.IDEAS.Fluid.HeatExchangers.RadiantSlab.EmbeddedPipe

Embedded pipe model based on EN 15377 and (Koschenz, 2000). The water capacity is lumped to TOut

Information

Dynamic model of an embedded pipe for a concrete core activation. This model is based on (Koschenz, 2000). In addition the model provides the options to simulate the concrete core activation as if there were multiple parallel branches. This affects the pressure drop calculation and also the thermal calculations.

Assumptions and limitations

The implementation of Koschenz mentions that a minimum discretization (i.e. using nDiscr) is required to avoid violation of the second law of thermodynamics. The model explicitly enforces the second law even for nDiscr=1 by upper bounding the heat flow rate such that this minimum discretization does not apply to our implementation. The parameter nDiscr thus only affects the results at larger flow rates. The example IDEAS.Fluid.HeatExchangers.RadiantSlab.Examples.EmbeddedPipeNDiscr provides an indication of the sensitivity of the results to the value of nDiscr.

The embeddedPipe model is designed to be used together with an IDEAS.Buildings.Components.InternalWall. When nDiscr>1, the wall/floor should also be discretized to be physically correct, although the discretizations can also be connected to the same wall/floor, which gives a reasonable approximation as illustrated by the example IDEAS.Fluid.HeatExchangers.RadiantSlab.Examples.EmbeddedPipeNDiscr.

R_x_val represents thermal resistance between the outer pipe wall temperature and the (fictive) uniform TABS temperature. For small concrete/screed layer thicknesses (di ≤ 0.3·T, with T the distance between the pipes), a correction factor needs to be taken into account (see Eq.4-4 and 4-24 in (Koschenz, 2000)).

R_w_val represents the convective thermal resistance between the embedded pipe wall and the water flowing in that pipe. Depending on the Reynolds number rey, laminar or turbulent flow is assumed. For turbulent flow, the convective heat transfer coefficient is determined using a correlation (Eq.4-37) from (Koschenz, 2000). For laminar flow, the convective heat transfer coefficent is calculated using a constant Nusselt number of 4.

Typical use and important parameters

Following parameters need to be set:

Options

By default dp_nominal is calculated by making an estimate of the total pipe length. This pressure drop can be an underestimation of the real pressure drop. The used pipe lengths can be changed in the Pressure drop tab. Parameter dp_nominal can be used to override the default calculation.

Validation

A limited verification has been performed in IDEAS.Fluid.HeatExchangers.RadiantSlab.Examples.EmbeddedPipeVerification.

References

EN 15377, Heating systems in buildings – Design of embedded water-based surface heating and cooling systems., 2008.

M. Koschenz and B. Lehmann, Thermoaktive Bauteilsysteme tabs. Dübendorf, Switzerland: EMPA Energyiesysteme/Haustechnik, 2000, ISBN: 9783905594195.

Transsolar, TRNSYS 16 - A TRaNsient SYstem Simulation program, User Manual. Volume 6: Multizone Building modeling with Type56 and TRNBuild. Madison, 2007.

Revisions


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