Lam Res No States $—$ Resistance with laminar flow

The Lam Res No States component describes the laminar flow through a resistance. The flow rate of the resistance is given by

$q=G\mathrm{Δp}$

Variables used in the above equations

 q flow rate $\left[\frac{{m}^{3}}{s}\right]$ G conductance $\left[\frac{{m}^{3}}{s\mathrm{Pa}}\right]$ $\mathrm{Δp}$ pressure drop across resistance $\left[\mathrm{Pa}\right]$

Equations to calculate the conductance G are given in the manual for several components. A conductance of G = 4.167e-13 $\frac{{m}^{3}}{s\mathrm{Pa}}$ leads to a flow rate of 1 $\frac{l}{\mathrm{minute}}$ at 40 $\mathrm{MPa}$. As the critical Reynolds number depends on the component, there is no check whether the flow is actually laminar or turbulent.

 Name Description Resistance with laminar flow and externally commanded conductance. The component, based on the loss coefficient K, describes both flow regimes: laminar for very small Reynolds numbers and turbulent for higher Reynolds numbers (default model). The component describes both flow regimes, using an interpolation polynomial. Orifice component checking for cavitation. Simple textbook component, using a constant discharge coefficient. It is valid for turbulent flow only; severe numerical problems for laminar flow. Metering Orifice (that is, model Orifice No States with variable diameter). Two orifices in series, one with variable the other with fixed flow area. Same as Orifice No States, but with the equations rearranged to compute $\mathrm{Δp}$ for given q.

 Equations $\left\{\begin{array}{cc}\left\{\mathrm{dpeff}=\mathrm{dpacting},\mathrm{dpeffu}=0,\mathrm{pmax}=0,\mathrm{pmin}=0,\mathrm{pminab}=0,\mathrm{alpha_dmax}=0,\mathrm{delta_pk}=0\right\}& \mathrm{checkvalve}\\ \left\{\begin{array}{cc}\left\{\mathrm{dpeff}=\mathrm{noEvent}\left(\left\{\begin{array}{cc}\mathrm{dpeffu}& 0<\mathrm{Δp}\\ -\mathrm{dpeffu}& \mathrm{otherwise}\end{array}\right\\right),\mathrm{dpeffu}=\mathrm{noEvent}\left(\left|\mathrm{pmax}-\mathrm{pmin}\right|\right),\mathrm{pmax}=\mathrm{max}\left({p}_{A\left(\mathrm{limited}\right)},{p}_{B\left(\mathrm{limited}\right)}\right),\mathrm{pmin}=\left\{\begin{array}{cc}\mathrm{pmax}-\mathrm{delta_pk}& \mathrm{pminab}<\mathrm{pmax}-\mathrm{delta_pk}\\ \mathrm{pminab}& \mathrm{otherwise}\end{array}\right\,\mathrm{pminab}=\mathrm{min}\left({p}_{A\left(\mathrm{limited}\right)},{p}_{B\left(\mathrm{limited}\right)}\right),\mathrm{alpha_dmax}=\frac{827}{1000}-\frac{17\ell }{2000\mathrm{D}},\mathrm{delta_pk}={\mathrm{α\left[k\right]}}^{2}{\left(\frac{\sqrt{\mathrm{max}\left(0,\mathrm{pmax}\right)}}{\mathrm{alpha_dmax}}+\frac{10\mathrm{\nu }\left(1+\frac{9\ell }{4\mathrm{D}}\right)\sqrt{2}}{\mathrm{α\left[k\right]}\sqrt{\frac{1}{\mathrm{\rho }}}\mathrm{D}}\right)}^{2}\right\}& \mathrm{cavitation}\\ \left\{\mathrm{dpeff}=\mathrm{Δp},\mathrm{dpeffu}=0,\mathrm{pmax}=0,\mathrm{pmin}=0,\mathrm{pminab}=0,\mathrm{alpha_dmax}=0,\mathrm{delta_pk}=0\right\}& \mathrm{otherwise}\end{array}\right\& \mathrm{otherwise}\end{array}\right\$ $\left\{\begin{array}{cc}\left\{\left\{\begin{array}{cc}\left\{\mathrm{\lambda }=0,\mathrm{qunsigned}=\mathrm{Hydraulics.Restrictions.Basic.PressureDrop.lossCoeff}\left(\mathrm{Δp}=\mathrm{dpeff}-{p}_{\mathrm{open}},{k}_{1}={k}_{1},{k}_{2}={k}_{2},\mathrm{\nu }=\mathrm{\nu },\mathrm{\rho }=\mathrm{\rho },A=A,\mathrm{D}=\mathrm{D},\mathrm{orif}=\mathrm{orif}\right)\right\}& \mathrm{Transition}=1\\ \left[\mathrm{qunsigned},\mathrm{\lambda }\right]=\mathrm{Hydraulics.Restrictions.Basic.PressureDrop.dischargeCoeff}\left(\mathrm{Δp}=\mathrm{dpeff}-{p}_{\mathrm{open}},{C}_{d}={C}_{d},{\mathrm{\lambda }}_{c}={\mathrm{\lambda }}_{c},\mathrm{\nu }=\mathrm{\nu },\mathrm{\rho }=\mathrm{\rho },A=A,\mathrm{D}=\mathrm{D},\mathrm{orif}=\mathrm{orif}\right)& \mathrm{otherwise}\end{array}\right\,\left\{\begin{array}{cc}{q}_{\mathrm{noleak}}=\mathrm{noEvent}\left(\left\{\begin{array}{cc}\mathrm{qunsigned}& 0\le \mathrm{dpeff}-{p}_{\mathrm{open}}\\ 0& \mathrm{otherwise}\end{array}\right\\right)& \mathrm{checkvalve}\\ {q}_{\mathrm{noleak}}=\mathrm{noEvent}\left(\left\{\begin{array}{cc}\mathrm{qunsigned}& 0\le \mathrm{dpeff}-{p}_{\mathrm{open}}\\ -\mathrm{qunsigned}& \mathrm{otherwise}\end{array}\right\\right)& \mathrm{otherwise}\end{array}\right\,\mathrm{q_reg}={q}_{\mathrm{noleak}},{p}_{\mathrm{open}}={p}_{\mathrm{trans}},{q}_{\mathrm{open}}=0\right\}& \mathrm{flowcond}=1\\ \left\{\mathrm{\lambda }=0,\mathrm{q_reg}={q}_{\mathrm{noleak}},\mathrm{qunsigned}=\mathrm{Hydraulics.Restrictions.Basic.PressureDrop.laminar}\left(\mathrm{Δp}=\mathrm{dpeff},G=G\right),{p}_{\mathrm{open}}=0,{q}_{\mathrm{noleak}}=\mathrm{qunsigned},{q}_{\mathrm{open}}=0\right\}& \mathrm{flowcond}=2\\ \left\{\mathrm{\lambda }=0,\mathrm{q_reg}={q}_{\mathrm{noleak}},\mathrm{qunsigned}=\mathrm{Hydraulics.Restrictions.Basic.PressureDrop.dischargeCoeff}\left(\mathrm{Δp}=\mathrm{dpeff},{C}_{d}={C}_{d},\mathrm{flownumber}=\mathrm{false},\mathrm{\rho }=\mathrm{\rho },A=A,\mathrm{D}=\mathrm{D},\mathrm{orif}=\mathrm{orif}\right),{p}_{\mathrm{open}}=0,{q}_{\mathrm{noleak}}=\mathrm{noEvent}\left(\left\{\begin{array}{cc}\mathrm{qunsigned}& 0\le \mathrm{dpeff}\\ -\mathrm{qunsigned}& \mathrm{otherwise}\end{array}\right\\right),{q}_{\mathrm{open}}=0\right\}& \mathrm{flowcond}=3\\ \left\{\left\{\begin{array}{cc}{q}_{\mathrm{noleak}}=\mathrm{noEvent}\left(\left\{\begin{array}{cc}\mathrm{smooth}\left(0,\left\{\begin{array}{cc}\mathrm{qunsigned}& {p}_{\mathrm{open}}<\mathrm{dpeff}\\ \mathrm{q_reg}& \mathrm{otherwise}\end{array}\right\\right)& 0\le \mathrm{dpeff}-{p}_{\mathrm{closed}}\\ 0& \mathrm{otherwise}\end{array}\right\\right)& \mathrm{checkvalve}\\ {q}_{\mathrm{noleak}}=\mathrm{noEvent}\left(\left\{\begin{array}{cc}\mathrm{smooth}\left(0,\left\{\begin{array}{cc}\mathrm{qunsigned}& {p}_{\mathrm{open}}<\mathrm{dpeff}\\ \mathrm{q_reg}& \mathrm{otherwise}\end{array}\right\\right)& 0\le \mathrm{dpeff}-{p}_{\mathrm{closed}}\\ \mathrm{smooth}\left(0,\left\{\begin{array}{cc}-\mathrm{qunsigned}& \mathrm{dpeff}<-{p}_{\mathrm{open}}\\ -\mathrm{q_reg}& \mathrm{otherwise}\end{array}\right\\right)& \mathrm{otherwise}\end{array}\right\\right)& \mathrm{otherwise}\end{array}\right\,\left\{\begin{array}{cc}\left\{\left\{\begin{array}{cc}{q}_{\mathrm{open}}=\frac{\left(\frac{1}{G}+\sqrt{\frac{1}{{G}^{2}}+\frac{2{p}_{\mathrm{closed}}\mathrm{\rho }}{{C}_{d}^{2}{A}^{2}}}\right){C}_{d}^{2}{A}^{2}}{\mathrm{\rho }}& \mathrm{Transition}=2\\ {q}_{\mathrm{open}}=\frac{\left(\frac{1}{G}-\frac{\mathrm{\rho }{k}_{1}\mathrm{\nu }}{2\mathrm{D}A}+\sqrt{{\left(-\frac{1}{G}+\frac{\mathrm{\rho }{k}_{1}\mathrm{\nu }}{2\mathrm{D}A}\right)}^{2}+\frac{2{p}_{\mathrm{closed}}\mathrm{\rho }{k}_{2}}{{A}^{2}}}\right){A}^{2}}{\mathrm{\rho }{k}_{2}}& \mathrm{otherwise}\end{array}\right\,\mathrm{\lambda }=0,{p}_{\mathrm{open}}={p}_{\mathrm{closed}}+\frac{{q}_{\mathrm{open}}}{G}\right\}& \mathrm{regparam}=1\\ \left\{\left\{\begin{array}{cc}{p}_{\mathrm{open}}=\mathrm{Hydraulics.Restrictions.Basic.PressureDrop.inv_lossCoeff}\left(q={q}_{\mathrm{open}},{k}_{1}={k}_{1},{k}_{2}={k}_{2},\mathrm{\rho }=\mathrm{\rho },\mathrm{\nu }=\mathrm{\nu },\mathrm{D}=\mathrm{D}\right)& \mathrm{Transition}=1\\ {p}_{\mathrm{open}}=\mathrm{Hydraulics.Restrictions.Basic.PressureDrop.inv_dischargeCoeff}\left(q={q}_{\mathrm{open}},{C}_{d}={C}_{d},\mathrm{\rho }=\mathrm{\rho },\mathrm{D}=\mathrm{D}\right)& \mathrm{otherwise}\end{array}\right\,\mathrm{\lambda }=0,{q}_{\mathrm{open}}=\frac{{\mathrm{Re}}_{\mathrm{trans}}\mathrm{\nu }A}{\mathrm{D}}\right\}& \mathrm{regparam}=2\\ \left\{\left\{\begin{array}{cc}\left\{\mathrm{\lambda }=0,{q}_{\mathrm{open}}=\mathrm{Hydraulics.Restrictions.Basic.PressureDrop.lossCoeff}\left(\mathrm{Δp}={p}_{\mathrm{open}},\mathrm{\rho }=\mathrm{\rho },A=A,\mathrm{D}=\mathrm{D},{k}_{1}={k}_{1},{k}_{2}={k}_{2},\mathrm{\nu }=\mathrm{\nu },\mathrm{orif}=\mathrm{orif}\right)\right\}& \mathrm{Transition}=1\\ \left[{q}_{\mathrm{open}},\mathrm{\lambda }\right]=\mathrm{Hydraulics.Restrictions.Basic.PressureDrop.dischargeCoeff}\left(\mathrm{Δp}={p}_{\mathrm{open}},\mathrm{\rho }=\mathrm{\rho },A=A,\mathrm{D}=\mathrm{D},{C}_{d}={C}_{d},\mathrm{flownumber}=\mathrm{false},\mathrm{orif}=\mathrm{orif}\right)& \mathrm{otherwise}\end{array}\right\,{p}_{\mathrm{open}}={p}_{\mathrm{trans}}\right\}& \mathrm{otherwise}\end{array}\right\,\left[\mathrm{qunsigned},\mathrm{q_reg}\right]=\mathrm{Hydraulics.Restrictions.Basic.PressureDrop.conditionalFlow}\left(\mathrm{Δp}=\mathrm{dpeff},\mathrm{\rho }=\mathrm{\rho },A=A,\mathrm{D}=\mathrm{D},\mathrm{Transition}=\mathrm{Transition},\mathrm{regtype}=\mathrm{regtype},\mathrm{\nu }=\mathrm{\nu },{p}_{\mathrm{closed}}={p}_{\mathrm{closed}},{p}_{\mathrm{open}}={p}_{\mathrm{open}},{q}_{\mathrm{open}}={q}_{\mathrm{open}},{k}_{1}={k}_{1},{k}_{2}={k}_{2},{C}_{d}={C}_{d}\right)\right\}& \mathrm{otherwise}\end{array}\right\$ $\mathrm{\nu }=\mathrm{Modelica.Media.Air.MoistAir.Utilities.spliceFunction}\left(x=\mathrm{Δp},\mathrm{pos}={\mathrm{\nu }}_{\mathrm{oil}}\left(p={p}_{A\left(\mathrm{abs}\right)},T=T,{v}_{\mathrm{air}}={v}_{\mathrm{gas}\left(\mathrm{oil}\right)},{p}_{\mathrm{sat}}={p}_{\mathrm{sat}}\right),\mathrm{neg}={\mathrm{\nu }}_{\mathrm{oil}}\left(p={p}_{B\left(\mathrm{abs}\right)},T=T,{v}_{\mathrm{air}}={v}_{\mathrm{gas}\left(\mathrm{oil}\right)},{p}_{\mathrm{sat}}={p}_{\mathrm{sat}}\right),\mathrm{Δx}=100\right)$ $\mathrm{\rho }=\mathrm{Modelica.Media.Air.MoistAir.Utilities.spliceFunction}\left(x=\mathrm{Δp},\mathrm{pos}={\mathrm{\rho }}_{\mathrm{oil}}\left(p={p}_{A\left(\mathrm{abs}\right)},T=T,{v}_{\mathrm{air}}={v}_{\mathrm{gas}\left(\mathrm{oil}\right)},{p}_{\mathrm{sat}}={p}_{\mathrm{sat}}\right),\mathrm{neg}={\mathrm{\rho }}_{\mathrm{oil}}\left(p={p}_{B\left(\mathrm{abs}\right)},T=T,{v}_{\mathrm{air}}={v}_{\mathrm{gas}\left(\mathrm{oil}\right)},{p}_{\mathrm{sat}}={p}_{\mathrm{sat}}\right),\mathrm{Δx}=100\right)$ $T={T}_{0\left(\mathrm{oil}\right)}+{\mathrm{ΔT}}_{\mathrm{system}}$ $q=\frac{{m}_{\mathrm{flow}\left(A\right)}}{\mathrm{\rho }}$ $q={q}_{\mathrm{noleak}}+{q}_{\mathrm{leak}}$ $\mathrm{Δp}={p}_{A\left(\mathrm{limited}\right)}-{p}_{B\left(\mathrm{limited}\right)}$ ${p}_{A\left(\mathrm{abs}\right)}={p}_{A}+{p}_{\mathrm{atm}\left(\mathrm{oil}\right)}$ ${p}_{A\left(\mathrm{limited}\right)}=\mathrm{max}\left({p}_{A},{p}_{\mathrm{vapour}\left(\mathrm{oil}\right)}-{p}_{\mathrm{atm}\left(\mathrm{oil}\right)}\right)$ ${p}_{B\left(\mathrm{abs}\right)}={p}_{B}+{p}_{\mathrm{atm}\left(\mathrm{oil}\right)}$ ${p}_{B\left(\mathrm{limited}\right)}=\mathrm{max}\left({p}_{B},{p}_{\mathrm{vapour}\left(\mathrm{oil}\right)}-{p}_{\mathrm{atm}\left(\mathrm{oil}\right)}\right)$ ${m}_{\mathrm{flow}\left(A\right)}+{m}_{\mathrm{flow}\left(B\right)}=0$

Variables

 Name Value Units Description Modelica ID $\mathrm{Δp}$ $\mathrm{Pa}$ Pressure drop dp $q$ $\frac{{m}^{3}}{s}$ Flow rate flowing into port_A q ${p}_{A\left(\mathrm{limited}\right)}$ $\mathrm{Pa}$ Limited gauge pressure pA_limited ${p}_{B\left(\mathrm{limited}\right)}$ $\mathrm{Pa}$ Limited gauge pressure pB_limited $\mathrm{\rho }$ $\frac{\mathrm{kg}}{{m}^{3}}$ Upstream density rho $\mathrm{\nu }$ $\frac{{m}^{2}}{s}$ Upstream kinematic viscosity nu ${p}_{A\left(\mathrm{abs}\right)}$ $\mathrm{Pa}$ Absolute pressure pA pA_abs ${p}_{B\left(\mathrm{abs}\right)}$ $\mathrm{Pa}$ Absolute pressure pB pB_abs $T$ $K$ Local temperature T ${p}_{A\left(\mathrm{summary}\right)}$ ${p}_{A}$ $\mathrm{Pa}$ Pressure at port A summary_pA ${p}_{B\left(\mathrm{summary}\right)}$ ${p}_{B}$ $\mathrm{Pa}$ Pressure at port B summary_pB ${\mathrm{Δp}}_{\mathrm{summary}}$ $\mathrm{Δp}$ $\mathrm{Pa}$ Pressure drop summary_dp ${q}_{\mathrm{summary}}$ $q$ $\frac{{m}^{3}}{s}$ Flow rate flowing into port_A summary_q ${P}_{\mathrm{hyd}\left(\mathrm{summary}\right)}$ $-\mathrm{Δp}q$ $W$ Hydraulic Power summary_HP ${p}_{\mathrm{sat}}$ [1] $\mathrm{Pa}$ Gas saturation pressure p_sat ${q}_{\mathrm{leak}}$ ${G}_{\mathrm{leak}}\mathrm{Δp}$ $\frac{{m}^{3}}{s}$ Leakage flow q_leak ${q}_{\mathrm{noleak}}$ $\frac{{m}^{3}}{s}$ Flow rate through component q_noleak $\mathrm{dpeff}$ $\mathrm{Pa}$ Effective pressure drop dpeff $A$ $1$ ${m}^{2}$ Orifice area A $\mathrm{D}$ $1$ $m$ Orifice diameter D ${q}_{\mathrm{open}}$ $\frac{{m}^{3}}{s}$ Flow when fully open orifice q_open ${p}_{\mathrm{open}}$ $\mathrm{Pa}$ Pressure when fully open orifice p_open $\mathrm{dpacting}$ $0$ $\mathrm{Pa}$ Acting, i.e. delayed pressure differential dpacting $G$ $4.2·{10}^{-13}$ $\frac{{m}^{3}}{s\mathrm{Pa}}$ Hydraulic conductance $G=\frac{\mathrm{∂q}}{\mathrm{∂p}}$ G $\mathrm{\lambda }$ Flow coefficient lambda

[1] $\mathrm{oil.gasSaturationPressure}\left(T=T,{v}_{\mathrm{gas}}={\mathrm{oil.v}}_{\mathrm{gas}}\right)$

Connections

 Name Description Modelica ID ${\mathrm{port}}_{A}$ Layout of port where oil flows into an element ($0<{m}_{\mathrm{flow}}$, ${p}_{B}<{p}_{A}$ means $0<\mathrm{Δp}$) port_A ${\mathrm{port}}_{B}$ Hydraulic port where oil leaves the component (${m}_{\mathrm{flow}}<0$, ${p}_{B}<{p}_{A}$ means $0<\mathrm{Δp}$) port_B $\mathrm{oil}$ oil

Parameters

General Parameters

 Name Default Units Description Modelica ID ${\mathrm{ΔT}}_{\mathrm{system}}$ $0$ $K$ Temperature offset from system temperature dT_system

Constant Parameters

 Name Default Units Description Modelica ID $\mathrm{orif}$ [1] Orifice dimension orif $\mathrm{flowcond}$ $2$ Flow condition flowcond $\mathrm{Transition}$ $0$ Transition model Transition reg type $1$ Regularization type regtype reg param $1$ Regularization parameter regparam $\mathrm{cavitation}$ $\mathrm{false}$ Cavitation cavitation $\mathrm{checkvalve}$ $\mathrm{false}$ checkvalve ${k}_{1}$ $1$ Laminar part k1 ${k}_{2}$ $1$ ${k}_{2}=\frac{1}{{C}_{d}^{2}}$ k2 ${C}_{d}$ $1$ Max discharge coefficient C_d ${\mathrm{\lambda }}_{c}$ $1$ Critical flow number lambdac $\ell$ $1$ $m$ Orifice length; $1<\frac{\ell }{d}$ length ${\Re }_{\mathrm{trans}}$ $1$ Transition Reynolds number Re_trans ${p}_{\mathrm{trans}}$ $1$ $\mathrm{Pa}$ Transition pressure p_trans ${p}_{\mathrm{closed}}$ $1$ $\mathrm{Pa}$ Cracking pressure p_closed ${G}_{\mathrm{leak}}$ $0$ $\frac{{m}^{3}}{s\mathrm{Pa}}$ Leakage conductance G_Leak

[1] $\mathrm{Hydraulics.Restrictions.Basic.PressureDrop.orifinput.D}$

Constants

 Name Value Units Description Modelica ID $\mathrm{α\left[k\right]}$ $0.649$ alpha_k