Mixer Cost Documentation

docs/technical_reference/costing/mixer.rst

@@ -9,7 +9,18 @@ The following parameters are constructed for the unit on the FlowsheetCostingBlo
 .. csv-table::
    :header: "Description", "Symbol", "Parameter Name", "Default Value", "Units"
 
-   "description", ":math:`Symbol_{example}`", "``parameter_name``", "1", ":math:`\text{dimensionless}`"
+   "**Standard mixer**"
+   "Mixer unit cost", ":math:`C_{mix, standard}`", "``unit_cost``", "361", ":math:`\text{USD}_{2018}\text{/L/s}`"
+
+   "**NaOCl mixer**"
+   "Mixer unit cost", ":math:`C_{mix, NaOCl}`", "``cost``", "5.08", ":math:`\text{USD}_{2018}\text{/m}^{3}\text{/day}`"
+   "NaOCl cost", ":math:`C_{NaOCl}`", "``unit_cost``", "0.23", ":math:`\text{USD}_{2018}\text{/kg}`"
+   "NaOCl purity", ":math:`p_{NaOCl}`", "``purity``", "0.15", ":math:`\text{dimensionless}`"
+
+   "**CaOH2 mixer**"
+   "Mixer unit cost", ":math:`C_{mix, CaOH2}`", "``cost``", "873.911", ":math:`\text{USD}_{2018}\text{/kg/day}`"
+   "CaOH2 cost", ":math:`C_{CaOH2}`", "``unit_cost``", "0.12", ":math:`\text{USD}_{2018}\text{/kg}`"
+   "CaOH2 purity", ":math:`p_{CaOH2}`", "``purity``", "1", ":math:`\text{dimensionless}`"
 
 Costing Method Variables
 ++++++++++++++++++++++++
@@ -19,41 +30,62 @@ The following variables are constructed on the unit block (e.g., m.fs.unit.costi
 .. csv-table::
    :header: "Description", "Symbol", "Variable Name", "Index", "Units"
 
-   "description", ":math:`Symbol_{example}`", "``variable_name``", "[t]", ":math:`\text{dimensionless}`"
+   "Inlet volumetric flow rate", ":math:`Q_{in}`", "``flow_in``", "[t]", ":math:`\text{m}^3\text{/hr}`"
+   "Lime mass flow", ":math:`M_{in}`", "``lime_kg_per_day``", "[t]", ":math:`\text{kg/day}`"
+   "Dosing rate", ":math:`D`", "``dosing_rate``", "[j]", ":math:`\text{kg/s}`"
 
 Capital Cost Calculations
 +++++++++++++++++++++++++
 
-Describe capital costs..keep it concise where possible
+Capital cost is dependent upon the volumetric flow rate, :math:`Q_{in}`, or
+lime mass flow, :math:`M_{in}`, as shown in the equations below.
+
+   "**Standard mixer**"
 
     .. math::
 
-        C_{cap,tot} = C_{cap,example1}+C_{cap,example2}+C_{cap,other}
+        C_{cap,tot} = C_{mix, standard} * Q_{in}
+
+
+   "**NaOCl mixer**"
 
     .. math::
 
-        C_{cap,example1} = fill in equation for each component in total capex equation
+        C_{cap,tot} = C_{mix, NaOCl} * Q_{in}
+
+
+   "**CaOH2 mixer**"
+
+    .. math::
+
+        C_{cap,tot} = C_{mix, CaOH2} * M_{in}
 
 
 Operating Cost Calculations
 +++++++++++++++++++++++++++
 
-Describe operating/maintenance costs..keep it concise where possible
+The total operating cost is dependent upon the dosing rate, :math:`D`, as shown in the equations below.
+
+   "**Standard mixer**"
+
+    .. math::
+
+        C_{op,tot} = 0
+
+   "**NaOCl mixer**"
 
     .. math::
 
-        C_{op,tot} = C_{op,example1}+C_{op,example2}+C_{op,other}
+        C_{op,tot} = D_{NaOCl} * C_{NaOCl} / p_{NaOCl}
+
+   "**CaOH2 mixer**"
 
     .. math::
 
-        C_{op,example1} = fill in equation for each component in total opex equation
+        C_{op,tot} = D_{CaOH2} * C_{CaOH2} / p_{CaOH2}
 
 
 Code Documentation
 ------------------
 
 * :mod:`watertap.costing.unit_models.mixer`
-
-References
-----------
-Aim to include at least one reference in most cases, but delete this section if no references used for cost relationships/default values