.IBPSA.Fluid.HeatExchangers.ActiveBeams.UsersGuide

Information

This package contains models of active beams. Active beams are devices used for heating, cooling and ventilation of spaces. A schematic diagram of an active beam unit is given below.

The active beam unit consists of a primary air plenum, a mixing chamber, a heat exchanger (coil) and several nozzles. Typically, an air-handling unit supplies primary air to the active beams. The primary air is discharged to the mixing chamber through the nozzles. This generates a low-pressure region which induces air from the room up through the heat exchanger, where hot or cold water is circulating. The conditioned induced air is then mixed with primary air, and the mixture descents back to the space.

This package contains two models. The model IBPSA.Fluid.HeatExchangers.ActiveBeams.Cooling is for cooling only, while the model IBPSA.Fluid.HeatExchangers.ActiveBeams.CoolingAndHeating has two water streams, one for heating and one for cooling.

Model equations for cooling

The performance of the model IBPSA.Fluid.HeatExchangers.ActiveBeams.Cooling is computed based on manufacturer data specified in the package IBPSA.Fluid.HeatExchangers.ActiveBeams.Data.

For off-design conditions, the performance is adjusted using modification factors that account for changes in water flow rate, primary air flow rate and temperature difference. The total heat flow rate of the active beam unit is the sum of the heat flow rate provided by the primary air supply Q_sa and the cooling heat flow rate provided by the beam convector Q_c,Beam which injects room air and mixes it with the primary air.

The heat flow rate Q_sa is delivered to a thermal zone through the fluid ports, while the heat flow rate from the convector Q_c,Beam is coupled directly to the heat port. See for example IBPSA.Fluid.HeatExchangers.ActiveBeams.Examples.CoolingOnly for how to connect these heat flow rates to a control volume.

The primary air contribution is

Q_sa = ṁ_sa c_p,sa (T_sa-T_z)

where ṁ_sa is the primary air mass flow rate, c_p,sa is the air specific heat capacity, T_sa is the primary air temperature and T_z is the zone air temperature.

The heat flow rate of the beam convector Q_c,Beam is determined using the rated capacity which is modified by three separate functions as

Q_c,Beam = Q_c,nominal f_ΔT ( ΔT_c ⁄ ΔT_c,nominal ) f_sa( ṁ_sa ⁄ ṁ_sa,nominal ) f_w( ṁ_c,w ),

the modification factors are as follows: The modification factor f_ΔT(·) describes how the capacity is adjusted to account for the temperature difference between the zone air and the water entering the convector. The independent variable is the ratio between the current temperature difference ΔT_c and the temperature difference used to rate beam performance ΔT_c,nominal. The temperature difference is

ΔT_c = T_cw-T_z,

where T_cw is the chilled water temperature entering the convector. The modification factor f_sa(·) adjusts the cooling capacity to account for varying primary air flow rate. The independent variable is the ratio between the current primary air flow rate ṁ_sa and the nominal air flow rate used to rate the beam performance. The modification factor f_w(·) adjusts the cooling capacity for changes in water flow rate through the convector. The independent variable is the ratio between the current water flow rate ṁ_w and the nominal water flow rate used to rate the beam performance.

Model equations for heating

The performance of the model IBPSA.Fluid.HeatExchangers.ActiveBeams.CoolingAndHeating is computed identical to the above described model that only provides cooling, with the exception that this model contains an additional water stream that can be used to provide heating.

For the heating water stream, the temperature difference ΔT_h used for the calculation of the modification factor f_ΔT(·) is

ΔT_h = T_hw-T_z,

where T_hw is the hot water temperature entering the convector in heating mode and T_z is the zone air temperature.

Dynamics

The model can be configured to be steady-state or dynamic. If configured as dynamic, then a dynamic conservation equation is applied to the water streams for heating and for cooling. However, because the capacity of the beam depends on its inlet temperature, and is independent of the outlet temperature, the heat transferred to the room at the port heaPor.Q_flow, as well as the heat added to or removed from the water streams, will instantaneously change. The only dynamic responses are the water outlet temperatures, which change with a first order response, parameterized with the time constant tau.

Energy balance

All heat flow rate that is added to or extracted from the room is transmitted through the heat port heaPor. Hence, this model does not cool the supply air between the ports air_a and air_b. Rather, it adds this heat flow rate to the heat port heaPor. The rationale for this implementation is that the beam transfers heat by convection directly to the room, and by induction of room air into the supply air. As this split of heat flow rate is generally not known, and because the amount of inducted air is also unknown, it was decided to transfer all heat through the heat port heaPor. This also avoids having to add an extra air flow path for the air induced from the room.