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The form for Jet/Plume the jet and plume boundary condition (Figure 1) features the Current Boundary Cell and Boundary Group Conditions frames similar to the Flow Boundary Conditions form. Although One difference is that in Current Boundary Cell for Jet/Plume, the user must define an upstream cell and a downstream cell simultaneously. In the Jet/Plume Type drop-down menu, the user specifies the flow data of a jet plume boundary to link to with the time series options. These options include by-passing (ICAL=0), using a flow time series (QSER, ICAL=1), and using a withdrawal return time series (W/R, ICAL=2). The Flow Series and W/R Series in Flow Assignment for Cell is enabled according to the Jet/Plume type selected.

In the Entrainment Opt menu the user sets whether to use the maximum of shear and forced entrainment or to use the sum of shear and forced entrainment.

The Entrainment Stop menu provides three options for stopping the entrainment: stop at a specified  From the release of EEMS11.2 WQ constituents may also be added to the plume. 

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Figure 1. Jet /Plume Boundary Condition form.

The Diagnostics drop-down menu allows the user to select from the display jet/plume stop conditions and save jet/plume growth details. The Stop Plume Growth Option allows the simulation to stop after a certain number of elements (ISTJP = 0), stop when the center-line penetrates the bottom of the plume centreline penetrates the surface or bottom (ISTJP = 1), or stop when the boundary penetrates the bottom of plume edge penetrates the surface or bottom (ISTJPISJTP = 2).Other options include setting the Entrainment Error Criteria, which is a factor used in the iterative solution. An adjustment factor for the Froude Number may also be set. The user may also specify the frequency, in the number of time steps, to update the jet/plume calculations, as shown in Figure 2. The neutrally buoyant condition, also shown in Figure 2, applies in all cases. 

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Figure 2. Stop plume growth options.


In the Diffuser Port Settings frame, the user may specify the settings for each discharge cell, including the number of ports, the elevation, and the diameters of the port outlets, as well as the horizontal (azimuth, measured from true north) and vertical (altitude) angles.  It should be noted that the flow in the QSER file is multiplied times the number of ports for the total flow for that BC cell. So, for example, if a user has 10 ports, with each port having a time series of 0.15 cms assigned for the jet, then the total flow is 10 * 0.15 cms = 1.5 cms.

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The Maximum Number of Elements option is mainly used for plume computation termination purposes.  This means that plume growth will always stop when the Maximum Number of Elements is exceeded, which is before reaching the neutral buoyancy level, or the plume reaches the surface (plume density less than ambient) or the bottom (plume density greater than ambient).  It is important not to set this value too small as it will cause the computations to cease before the plume reaches the stop growth option.

The Maximum Number of Iterations is the maximum number of loops to calculate within each step of the element computation. Since there are multiple loops in the jet/plume computation, the actual computation can be time-consuming. Therefore, Number of Time Steps for Update lets users define after how many hydrodynamic time steps EFDC+ should compute the jet/plume result again and update the results. If simulating a uniform flow condition, the number of time steps for each update can be set much greater than in a more complex and changing environment.

In theCalculation Optionmenu, the user can select the Use Max of Shear or  Forced option or Use Sum of Shear & Forced.

An adjustment factor for the Froude Number may also be set.


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titleNote to User

EFDC+ shouldn't be deemed as a local scale jet/plume solver. It is designed for scale from 10~100m or even 1000m where the local momentum effect at the beginning is not as important to the plume growth and the following advection/diffusion transport process. The momentum calculation for the diffuser implementation in EFDC+ does not cross the cell boundary in the current implementation. Furthermore, EFDC+ only distributes the computed ambient water entrainment flow rate along the vertical layers of the cell where the port is located. 



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Figure 1
Figure 1