modelE_Filter_L2_Detailed

Gas || L2 || Detailed E-Filter

Extends from ClaRa.Basics.ControlVolumes.Fundamentals.ChemicalReactions.E_FilterBase, ChemicalReactionsBaseGas (Gas || L2 || Chemical Reactions Base Class).

Information

For detailed model documentation please consult the html-documentation shipped with ClaRa.

Authorship and Copyright Statement for original (initial) Contribution

Author:

References:

For references please consult the html-documentation shipped with ClaRa.

Remarks:

This component was developed by ClaRa development team under the 3-clause BSD License.

Acknowledgements:

ClaRa originated from the collaborative research projects DYNCAP and DYNSTART. Both research projects were supported by the German Federal Ministry for Economic Affairs and Energy (FKZ 03ET2009 and FKZ 03ET7060).

CLA:

The author(s) have agreed to ClaRa CLA, version 1.0. See https://claralib.com/pdf/CLA.pdf

By agreeing to ClaRa CLA, version 1.0 the author has granted the ClaRa development team a permanent right to use and modify his initial contribution as well as to publish it or its modified versions under the 3-clause BSD License.

The ClaRa development team consists of the following partners:

TLK-Thermo GmbH (Braunschweig, Germany)

XRG Simulation GmbH (Hamburg, Germany).

Parameters

Type	Name	Default	Description
Boolean	use_signal (from ChemicalReactionsBaseGas)
Boolean	use_dynamicMassbalance (from ChemicalReactionsBaseGas)
Integer	i (from ChemicalReactionsBaseGas)		Number of separation mas flows involved
Real	epsilon_r	10	Dielectric number of flueGas
Fundamental Definitions
Real	specific_powerConsumption	0.15	Specific power consumption
Geometry
ClaRa.Basics.Units.Area	A_filter	100	Collector area of E-Filter
ClaRa.Basics.Units.Length	d_plate	0.2	Distance Plate-to-Plate or Plate-to-Wire, repectivaly
ClaRa.Basics.Units.Length	diameter_particle	50e-6	Average diameter of ash particles
Real	A1	1.257	Auxiliary Area
Real	A2	0.4	Auxiliary Area
Real	A3	0.55	Auxiliary Area

Components

Type	Name	Description
ClaRa.Basics.Records.IComGas_L2	iCom (from ChemicalReactionsBaseGas)
ClaRa.Basics.Units.HeatFlowRate	Q_flow_reaction (from ChemicalReactionsBaseGas)
ClaRa.Basics.Units.MassFlowRate[i]	m_flow_reaction (from ChemicalReactionsBaseGas)
ClaRa.Basics.Units.MassFraction[iCom.mediumModel.nc - 1]	xi (from ChemicalReactionsBaseGas)
ClaRa.Basics.Units.EnthalpyMassSpecific[i]	h_reaction (from ChemicalReactionsBaseGas)
ClaRa.Basics.Units.MassFraction[iCom.mediumModel.nc - 1]	xi_aux (from ChemicalReactionsBaseGas)
ClaRa.Basics.Units.MassFlowRate	m_flow_aux (from ChemicalReactionsBaseGas)
ClaRa.Basics.Units.EnthalpyMassSpecific	h_aux (from ChemicalReactionsBaseGas)
ClaRa.Basics.Units.Mass	mass (from ChemicalReactionsBaseGas)
Units.Velocity	w_m	Migration speed of dust particles in the E-field
Units.Length	lambda	Mean free path of particles
Modelica.Units.SI.ElectricFieldStrength	E_applied	E-Field in Filter estimated as E = U/d with U being the applied potential and d the distance between elektrodes, refer to Riehle 1997
ClaRa.Basics.Units.DynamicViscosity	mu_flueGas	Dynamic viscosity of flueGas in E-Filter
Real	Cu	Cunningham slip correction factor Cu = 1 + 2lambda/d (A1 +A2exp[-A3diameter_particle/lambda]])
Modelica.Units.SI.ElectricCharge	Q_sat	Saturation charge of particles
Units.Power	powerConsumption	Power consumption
Units.DensityMassSpecific	d_flueGas_in
Units.DensityMassSpecific	d_flueGas_out
Units.MassFraction[iCom.mediumModel.nc - 1]	xi_dust
Real	separationRate	Separation rate
ClaRa.Basics.Units.VolumeFlowRate	V_flow	Volume flow rate of flue Gas entering the E-Filter
Real	U_applied

Revisions

For revisions please consult the html-documentation shipped with ClaRa.