FlameRoom L2 Dynamic

Created Tuesday 18 March 2014

A 0d-flame room volume model with dynamic mass and energy balance regarding heat exchange with neighbouring furnace models and boiler casing walls.

1. Purpose of Model

This model is well suited to model the flame room areas of a boiler. In combination with Hopper_L2, Burner L2 Dynamic and FlameRoomWithTubeBundle L2 Dynamic models a 1-dimensional boiler model could be achieved which is discretised in flow direction. Radiative and/or convective heat transfer between linked furnace models or boiler casing walls can be calculated using replaceable models.

2. Level of Detail, Physical Effects Considered and Physical Insight

2.1 Level of Detail

Referring to Brunnemann et al. [1], this model refers to the level of detail L2.

2.2 Physical Effects Considered

this model uses TIL-Media
dynamic conservation of energy (neglecting kinetic energy terms)
dynamic conservation of mass
combustion of unburnt fuel from lower burner or flame room models is considered
outlet composition is calculated according to the elemental composition of the burnt fuel in the replaceable model CoalReactionZone
enthalpy of formation is calculated for an

idealised combustion with the flue gas composition and the elemental composition and the lower heating value of the burnt fuel

the lower heating value of the burnt fuel is given or calculated according to the "Verbandsformel"
calculation of radiative heat transfer between connected models
calculation of radiative or convective heat transfer to boiler casing walls

2.3 Level of Insight

Heat Transfer

The following listed heat transfer models are the recommended ones. Of course other (e.g. generic ones: Generic HT) heat transfer models could be chosen.

top (radiation to neighbored furnace volumes)

Basics:ControlVolumes:Fundamentals:HeatTransport:Gas HT:Radiation:Radiation gas2Gas L2: calculation of radiant heat transfer between furnace models with constant emissivity and absorbance values
Basics:ControlVolumes:Fundamentals:HeatTransport:Gas HT:Radiation:Radiation gas2Gas advanced L2: calculation of radiant heat transfer between furnace models with constant or calculated emissivity and absorbance values (temperature dependent calculation of gas and particle emissivities)

wall (radiation or convection to boiler casing walls) :

Basics:ControlVolumes:Fundamentals:HeatTransport:Gas HT:Radiation:Radiation gas2Wall L2: calculation of radiant heat transfer between furnace model and boiler casing walls with constant emissivity and absorbance values
Basics:ControlVolumes:Fundamentals:HeatTransport:Gas HT:Radiation:Radiation gas2Wall advanced L2: calculation of radiant heat transfer between furnace model and boiler casing walls with constant or calculated emissivity and absorbance values (temperature dependent calculation of gas and particle emissivities)
Basics:ControlVolumes:Fundamentals:HeatTransport:Gas HT:Convection:Convection flatWall L2: calculation of convective heat transfer to boiler casing walls

Pressure Loss

No pressure losses are considered.

The following replaceable models are used to model the combustion of fuel inside the different furnace volume models. The model for the chemical conversion of fuel can be chosen with the replaceable model ChemicalReactions. The models BurningTime and ParticleMigration are used to calculate the amount of fuel burned inside the current furnace volume. If the preset burning time is lower than the time span for the fuel particles needed to travel though the current furnace volume, the complete amount of fuel is burned inside this component. If the burning timer is higher than the particle migration time, unburnt fuel is entering the following downstream furnace model.

Chemical Reaction

CoalReactionZone: calculates the outlet composition for combustion of the used fuel and its elemental composition.

Burning Time

ConstantBurningTime: setting a fixed value for the time needed to burn the whole amount of fuel entering the combustion volume.

Particle Migration

FixedMigrationSpeed: setting a fixed value for the time span needed for particles to travel through the combustion volume.
MeanMigrationSpeed: calculates a mean value for the time span needed for particles to travel through the combustion volume.

3. Limits of Validity

flow in design direction is considered only

4. Interfaces

4.1 Physical Connectors

Basics:Interfaces:FuelSlagFlueGas inlet inlet
Basics:Interfaces:FuelSlagFlueGas outlet outlet

Basics:Interfaces:HeatPort a heat_top
Basics:Interfaces:HeatPort a heat_bottom
Basics:Interfaces:HeatPort a heat_wall

4.2 Medium Models

Gas Medium Model at the inlet and outlet ports and additional ones inside the volume needed for the calculation of combustion processes

5. Nomenclature

6. Governing Equations

6.1 System Description and General model approach

This model is used to build up furnace models with 1-dimensional discretisation and is used together with other models of the furnace package.

This model supports an nonstationary energy and mass balance (only thermal expansion considered) for the flue gas. The amount of burned fuel takes the particle migration time and the burning time from the replaceable model BurningTime into account. The lower heating value of the fuel can either be set in the parameter dialog or is calculated from the fuel's elementary analysis according to the "Verbandsformel" from [?]. Based on the elemental composition of the used fuel and a generalised ideal fuel combustion, the formation enthalpy is calculated to be considered in the energy balance.
All chemical reactions are calculated inside the replaceable model CoalReactionZone which determines the resulting flue gas mixture according to a combustion calculation and fixed parameters for the produced amount of CO and NOx, as well as the fraction of ash turned into slag. The slag moves through the furnace models in reverse direction (downwards). The slag outlet temperature is given by a parameter.

The component exchanges heat flows with up- and downstream models (via the heat ports heat_top and heat_bottom) as well as the surrounding walls (heat_wall) which are calculated with replaceable models for heat transfer correlations. If radiative heat transfer correlations are used inside a 1-dimensional discretised (sequential model arrangement) furnace, radiative heat flows are exchanged between the directly connected models (via heat ports top and bottom) and the surrounding walls (heat port wall). The calculation is performed with view factors which are calculated inside the heat transfer correlations. The following sketch shows the modelling principle for radiative heat transfer between the sequential arranged volumes and the calculation formula for the view factor. The amount of emitted radiation is calculated for a three dimensional volume, but the radiative heat flow between the models is assumed to be exchanged between two flat surfaces with the size of the furnace cross sectional area.

6.2 General Model Equations

In the following equations, ξ describes a vector filled with mass fractions of fuel or gas compositions. The indexed brackets are used to account for a single composition species.

The overall gas mass inside the volume is calculated with the mean value of the the inflowing gas mixture and the bulk density as follows:

The solid particles of fuel (here mainly coal) are neglected.

The nonstationary mass balance for the flue gas is calculated as follows. Except the ash fraction, the amount of burned fuel is added to the flue gas:

with

The mass balances of slag and fuel are modelled stationary and are not effected from the thermal expansion of the flue gas:

The molar low rates of the educts are calculated as follows:

The stoichiometric amount of air required to burn the fuel mass flow (unburnt fuel from lower control volumes) completely (considering the fuel diffusity too) is calculated as follows:

The fuel diffusity is calculated with the dwell time of the flue gas and the burning time of the (coal) particles to estimate the amount of fuel burned inside the control volume.

The dwelltime of the fuel particles is calculated with the migration speed (calculated inside MeanMigrationSpeed for example) :

The amount of air required is calculated with the mass fraction of of oxygen inside the flue gas:

The excess air is calculated as follows:

The lower heating value of the burnt fuel (and the unburnt fuel leaving the volume):

The lower heating value is used to calculate the formation enthalpy of the used fuel. Therefore the flue gas products of an idealised combustion of 1 kg of fuel per second with the given composition are needed which are calculated inside the replaceable model CoalReactionZone. The produced flue gas flow per combustion of 1 kg of fuel per second is calculated as follows:

With the composition:

The formation enthalpy is calculated as follows:

The flue gas enthalpy inside the control volume, which is used to calculate the outlet temperature with a media object, is calculated with the following energy balance:

The resulting flue gas composition after combustion is calculated with the burned fuel mass:

The pressures are calculated with the flue gas pressure losses:

The resulting control volume temperature T_fg(h_fg)as well as the composition ξ_fg are set to the corresponding streaming connectors of the component.

Summary

A summary record is available which bundles important component values.

7. Remarks for Usage

8. Validation

The adiabatic outlet temperature of this model has been validated with Ebsilon calculations at identical boundary conditions.

The image below shows the flue gas temperatures over the furnace height. As can be seen there is a good compliance with the design values.

9. References

[1] Johannes Brunnemann and Friedrich Gottelt, Kai Wellner, Ala Renz, André Thüring, Volker Röder, Christoph Hasenbein, Christian Schulze, Gerhard Schmitz, Jörg Eiden: "Status of ClaRaCCS: Modelling and Simulation of Coal-Fired Power Plants with CO2 capture", 9th Modelica Conference, Munich, Germany, 2012

10. Authorship and Copyright Statement for original (initial) Contribution

Author:
DYNCAP/DYNSTART development team, Copyright 2011 - 2022.
Remarks:
This component was developed during DYNCAP/DYNSTART projects.
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.

11. Version History

2013 - v 0.1 - initial implementation - L. Nielsen, A. Thüring, TLK-Thermo GmbH
26.03.2019 - chattering countermeasures applied (noEvents)
16.07.2019 - introduced pressure state

Backlinks: ClaRa:Components:Furnace:Burner:Burner L2 Dynamic ClaRa:Components:Furnace:Burner:Burner L2 Dynamic fuelDrying ClaRa:Components:Furnace:FlameRoom:FlameRoomWithTubeBundle L2 Dynamic ClaRa:Components:Furnace:FlameRoom:FlameRoom L2 Static