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September 2025 Typos update (#1675)
* September 2025 Typos update * Fix underscore * Random reformatting apparently --------- Co-authored-by: Sufi Kaur <[email protected]>
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.github/workflows/typos.toml

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@@ -43,6 +43,12 @@ fom = "fom"
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# Minimal Infeasible System
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mis = "mis"
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MIS = "MIS"
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# Commonly used in place of type
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typ = "typ"
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# Real heat-exchanger word
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cocurrent = "cocurrent"
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# Used for a regex
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deprecat = "deprecat"
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# false positive from 1.20.3
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RTO = "RTO"

docs/explanations/components/property_package/general_reactions/equil_constant.rst

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@@ -16,7 +16,7 @@ The method uses the van 't Hoff equation to calculate the equilibrium constant.
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.. csv-table::
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:header: "Symbol", "Parameter Name", "Units", "Description"
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":math:`k_{eq, ref}`", "k_eq_ref", "Varies, depends on equilibrium form", "Equlibrium constant at reference temperature"
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":math:`k_{eq, ref}`", "k_eq_ref", "Varies, depends on equilibrium form", "Equilibrium constant at reference temperature"
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":math:`T_{ref, eq}`", "temperature_eq_ref", "Base units", "Reference temperature for calculating equilibrium constant"
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Gibbs Energy (gibbs_energy)

docs/reference_guides/apps/grid_integration/Bidder.rst

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============================================
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The ``PEMParametrizedBidder`` bids the renewable-PEM IES at a constant price.
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The logic of ``PEMParametrizedBidder`` is to reserve a part of the renewable generation
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to co-prodcue the hydrogen. The reserved power can be sold at the marginal cost of the hydrogen
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to co-produce the hydrogen. The reserved power can be sold at the marginal cost of the hydrogen
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price.
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.. autoclass:: PEMParametrizedBidder

docs/reference_guides/configuration.rst

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Changes require ``idaes.reconfig()``. The default setting is ``False``.
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depracation_to_exception
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deprecation_to_exception
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~~~~~~~~~~~~~~~~~~~~~~~~
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If this option is True, any log messages at level warning or above that contain

docs/reference_guides/core/uom.rst

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Unit Sets
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=========
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All property packages within IDAES are expected to define a metadata class as part of the package's ParameterBlock, which among other things contains a definition of the base units of measurement used by that property package. The definition of units of measurement is held wihin a `UnitSet` object that defines a number of common quantities of interest in process applications.
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All property packages within IDAES are expected to define a metadata class as part of the package's ParameterBlock, which among other things contains a definition of the base units of measurement used by that property package. The definition of units of measurement is held within a `UnitSet` object that defines a number of common quantities of interest in process applications.
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An example of defining the default units for a property package is shown below.
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docs/reference_guides/logging.rst

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===================== ====== ============ ============================
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Constant Name Value Name Log Method
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===================== ====== ============ ============================
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CRITICAL 50 CRITICAL ``critial()``
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CRITICAL 50 CRITICAL ``critical()``
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ERROR 40 ERROR ``error()``, ``exception()``
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WARNING 30 WARNING ``warning()``
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INFO_LOW 21 INFO ``info_low()``

docs/reference_guides/model_libraries/generic/property_models/activity_coefficient.rst

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Vapor-Liquid Equilibrium Property Models (Ideal Gas - Non-ideal Liquids)
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=========================================================================
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This property package supports phase equilibrium calucations with a smooth phase transition formulation that makes it amenable for equation oriented optimization. The gas phase is assumed to be ideal and for the liquid phase,
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This property package supports phase equilibrium calculations with a smooth phase transition formulation that makes it amenable for equation oriented optimization. The gas phase is assumed to be ideal and for the liquid phase,
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the package supports an ideal liquid or a non-ideal liquid using an activity
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coefficient model. To compute the activity coefficient, the package currently supports the Non Random Two Liquid Model (NRTL) or the
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Wilson model. Therefore, this property package supports the following combinations for gas-liquid mixtures for VLE calculations:

docs/reference_guides/model_libraries/generic/property_models/helmholtz.rst

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and "Liq". This option requires one of two unit model options to be set. You
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can use the total material balance option for unit models, to specify that only
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one material balance equation should be written not one per phase. The other
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possible option is to specify ``has_phase_equlibrium=True``. This will
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possible option is to specify ``has_phase_equilibrium=True``. This will
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write a material balance per phase, but will add a phase generation term to the
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model. For Helmholtz EoS packages, it is generally recommended that specifying
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total material balances is best because it results in a problem with fewer

docs/reference_guides/model_libraries/generic/property_models/helmholtz_parameters.rst

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IDAES property functions possibly using the expression writer class. The reference enthalpy and
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entropy are chosen arbitrarily. The reference state offset is dimensionless and is added to the
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:math:`n^\circ_1` and :math:`n^\circ_2` parameters in the ideal part for the dimensionless Helmholtz free
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energy corelation.
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energy correlation.
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The following example shows how to set the reference state in the main parameter file::
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docs/reference_guides/model_libraries/power_generation/costing/power_plant_costing_netl.rst

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It is recognized that many users will be unfamiliar with the accounts in the Bituminous Baseline.
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For this reason the cost_accounts argument will also accept a string with the name of a pre-named
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account. Pre-nammed accounts aggregate the relevant accounts for certain systems. The pre-named
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account. Pre-named accounts aggregate the relevant accounts for certain systems. The pre-named
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accounts for each technology can be found in the tables below.
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Table 2. Pre-named Accounts for PC technologies

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