.TRANSFORM.Fluid.Volumes.Pressurizer .TRANSFORM.Fluid.Volumes.PressurizerSpray stream is assumed to be saturated liquid. This means there is no equation for condensing due to spray.... this was causing solver problems... Should be addressed.
This model describes the cylindrical drum of a drum boiler, without assuming thermodynamic equilibrium between the liquid and vapour holdups. Connectors are provided for surgePort inlet, steamPort outlet, downcomer outlet, riser inlet, and blowdown outlet.
The model is based on dynamic mass and energy balance equations of the liquid volume and vapour volume inside the drum. Mass and energy tranfer between the two phases is provided by bulk condensation and surface condensation of the vapour phase, and by bulk boiling of the liquid phase. Additional energy transfer can take place at the surface if the steamPort is superheated.
The riser flowrate is separated before entering the drum, at the vapour pressure. The (saturated) liquid fraction goes into the liquid volume; the (wet) vapour fraction goes into the vapour volume, vith a steamPort quality depending on the liquid/vapour density ratio and on the avr parameter.
The enthalpy of the liquid going to the downcomer is computed by assuming that a fraction of the total mass flowrate (afd) comes directly from the surgePort inlet. The pressure at the downcomer connector is equal to the vapour pressure plus the liquid head.
The metal wall dynamics is taken into account, assuming uniform temperature. Heat transfer takes place between the metal wall and the liquid phase, vapour phase, and external atmosphere, the corresponding heat transfer coefficients being gl, gv, and gext.
The drum level is referenced to the centreline.
The start values of drum pressure, liquid specific enthalpy, vapour specific enthalpy, and metal wall temperature can be specified by setting the parameters p_start, h_liquid_start, h_vapor_start, Tmstart
The following options are available to specify the orientation of the cylindrical drum:
DrumOrientation = 0: horizontal axis. DrumOrientation = 1: vertical axis. | Name | Description |
|---|---|
 DrumType | 1. Select model 2. Set parameters (Total volume must match V_total) |
 BulkEvaporation | Vapor bubble transport from liquid to vapor phase |
 BulkCondensation | Liquid droplet transport from vapor to liquid phase |
 MassTransfer_VL | Vapor-liquid interface mass transport coefficient |
 HeatTransfer_VL | Vapor-liquid interface heet transfer coefficient |
 HeatTransfer_WL | Wall-vapor heat transfer coefficient |
 HeatTransfer_WV | Wall-liquid heat transfer coefficient |