docs: drop non-existant refs to p_int

Author: ven-k

src/Hydraulic/IsothermalCompressible/components.jl

@@ -1,20 +1,17 @@
 
 """
-    Cap(; p_int, name)
+    Cap(; name)
 
 Caps a hydraulic port to prevent mass flow in or out.
 
-# Parameters:
-- `p_int`: [Pa] initial pressure (set by `p_int` argument)
-
 # Connectors:
 - `port`: hydraulic port
 """
 @mtkmodel Cap begin
 
     @variables begin
         p(t), [guess = 0]
-    end 
+    end
 
     @components begin
         port = HydraulicPort()
@@ -28,12 +25,9 @@ Caps a hydraulic port to prevent mass flow in or out.
 end
 
 """
-    Open(; p_int, name)
+    Open(; name)
 
-Provides an "open" boundary condition for a hydraulic port such that mass flow `dm` is non-zero.  This is opposite from an un-connected hydraulic port or the `Cap` boundary component which sets the mass flow `dm` to zero.  
-
-# Parameters:
-- `p_int`: [Pa] initial pressure (set by `p_int` argument)
+Provides an "open" boundary condition for a hydraulic port such that mass flow `dm` is non-zero.  This is opposite from an un-connected hydraulic port or the `Cap` boundary component which sets the mass flow `dm` to zero.
 
 # Connectors:
 - `port`: hydraulic port
@@ -230,12 +224,11 @@ end
 @deprecate Pipe Tube
 
 """
-    FlowDivider(;p_int, n, name)
+    FlowDivider(; n, name)
 
 Reduces the flow from `port_a` to `port_b` by `n`.  Useful for modeling parallel tubes efficiently by placing a `FlowDivider` on each end of a tube.
 
 # Parameters:
-- `p_int`: [Pa] initial pressure
 - `n`: divide flow from `port_a` to `port_b` by `n`
 
 # Connectors:
@@ -738,7 +731,7 @@ end
 """
     SpoolValve2Way(reversible = false; p_s_int, p_a_int, p_b_int, p_r_int, m, g, x_int, Cd, d, name)
 
-2-ways spool valve with 4 ports and spool mass. Fluid flow direction S → A and B → R when `x` is positive and S → B and A → R when `x` is negative. 
+2-ways spool valve with 4 ports and spool mass. Fluid flow direction S → A and B → R when `x` is positive and S → B and A → R when `x` is negative.
 
 # Parameters:
 - `p_s_int`: [Pa] initial pressure for `port_s`
@@ -819,7 +812,7 @@ end
         Cd = 1e4,
         Cd_reverse = Cd,
         name)
-        
+
 Actuator made of two DynamicVolumes connected in opposite direction with body mass attached.
 
 # Features:

src/Hydraulic/IsothermalCompressible/sources.jl

@@ -1,12 +1,12 @@
 """
-    MassFlow(; name, p_int)
+    MassFlow(; name)
 
 Hydraulic mass flow input source
 
 # Connectors:
 
   - `port`: hydraulic port
-  - `dm`: real input 
+  - `dm`: real input
 """
 @mtkmodel MassFlow begin
 
@@ -55,7 +55,7 @@ input pressure source
 
 # Connectors:
 - `port`: hydraulic port
-- `p`: real input 
+- `p`: real input
 """
 @mtkmodel Pressure begin
 

src/Hydraulic/IsothermalCompressible/utils.jl

@@ -4,14 +4,10 @@ regPow(x, a, delta = 0.01) = x * (x * x + delta * delta)^((a - 1) / 2);
 regRoot(x, delta = 0.01) = regPow(x, 0.5, delta)
 
 """
-    HydraulicPort(;p_int, name)
+    HydraulicPort(; name)
 
 Connector port for hydraulic components.
 
-# Arguments:
-
-- `p_int`: [Pa] initial gauge pressure
-
 # States:
 - `p`: [Pa] gauge total pressure
 - `dm`: [kg/s] mass flow
@@ -38,15 +34,15 @@ end
 """
     HydraulicFluid(; density = 997, bulk_modulus = 2.09e9, viscosity = 0.0010016, gas_density = 0.0073955, gas_pressure = -1000, n = 1, let_gas = 1, name)
 
-Fluid parameter setter for isothermal compressible fluid domain.  Defaults given for water at 20°C and 0Pa gage (1atm absolute) reference pressure. Density is modeled using the Tait equation of state.  For pressures below the reference pressure, density is linearly interpolated to the gas state (when `let_gas` is set to 1), this helps prevent pressures from going below the reference pressure.  
+Fluid parameter setter for isothermal compressible fluid domain.  Defaults given for water at 20°C and 0Pa gage (1atm absolute) reference pressure. Density is modeled using the Tait equation of state.  For pressures below the reference pressure, density is linearly interpolated to the gas state (when `let_gas` is set to 1), this helps prevent pressures from going below the reference pressure.
 
 # Parameters:
 
 - `ρ`: [kg/m^3] fluid density at 0Pa reference gage pressure (set by `density` argument)
 - `Β`: [Pa] fluid bulk modulus describing the compressibility (set by `bulk_modulus` argument)
 - `μ`: [Pa*s] or [kg/m-s] fluid dynamic viscosity  (set by `viscosity` argument)
 - `n`: density exponent
-- `let_gas`: set to 1 to allow fluid to transition from liquid to gas (for density calculation only)  
+- `let_gas`: set to 1 to allow fluid to transition from liquid to gas (for density calculation only)
 - `ρ_gas`: [kg/m^3] density of fluid in gas state at reference gage pressure `p_gas` (set by `gas_density` argument)
 - `p_gas`: [Pa] reference pressure (set by `gas_pressure` argument)
 """
@@ -80,12 +76,12 @@ f_turbulent(shape_factor, Re) = (shape_factor / 64) / (0.79 * log(Re) - 1.64)^2
 """
     friction_factor(dm, area, d_h, viscosity, shape_factor)
 
-Calculates the friction factor ``f`` for fully developed flow in a tube such that ``Δp = f \\cdot \\rho \\frac{u^2}{2} \\frac{l}{d_h}`` where 
+Calculates the friction factor ``f`` for fully developed flow in a tube such that ``Δp = f \\cdot \\rho \\frac{u^2}{2} \\frac{l}{d_h}`` where
 
 - ``Δp``: [Pa] is the pressure difference over the tube length ``l``
 - ``\\rho``: [kg/m^3] is the average fluid density
 - ``u``: [m/s] is the average fluid velocity
-- ``l``: [m] is the tube length 
+- ``l``: [m] is the tube length
 
 The friction factor is calculated for laminar and turbulent flow with a transition region between Reynolds number 2000 to 3000.  Turbulent flow equation is for smooth tubes, valid for the Reynolds number range up to 5e6.