Resolve CI failures from new version (1.20.4) of spellchecker

.github/workflows/typos.toml

@@ -38,3 +38,12 @@ astroid = "astroid"
 delt = "delt"
 # TEMPORARY - Remove after example update
 upadate = "upadate"
+
+# false positive from 1.20.3
+RTO = "RTO"
+ans = "ans"
+PN = "PN"
+hd = "hd"
+Tge = "Tge"
+iy = "iy"
+frst = "frst"  # variable name in idaes/core/util/model_serializer.py

docs/reference_guides/model_libraries/generic/costing/process_costing_sslw.rst

@@ -138,7 +138,7 @@ Heat Exchanger Cost
 
 .. note:: IDAES does not yet support costing for heat exchangers requiring both shell and tube area (HX1D).
 
-The purchse cost is computed based on the base unit cost and three correction factors (Eq. 22.43 in Seider et al.), and is adjusted by user-defined currency units with the appropriate CE index value. The base cost is computed depending on the heat exchanger type selected by the user.
+The purchase cost is computed based on the base unit cost and three correction factors (Eq. 22.43 in Seider et al.), and is adjusted by user-defined currency units with the appropriate CE index value. The base cost is computed depending on the heat exchanger type selected by the user.
 
 The heat exchanger costing method has three arguments, hx_type = heat exchanger type, material_type = construction material, and tube_length = tube length ('*' corresponds to the default options):
 

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

@@ -28,7 +28,7 @@ Option 1 - "FTPz":
       	<ul>
  	<li>Total molar flow rate (mol/s) - <code> <font color="red"> flow_mol </font> </code>
  	<li>Temperature (K) - <code> <font color="red"> temperature </font> </code>
-	<li>Presure (Pa) - <code> <font color="red"> pressure</font></code>
+	<li>Pressure (Pa) - <code> <font color="red"> pressure</font></code>
 	<li>Mole fraction of the mixture - <code> <font color="red"> mole_frac_comp</font></code> 
 	</ul>
 	</body>
@@ -43,7 +43,7 @@ Option 2 - "FcTP":
       	<ul>
  	<li>Component molar flow rate (mol/s) - <code> <font color="red"> flow_mol_comp </font> </code>
  	<li>Temperature (K) - <code> <font color="red"> temperature </font> </code>
-	<li>Presure (Pa) - <code> <font color="red"> pressure</font></code>
+	<li>Pressure (Pa) - <code> <font color="red"> pressure</font></code>
 	</ul>
 	</body>
 

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

@@ -183,7 +183,7 @@ List of Variables
    "``fug_phase_comp``", "Fugacity indexed by phase and component", "Pa"
    "``fug_coeff_phase_comp``", "Fugacity coefficient indexed by phase and component", "None"
    "``gibbs_mol_phase``", "Molar Gibbs energy indexed by phase", "J/mol"
-   "``heat_capacity_ratio_phase``", "Heat capcity ratio by phase", "-"
+   "``heat_capacity_ratio_phase``", "Heat capacity ratio by phase", "-"
    "``isothermal_speed_sound_phase``", "Isothermal speed of sound by phase", "m/s"
    "``isentropic_speed_sound_phase``", "Isentropic speed of sound by phase", "m/s"
    "``mw``", "Molecular weight of mixture", "kg/mol"

docs/reference_guides/model_libraries/power_generation/costing/power_plant_costing_netl.rst

@@ -300,7 +300,7 @@ The function has has five arguments, self, equipment, scaled_param, temp_C, and
 * self : an existing unit model or Pyomo Block
 * equipment : The type of equipment to be costed, see table 6
 * scaled_param : The Pyomo Variable representing the component's scaled parameter
-* temp_C : The Pyomo Variable representing the hottest temperature of the piece of equiment being costed. Some pieces of equipment do not have a temperature associated with them, so the default argument is None. This variable must have units of Celsius (Pyomo label `pyunits.C`).
+* temp_C : The Pyomo Variable representing the hottest temperature of the piece of equipment being costed. Some pieces of equipment do not have a temperature associated with them, so the default argument is None. This variable must have units of Celsius (Pyomo label `pyunits.C`).
 * n_equip : The number of pieces of equipment to be costed. The function will evenly divide the scaled parameter between the number passed.
 * CE_index_year : Chemical Engineering Cost Index base year, defaults to 2018; calling the registered Pyomo currency units dictionary of plant cost index values will allow conversion between base years within the flowsheet
 * custom_accounts : Additional accounts to cost

idaes/core/solvers/tests/test_petsc_pid.py

@@ -245,7 +245,7 @@ def inlet_pressure_eqn(b, t):
     assert pyo.value(
         tj2.get_vec(m.fs.valve_1.control_volume.properties_in[24].pressure)[20]
     ) == pytest.approx(6e5)
-    # make sure after the controller comes on the presure goes to the set point
+    # make sure after the controller comes on the pressure goes to the set point
     assert pyo.value(
         tj2.get_vec(m.fs.tank.control_volume.properties_out[24].pressure)[9]
     ) == pytest.approx(3e5)

idaes/models_extra/power_generation/unit_models/boiler_fireside.py

@@ -1018,7 +1018,7 @@ def flow_mass_flyash(b, t):
             return b.flowrate_daf_flyash[t] + b.flowrate_ash[t]
 
     def _make_momentum_balance(self):
-        # flue gas pressure is secondary air presure
+        # flue gas pressure is secondary air pressure
         # - pressure drop through windbox
         # and burner secondary air register
         @self.Constraint(self.flowsheet().time, doc="Flue gas pressure in Pascals")

idaes/models_extra/power_generation/unit_models/boiler_heat_exchanger_2D.py

@@ -2869,7 +2869,7 @@ def sigma_eff_P2(b, t):
 
             # rupture time calculation at crotch corner
             @self.Expression(
-                self.flowsheet().time, doc="Rupture Tme at Crotch Corner for Header"
+                self.flowsheet().time, doc="Rupture Time at Crotch Corner for Header"
             )
             def rupture_time_crotch_corner(b, t):
                 if value(b.sigma_eff_P1[t]) > 10:  # MPa