Feedwatertank4

Created Monday 11 February 2013

A stationary model for a feed water tank computing the corresponding feed water tank pressure, the tapping, the feed water and the condenser mass flow rate and the specific enthalpy at the tank outlet. The component has 4 connectors.

1. Purpose of Model


The model is supposed to be used for the simplified simulation of static cases. Its main purpose is to provide appropriate start or nominal values for similar dynamic model versions.

It computes the stationary values of:


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 L1 because the model only computes a set of parameters for the given scenario.

2.2 Physical Effects Considered


3. Limits of Validity


The model is only able to calculate stationary situations.

4. Interfaces


4.1 Steam Signals


For details see Fundamentals:SteamSignal blue , Fundamentals:SteamSignal green and Fundamentals:SteamSignal red .

Tapping 1 inlet Blue Connector
Tapping 2 inlet: Red connector
Condensate inlet: Blue connector
Condensate outlet: Green connector


4.2 Medium Models


VLE medium model

5. Nomenclature



6. Governing Equations


In general the derived equations for the model consider stationary mass flow balance and momentum.

6.1 Governing Model Equations


The parameter for Feedwater Tank Pressure is modelled using the operating power and the nominal pressure in the tank.

The operating power is also used to implicitly express the mass flow at the outlet of the water tank:

The tapping mas flow rate is given by a ratio between the enthalpies and the condensate mass flow, which follows from an energy balance.

The condensate outlet enthalpy is the bubble enthalpy at the feed water tank pressure,

The pressures at the inlets equal the feedwater tank pressure while the outlet pressure also takes the geodetic pressure difference into account:

Note that the mass balance is not fulfilled by construction, i.e. the sum of inlet mass flows must not equal the outflow mass flow:


Summary

A summary is available including the following:

7. Remarks for Usage


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 Simulationof 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

04.08.2014 - Version:1.0 - Timo Tumforde
06.06.2017 - Version 1.2.2 - Added summary, Timm Hoppe XRG Simulation GmbH