem
s to anODESystem
with a constraintODESystem
orNonlinearSystem
, or conversion to aNonlinearSystem
with a constraintNonlinearSystem
, are supported. Constraints are not supported inSDESystem
orJumpSystem
conversion, and so boundary condition species are effectively constant when converting to those model types (but still left as states instead of parameters). Defining constant and boundary condition species is done byHere@parameters k A [isconstantspecies=true] @variables t B(t) [isbcspecies=true] C(t) rx = Reaction(k, [A,B], [B,C], [1,2], [1,1])
A
is a constant species,B
is a non-constant boundary condition species, andC
is a normal species. Constant and boundary condition species can be used in creatingReaction
s like normal species as either substrates or products. Note that network API functions such asnetstoichmat
,conservationlaws
, orreactioncomplexes
ignore constant species. i.e. forA
a constant species the reaction2A + B --> C
is treated as equivalent toB --> C
with a modified rate constant, whileB --> A
would be identical toB --> 0
. Boundary condition species are checked to be balanced by default whenReactionSystem
s are constructed, i.e.would error sincerx = Reaction(k, [A,B], [C], [1,2], [1]) @named rs = ReactionSystem(rs, t)
B
only appears as a substrate. This check can be disabled withNote that network analysis functions assume BC species appear in a balanced manner, so may not work correctly if one appears in an unbalanced fashion. (Conversion to other system types should still work just fine.)@named rs = ReactionSystem(rs, t; balanced_bc_check=false)
- BREAKING: Added the ability to eliminate conserved species when generating
ODEs, nonlinear problems, SDEs, and steady state problems via the
remove_conserved=true
keyword that can be passed toconvert
or toODEProblem
,NonlinearProblem
,SDEProblem
, orSteadyStateProblem
when called with aReactionSystem
. For example,givesrn = @reaction_network begin k, A + B --> C k2, C --> A + B end k k2 osys = convert(ODESystem, rn; remove_conserved=true) equations(osys)
Initial conditions should still be specified for all the species inDifferential(t)(A(t)) ~ k2*(_ConLaw[2] - A(t)) - k*(A(t) + _ConLaw[1])*A(t)
rn
, and the conserved constants will then be calculated automatically. Eliminated species are stored as observables inosys
and still accessible via solution objects. Breaking as this required modifications to theReactionSystem
type signature. - BREAKING: Added an internal cache in
ReactionSystem
s for network properties, and revamped many of the network analysis functions to use this cache (so just aReactionSystem
can be passed in). Most of these functions will now only calculate the chosen property the first time they are called, and in subsequent calls will simply returned that cached value. Callreset_networkproperties!
to clear the cache and allow properties to be recalculated. The new signatures forrn
aReactionSystem
areBreaking as this required modifications to thereactioncomplexmap(rn) reactioncomplexes(rn) complexstoichmat(rn) complexoutgoingmat(rn) incidencemat(rn) incidencematgraph(rn) linkageclasses(rn) deficiency(rn) sns = subnetworks(rn) linkagedeficiencies(rn) isreversible(rn) isweaklyreversible(rn, sns)
ReactionSystem
type signature. - BREAKING
ReactionSystem
s now store a default value forcombinatoric_ratelaws=true
. This default value can be set in theReactionSystem
constructor call as a keyword argument. Passingcombinatoric_ratelaws
as a keyword toconvert
or problem calls involving aReactionSystem
is still allowed, and will override theReactionSystem
's default. - Fixed a bug where
ODESystem
constraint systems did not propagatecontinuous_events
during calls toconvert(ODESystem, rn::ReactionSystem)
. - Added constant and boundary condition species (in the SBML sense). During
conversion constant species are converted to parameters, while boundary
condition species are kept as state variables. Note that boundary condition
species are treated as constant with respect to reactions, so their dynamics
must be defined in a constraint system. Right now only conversion of
ReactionSystem
s to anODESystem
with a constraintODESystem
orNonlinearSystem
, or conversion to aNonlinearSystem
with a constraintNonlinearSystem
, are supported. Constraints are not supported inSDESystem
orJumpSystem
conversion, and so boundary condition species are effectively constant when converting to those model types (but still left as states instead of parameters). Defining constant and boundary condition species is done byHere@variables t A(t) [isconstant=true] B(t) [isbc=true] C(t)
A
is a constant species,B
is a boundary condition species, andC
is a normal species. Note that network API functions do not make use of these labels, and treat all species as normal -- these properties are only made use of when converting to other system types.
-
Added the ability to use symbolic stoichiometry expressions via the DSL. This should now work
rn = @reaction_network rs begin t*k, (α+k+B)*A --> B 1.0, α*A + 2*B --> k*C + α*D end k α
Here Catalyst will try to preserve the order of symbols within an expression, taking the rightmost as the species and everything multiplying that species as stoichiometry. For example, we can interpret the above reaction as
S1 A --> S2 b
whereS1 = (α+k+B)
is the stoichiometry of the reactantA
and1
is the stoichiometry of the reactantB
. Forrn = @reaction_network rs begin 1.0, 2X*(Y + Z) --> XYZ end
all of
X
,Y
andZ
will be registered as species, with substrates(Y,Z)
having associated stoichiometries of(2X,2X)
. As for rate expressions, any symbols that appear and are not defined as parameters will be declared to be species.In contrast, when declaring reactions
rx = @reaction t*k, (k+α)*A --> B
will work, with every symbol declared a parameter except the leftmost symbol in the reaction line. So
rx = @reaction 1.0, 2X*(Y + Z) --> XYZ
will make
X
a parameter andY
,Z
andXYZ
species. -
Symbolic stoichiometry supports interpolation of expressions in
@reaction_network
and@reaction
.
- Added the ability to use symbolic variables, parameters and expressions for
stoichiometric coefficients. See the new tutorial on Parametric
Stoichiometry for
details, and note the caveat about ModelingToolkit converting integer
parameters to floating point types that must be worked around to avoid calls
to
factorial
that involvefloat
s.
- Added the ability to use floating point stoichiometry (currently only tested
for generating ODE models). This should now work
or directly
rn = @reaction_network begin k, 2.5*A --> 3*B end k
Note, when using@parameters k b @variables t A(t) B(t) C(t) D(t) rx1 = Reaction(k,[B,C],[B,D], [2.5,1],[3.5, 2.5]) rx2 = Reaction(2*k, [B], [D], [1], [2.5]) rx3 = Reaction(2*k, [B], [D], [2.5], [2]) @named mixedsys = ReactionSystem([rx1,rx2,rx3],t,[A,B,C,D],[k,b]) osys = convert(ODESystem, mixedsys; combinatoric_ratelaws=false)
convert(ODESystem, mixedsys; combinatoric_ratelaws=false)
thecombinatoric_ratelaws=false
parameter must be passed. This is also true when callingODEProblem(mixedsys,...; combinatoric_ratelaws=false)
. This disables Catalyst's standard rescaling of reaction rates when generating reaction rate laws, see the docs. Leaving this out for systems with floating point stoichiometry will give an error message.
- Added
@reaction
macroHererx = @reaction k*v, A + B --> C + D # is equivalent to @parameters k v @variables t A(t) B(t) C(t) D(t) rx == Reaction(k*v, [A,B], [C,D])
k
andv
will be parameters andA
,B
,C
andD
will be variables. Interpolation of existing parameters/variables also worksAny symbols arising in the rate expression that aren't interpolated are treated as parameters, while any in the reaction part (@parameters k b @variables t A(t) ex = k*A^2 + t rx = @reaction b*$ex*$A, $A --> C
A + B --> C + D
) are treated as species.
- Added
symmap_to_varmap
,setdefaults!
, and updated all*Problem(rn,...)
calls to allow setting initial conditions and parameter values using symbol maps. See the Catalyst API for details. These allow using regular JuliaSymbols
to specify parameter values and initial conditions. i.e. to set defaults we can doTo explicitly pass initial conditions and parameters using symbols we can dorn = @reaction_network begin α, S + I --> 2I β, I --> R end α β setdefaults!(rn, [:S => 999.0, :I => 1.0, :R => 0.0, :α => 1e-4, :β => .01]) op = ODEProblem(rn, [], (0.0,250.0), []) sol = solve(op, Tsit5())
In each case ModelingToolkit symbolic variables can be used instead ofrn = @reaction_network begin α, S + I --> 2I β, I --> R end α β u0 = [:S => 999.0, :I => 1.0, :R => 0.0] p = (:α => 1e-4, :β => .01) op = ODEProblem(rn, u0, (0.0,250.0), p) sol = solve(op, Tsit5())
Symbol
s, e.g.@parameters α β @variables t S(t) I(t) R(t) setdefaults!(rn, [S => 999.0, I => 1.0, R => 0.0, α => 1e-4, β => .01])
- BREAKING: The order of the parameters in the
ReactionSystem
's.ps
field has been changed (only when created through the@reaction_network
macro). Previously they were ordered according to the order with which they appeared in the macro. Now they are ordered according the to order with which they appeared after theend
part. E.g. inpreviously the order wasrn = @reaction_network begin (p,d), 0 <--> X end d p
[p,d]
, while now it is[d, p]
.
- Added support for
@unpack observable_variable = rn
andrn.observable_variable
. This requires a new inner constructor definition forReactionSystem
s, but is not considered breaking as the inner constructor is considered private. - Support added for ModelingToolkit 7 and Symbolics 4.
-
ReactionSystem(rxs::Vector{Reaction}, t)
should now work and will infer the species and parameters. -
BREAKING: Any undeclared variables in the DSL are now inferred to be
species. i.e. this no longer errors, and
B
is assumed to be a speciesrn = @reaction_network begin k*B, A --> C end k
- BREAKING: Internal changes mean the order of species or parameters in generated systems may have changed. Changes that induce different orders will not be considered breaking in the future.
- Added interpolation in the DSL for species, variables, and the network name.
i.e. this is now valid
@parameters k @variables t, A(t) spec = A rate = k*A name = :network rn = @reaction_network $name begin $rate*B, 2*$spec + B --> $spec + C end
- Added the ability to compose
ReactionSystem
s via subsystems, and include eitherODESystem
s orNonlinearSystem
s as subsystems. Note, if using non-ReactionSystem
subsystems it is not currently possible to convert to aJumpSystem
orSDESystem
. It is also not possible to include eitherSDESystem
s orJumpSystems
as subsystems. - Added
extend(sys, reactionnetwork, name=nameof(sys))
to extendReactionSystem
s with constraint equations (algebraic equations or ODEs), or otherReactionSystem
s. Algebraic or differential constraints are stored as aNonlinearSystem
orODESystem
within theReactionSystem
, and accessible viaget_constraints(reactionnetwork)
. - Added
Catalyst.flatten(rn)
to allow flattening of aReactionSystem
with sub-systems into oneReactionSystem
. Non-ReactionSystem
subsystems are merged into the constraints of the flattenedReactionSystem
, and accessible viaget_constraints
. -
BREAKING:
ReactionSystem
s are now always flattened when callingconvert
. This should only affect models that usesubsystem
s. - Added
incidencematgraph
,linkageclasses
,deficiency
,subnetworks
,linkagedeficiency
,isreversible
andisweaklyreversible
API functions. - Deprecated
merge
, useModelingToolkit.extend
instead. - Deprecated
params
andnumparams
(useModelingToolkit.parameters
to get all parameters of a system and all subsystems, or usereactionparams
to get all parameters of a system and allReactionSystem
subsystems. The latter correspond to those parameters used withinReaction
s.) -
BREAKING: Added a custom
hash
forReaction
s to ensure they work inDict
s andSet
s properly, ensuring set-type comparisons between collections ofReaction
s work. - Updated the docs and added a new tutorial on using compositional tooling.
1. BREAKING: netstoichmat
, prodstoichmat
and substoichmat
are now
transposed to be number of species by number of reactions. This is more
consistent with the chemical reaction network literature for stoichiometry
matrices.
2. reactioncomplexmap
added to provide a mapping from reaction complexes to
reactions they participate in.
3. Most API *mat
functions now take an optional sparse
keyword argument.
If passed sparse=true
a sparse matrix representation is generated, otherwise
the default sparse=false
value returns dense Matrix
representations.
1. Network representations for the reaction complexes of a system along with associated graph functionality:
rn = @reaction_network begin
k₁, 2A --> B
k₂, A --> C
k₃, C --> D
k₄, B + D --> E
k₅, B --> E
k₆, D --> C
end k₁ k₂ k₃ k₄ k₅ k₆
smap = speciesmap(rn)
rcs,B = reactioncomplexes(rn; smap=smap)
Z = complexstoichmat(rn; rcs=rcs)
Δ = complexoutgoingmat(rn; B=B)
complexgraph(rn; complexdata=(rcs,B))
which gives
2. Support for units via ModelingToolkit and
Unitful.jl in directly constructed
ReactionSystem
s:
# ]add Unitful
using Unitful
@parameters α [unit=u"μM/s"] β [unit=u"s"^(-1)] γ [unit=u"μM*s"^(-1)]
@variables t [unit=u"s"] A(t) [unit=u"μM"] B(t) [unit=u"μM"] C(t) [unit=u"μM"]
rxs = [Reaction(α, nothing, [A]),
Reaction(β, [A], [B]),
Reaction(γ, [A,B], [B], [1,1], [2])]
@named rs = ReactionSystem(rxs, t, [A,B,C], [α,β,γ])
By default, during construction of rs
Catalyst will call
validate(rs)
which will print warnings and return false
if either
- The
species(rs)
do not all have the same units. - The implicit (ODE) rate laws for each reaction do not have units of (species
units) / (time units), where the time units are the units of
t
.
(Note, at this time the @reaction_network
macro does not support units.)
3. Calculation of conservation laws
rn = @reaction_network begin
(k₊,k₋), A + B <--> C
end k₊ k₋
clawmat = conservationlaws(netstoichmat(rn))
giving
1 -1 0
0 1 1
and
cquants = conservedquantities(species(rn), clawmat)
giving
A(t) - B(t)
B(t) + C(t)
See the API docs for more details about each of these new features.
1. Basic unit validation has been added following its addition for all ModelingToolkit systems.
1. reactioncomplexes
, ReactionComplex
, reactionrates
, complexstoichmat
and complexoutgoingmat
are added to allow the calculation of reaction complex-based
network matrix representations.
BREAKING: This is a breaking release, with all ModelingToolkit ReactionSystem
and
Reaction
functionality migrated to Catalyst.
1. Plain text arrows "<--" and "<-->" for backward and reversible reactions are available if using Julia 1.6 or higher:
rn = @reaction_network begin
(k1,k2), A + B <--> C
k3, 0 <-- C
end k1 k2 k3
2. BREAKING: Reaction networks can be named
rn = @reaction_network Reversible_Reaction begin
k1, A --> B
k2, B --> A
end k1 k2
ModelingToolkit.nameof(rn) == :Reversible_Reaction
Note, empty networks can no longer be created with parameters, i.e. only
rn = @reaction_network # uses a randomly generated name
rn = @reaction_network MyName # is named MyName
are allowed.
3. Compositional modeling with generated ODESystem
s, see
here
for an example that composes three gene modules to make the repressilator.