| Literature DB >> 35708774 |
Abstract
Heat transfer is key to the survival of honey bee colonies (Apis mellifera L.) in the wide range of hot (e.g. sub-Saharan) and cool climates (e.g. maritime-temperate) in which they have evolved and adapted. Here, a validated computational fluid dynamics, conjugate heat transfer model was used to determine the heat transfer of honey bee colonies in simulated standard wooden hives, complete with combs and brood, for a broad range of honey bee sizes, from slender lowland African A.m. scutellata, to broader (larger diameter) Northern European A.m. mellifera, across the whole range of brood covering honey bee densities, as well as when evenly distributed throughout the hive. It shows that under cooling stress, brood covering, broad subspecies need less than a third of the number of bees per unit of brood area for thermal insulation compared to slender subspecies. Also, when distributed evenly around the nest, broad subspecies lose less brood heat than when brood covering. These simulations demonstrate that honey bee girth has climate-based evolutionary advantages directly for the colony as well as via the survival of the individual. In addition, it shows that non-clustering behavioural patterns of passive honey bees can make significant, subspecies distinctive changes to nest heat loss and therefore honey production and climate change survival.Entities:
Keywords: Acclimation; CFD; Climate change; Heat transfer; Thermofluids
Mesh:
Year: 2022 PMID: 35708774 PMCID: PMC9300531 DOI: 10.1007/s00484-022-02308-z
Source DB: PubMed Journal: Int J Biometeorol ISSN: 0020-7128 Impact factor: 3.738
Symbols
| Symbol | Units | Description |
|---|---|---|
| N m−3 | Pressure differential per unit length | |
| ms−1 | Velocity | |
| kgm−4 | 2nd order velocity coefficient (impact) | |
| Nm−4 s | 1st order velocity coefficient (viscous drag) | |
| Nm−2 s | Dynamic viscosity | |
| - | Porosity | |
| m | Particle diameter | |
| kgm−3 | Density | |
| m | Generic effective diameter | |
| m | Effective particle diameter after Sudarsan et al. ( | |
| m3 | Volume of particle | |
| - | Shape factor | |
| m2 | Surface area of particle | |
| m | Sauter mean value | |
| m | Effective particle diameter after Li and Ma ( | |
| m | Effective diameter of mesh opening | |
| m | Depth of mesh in simulation | |
| m−3 | Number of honey bees per unit volume | |
| m3 | Average volume of individual honey bee | |
| m | Length of honey bee |
Subspecies cell sizes, colony populations and volumes (Schneider and Blyther 1988; Saucy 2014; Mulisa et al. 2018)
| Parameter | European | ||
|---|---|---|---|
| 1 | Nest volume m3 10−3 | 17 | 45 |
| 2 | Population 103 | 6.4 | 18.8 |
| 3 | Cell diameter m 10−3 | 2.5–4.3 | 4.4–5.5 |
| 4 | Cell length m 10−3 | 9.5–11.4 | 11–12 |
| 5 | Inter-comb gap (bee space) m 10−3 | 9–11 | 9–11 |
| 6 | Total inter-comb volume m3 10−3 | 5.1 | 13.5 |
| 7 | Individual honey bee volume m3 10−9 | 54–138 | 167–261 |
| 8 | Distributed bee number density in inter-comb volume m−3 106 | 1.25 | 1.39 |
| 9 | Distributed bee volume density in inter-comb volume m3 m−3 | 0.07–0.18 | 0.23–0.36 |
| 10 | Distributed bee porosity of inter-comb volume | 0.82–0.93 | 0.64–0.77 |
| 11 | Brood area m2 | 0.24 | 0.59 |
| 12 | Bees per unit area of brood m−2 103 | 17.3–40.2 | 24.1–42.4 |
Fig. 1Cutaway of CFD model showing combs and typical temperature distribution and meshing
Fig. 2CFD brood comb frames, with covering honey bees (a) and without (b) colour code: frame as grey, comb as yellow, brood covering honey bees as blue and brood cells as red
CFD parameters
| Parameter | Value | Units | |
|---|---|---|---|
| 1 | Empty comb conductance | 0.023 | WK−1 m−1 |
| 2 | Ambient air velocity (inlet) | 0.05 | ms−1 |
| 3 | Inlet turbulent energy k | 9.79 10−8 | m2s−2 |
| 4 | Inlet turbulent dissipation rate ε | 9.94 10−11 | M2s−3 |
| 5 | Inlet-specific turbulent dissipation rate ω | 3.38 10−3 | s−1 |
| 6 | Comb frame conductance | 0.12 | WK−1 m−1 |
| 6 | Hive conductance | 0.12 | WK−1 m−1 |
| 8 | Wire mesh pitch | 4 | mm |
| 9 | Wire mesh wire diameter | 1 | mm |
| 10 | Brood covering volume | 3.4 | Litres |
| 11 | Model mesh size | 3.2 | Cells × 106 |
Fig. 3α and β air flow resistance coefficients versus a and b porosity Ψ for varying effective diameters (dEQ) and c and d actual bee diameters dBee at constant bee number densities ρB
Fig. 4Brood covering and distributed hive thermal resistance vs colony number density for effective diameters at constant ambient temperatures a 273 K brood covering, b 273 K distributed, c 293 K Brood covering and d 293 K distributed. The rightmost termination of the lines for distributed indicates the geometric packing limit with the exception of 2.5 mm diameter between
Fig. 5Brood covering and distributed hive thermal resistance vs porosity for constant effective diameters at constant ambient temperatures a 273 K brood covering, b 273 K distributed, c 293 K brood covering and d 293 K distributed