Abstract
The energy needed for the production of domestic hot water (DHW) represents an important share in the total energy demand of well-insulated and airtight buildings. DHW is produced, stored and distributed above 60°C to kill Legionella pneumophila. This elevated temperature is not necessary for DHW applications and has a negative effect on the efficiency of hot water production units.
In this paper, system component models are developed/updated with L. pneumophila growth equations. For that purpose, different existing Modelica pipe and boiler models are investigated to select useful models that could be extended with equations for simulation of bacterial growth. In future research, HVAC designers will be able to investigate the contamination risk for L. pneumophila in the design phase of a hot water system, by implementing the customized pipe and boiler model in a hot water system model. Additionally it will be possible, with simulations, to optimize temperature regimes and estimate the energy saving potential without increasing contamination risk.
Supplemental data
Supplemental data for this article can be accessed at https://doi.org/10.1080/19401493.2019.1583286.
Nomenclature
A(T) [–] | = | Growth function depending on water temperature, the species of the organism and the chemical nature of water |
B(T) [–] | = | Death function depending on water temperature, the species of the organism and the chemical nature of water |
C0 [cfu/m3] | = | Start concentration of L. pneumophila in water entering system |
C(t) [cfu/m3] | = | Concentration of L. pneumophila in water at time t |
Cprevious [cfu/m3] | = | Concentration of L. pneumophila in water on previous timestep. Cprevious = C0 on first timestep. |
Cin(t) [cfu/m3] | = | Concentration of L. pneumophila in water entering system |
Cout(t) [cfu/m3] | = | Concentration of L. pneumophila in water leaving tap |
Cb,in(t) [cfu/m3] | = | Concentration of L. pneumophila. entering biofilm |
Cb,out(t) [cfu/m3] | = | Concentration of L. pneumophila in water leaving biofilm |
Cb(t) [cfu/m3] | = | Concentration of L. pneumophila. in biofilm at time t |
Cb,previous [cfu/m3] | = | Concentration of L. pneumophila in water on previous timestep. Cprevious = C0 on first timestep. |
= | Heat capacity | |
dC(t)/dt [cfu/m3·s] | = | Changing concentration of L. pneumophila over time |
dCb(t)/dt [cfu/m3·s] | = | Changing concentration of L. pneumophila in biofilm over time |
D [m] | = | Tube diameter |
g [m/s2] | = | Acceleration due to gravity |
K [cfu/m3] | = | Carrying capacity |
k [W/m·K] | = | Thermal conductivity |
= | Change in concentration of L. pneumophila. due to growth or starvation | |
= | Change in concentration of L. pneumophila in biofilm due to growth or starvation | |
P [Pa] | = | Total pressure |
Qin(t) [kg/s] | = | Mass flow rate of L. pneumophila in water entering system |
Qout(t) [kg/s] | = | Mass flow rate of L. pneumophila in water leaving tap |
Qb(t) [kg/s] | = | Mass flow rate of L. pneumophila entering/leaving biofilm |
= | Volumetric energy generation rate | |
t [s] | = | Time |
T [K] | = | Absolute temperature |
Vp [m3] | = | Volume of water in pipe |
Vb [m3] | = | Volume of biofilm in pipe |
y [s] | = | Multiplication time of L. pneumophila in water dependent on temperature |
yb [s] | = | Multiplication time of L. pneumophila in biofilm dependent on temperature |
v [m/s] | = | Mass-average velocity for multicomponent mixture |
μ [Pa·s] | = | Viscosity |
ρ [kg/m3] | = | Mass density of mixture |
Φ | = | Function of fluid viscosity and shear strain rates |
ORCID
Elisa Van Kenhove http://orcid.org/0000-0002-4648-0551
Lien De Backer http://orcid.org/0000-0002-0476-3537
Arnold Janssens http://orcid.org/0000-0003-4950-4704
Jelle Laverge http://orcid.org/0000-0002-5334-1314