This technote explains how the Discharge to Atmosphere (D2A) element works and its typical application in HAMMER. It also provides an example model file for demonstration purposes.
The "discharge to Atmosphere" element encompasses a valve to atmosphere, orifice to atmosphere and head vs. flow rating table. It is used to model an opening / orifice that allows flow to leave the pipe network and discharge to the atmosphere. You can model it as a fixed orifice that is always open, or a valve that is either initially open or closed, then opens or closes during the transient simulation. It can be placed in series with the main water line or at a "T"
Note: it is important to understand that this element discharges to atmosphere, not between the adjacent pipes. So in the above case of an in-line orientation, flow still passes through the pipeline beneath the valve, regardless of if the valve is opened or closed.
In the calculation engine, it is essentially modeled as a demand point located a hydraulically short distance from its node coordinates (based on the wave speeds of the pipes connected to it). The initial pressure and flow (entered by the user) are used to automatically calculate a flow emitter (orifice) coefficient (the term CA in the orifice equation below), which will be used during the simulation to calculate transient outflows as the pressure changes. This applies to both the initial conditions (steady state) solver as well as the transient solver (they both use the same resulting pressure/flow relationship) Basically HAMMER uses that coefficient (CA term) to calculate other flows and their corresponding pressure drop:
Q = C A (2 g P)^0.5
Q - Discharge (cfs, cms) C - A 'discharge coefficient' (distinct from CV used elsewhere in HAMMER) which will be computed based on the typical flow/pressureA - The cross-sectional area of the opening (ft, m) - this is combined with the "C" as a single termg - gravitational acceleration P - Pressure head (ft, m)
As you can see, once the "C A" is calculated from the initial head/flow, HAMMER can solve for other flows, as the pressure head changes during the simulation.
Let's take a look at an example, where the "Pressure Drop (typical)" is set to 1 m and the "Flow (typical)" is set to 0.5 m^3/s :
Q = CA (2*g*P)^0.50.5 = CA (19.6)^0.50.5 = CA * 4.4272CA = 0.1129
If the pressure at the D2A is example 1 m, then the outflow is exactly 0.5 m:
Now, say the pressure changes (due to system conditions) from 1 m to 10 m:
Q = CA (2*g*P)^0.5Q = (0.1129) * (2*g*10)^0.5Q = (0.1129) * 196^0.5Q = 1.58 m^3/s
This is the flow you see when the pressure in the model is 10 m:
If the pressure drops below zero (subatmospheric) at the D2A element during the transient simulation, the D2A allows air into the system. When this happens, the air enters the pipeline freely on the assumption that the opening for the liquid is infinite for air. In this case, the node acts like a reservoir at zero pressure and the air pocket respectively expands or contracts accordingly as the liquid flows away from or towards the node, but the air remains at the branch end point(s) located at the D2A. The rate of change of the air volume is based on the water flow rate of the adjacent water column in the pipe. If a check valve further upstream is closed (for example in an upstream pump station at a lower elevation), you may not see any air enter because the water column will not be able to move backwards (or may only be able to move slightly due to the elasticity of the water column.) Similar to an air valve, the admittance of air from a D2A will only be able to help protect the system in the immediate vicinity of the D2A; pressure can still drop further upstream. See further below for details on the application of a D2A for simulating an "inrush" or pipe filling/emptying.
Please also note the following: Assumptions and limitations of tracking air or vapor pockets in HAMMER
A sensitivity analysis wherein the cross sectional area, A is varied would illustrate the consequences of a range of breaks, with an upper limit to A being the diameter of the incoming pipe(s).
The analysis should also consider different locations of the break(s). Depending on the pipe network's topology, a sudden break can lead to the formation of vapor pockets with ensuing collapses and pressure spikes.
As an example, assume a case where you know the flow but not the pressure/head. Say for example the flow is 10 cfs through a 12 inch opening. The velocity in this case would be: V = Q/A = 10 / (pi*0.5^2) = 12.73 ft/s. If you assume C = 0.6, (a typical orifice coefficient, just for example purposes and may not reflect your orifice/opening) you could calculate the corresponding appropriate headloss using the orifice equation relationship: = (V/C)^2 / 2g = (12.73 / 0.6)^2 / (2 * 32.174) = 7 ft. In this example, the "Pressure Drop (Typical)" would be set as 7 ft H2O. HAMMER would then use the orifice equation (see above under "how it works") to compute a change in outflow as the pressure changes. If you already know the flow at a corresponding head, you would simply enter them in the D2A properties and HAMMER will calculate the discharge coefficient internally and use that during the transient simulation to vary outflow with pressure.
Note: The "Gas Volume (Initial)" will impact the timing of the release of the air. The value you enter will be up to your engineering judgment, but a good starting point may be the volume of the "empty" pipe. A larger volume of air for the same size orifice will take longer to be expelled from the D2A. This, in turn, will impact the head increase at the source. The most important impact on the system will occur with the air is fully expelled, which is when the transient would occur. So while a large air volume will take longer to expel, the setup and size of the D2A may prove to the be most important part of the transient event.
Note: the "rating curve" discharge element type is used when the discharge out of your orifice does not follow a typical orifice-equation relationship. It allows you to explicitly define the flow released out of the system for certain pressures at the discharge location.
The following attributes are available when the "discharge element type" is set to "Valve":
"Valve Initial Status" - This specifies whether the valve is initially open or initially closed.
"Time to Start Operating" - The valve starts to operate after this time. (either starts to open or starts to closed, based on the initial status selection) It is measured from the start of the simulation. So a value of 5s means that the valve remains in a fixed position for the first 5 seconds, and then starts to operate.
"Time to Fully Open or Close" - This is the time it takes for the valve to either fully open (if the initial status is closed) or fully close (if the initial status is open. It is measured from the "time to start operating". Meaning, if the "time to start operating" is set to 5s and the "time to fully open or close" is set to 10 seconds, then the valve closes linearly between time t=5 and t=15. (the valve is fully closed 10 seconds after it starts operating).
"Flow (Typical)" - This is the typical discharge out of the valve when it is open.
"Pressure Drop (Typical)" - This is the pressure corresponding to the typical flow through the valve. It is referred to as the "drop" because the pressure beyond the orifice is zero. The pressure and flow computed in the initial conditions will not necessarily be equal to these values, so you only need to enter any known pair. For example, if modeling a hydrant closure, you might enter the typical pressure and flow as the flow and pressure observed in a field test when the hydrant was opened.
You are basically defining an orifice size by way of the "typical" flow and pressure drop fields. By supplying one pair of pressure and flow, HAMMER can figure out the relationship based on the orifice equation that gives the pressure drop for any flow value. So, if unsure, you can use the orifice equation along with the size of your opening and an estimate of the "head" (pressure head drop) to solve for the typical flow. Selecting a pressure head drop close to a typical value you might see under normal operating conditions will yield the most accurate pressure/flow relationship during both the initial conditions and transient simulation. See further above under "How it works".
Note: a standard 2.5 in. (100 mm) hydrant outlet would have a pressure drop of roughly 10 psi at 500 gpm.
When the Discharge Element type is set to "orifice", only the typical pressure drop and typical flow are available. When set to Rating Curve, only a rating curve table is available, where you would enter the table of head versus flow for your discharge. Initial conditions and transient head/flow is computed based on the values in this rating table.
The below model is an example of the use of the D2A element in HAMMER and has several scenarios for different configurations. Note:
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How do do WaterCAD/WaterGEMS treat the discharge to atmosphere element?
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