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Objectives. Finish with Exchangers - Start Air Distribution Systems - Diffuser selection. Fin Efficiency. Assume entire fin is at fin base temperature Maximum possible heat transfer Perfect fin Efficiency is ratio of actual heat transfer to perfect case Non-dimensional parameter.
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Objectives • Finish with Exchangers - Start Air Distribution Systems - Diffuser selection
Fin Efficiency • Assume entire fin is at fin base temperature • Maximum possible heat transfer • Perfect fin • Efficiency is ratio of actual heat transfer to perfect case • Non-dimensional parameter
Heat Transfer tP,o From the pipe and fins we will find t tF,m
Resistance model • Q = U0A0Δtm • Often neglect conduction through tube walls • Often add fouling coefficients
Heat exchanger performance (Book section 11.3) • NTU – absolute sizing (# of transfer units) • ε – relative sizing (effectiveness)
Summary • Calculate efficiency of extended surface • Add thermal resistances in series • If you know temperatures • Calculate R and P to get F, ε, NTU • Might be iterative • If you know ε, NTU • Calculate R,P and get F, temps
Air Distribution System Design • Describe room distribution basics • Select diffusers • Supply and return duct sizing
L = characteristic length (m, ft) g = acceleration due to gravity (m/s2, ft/min2) T = absolute temperature (K, °R) β = 1/T (1/K, 1/ °R) v = kinematic viscosity (m2/s, ft2/min) Designing Room Airflow • Very complex problem • Pumped flow, buoyant flow (or mixed flow) • What non-dimensional parameters govern each regime? • Archimedes number = Ar = gβLΔT/v2
CFD in Air Distribution Design Contaminant concentration in a kitchen
Buoyancy driven flow:Example of airflow in a stairway Heater (radiator)
Forced driven air flowDiffusers Grill (side wall) diffusers Linear diffusers Vertical Horizontal one side
Diffusers types Valve diffuser swirl diffusers ceiling diffuser wall or ceiling floor
V = maximum volumetric flow rate (m3/s, ft3/min) Qtot = total design load (W, BTU/hr) Qsen = sensible design load (W,BTU/hr) ρ = air density (kg/m3, lbm/ft3) Δt = temperature difference between supply and return air (°C, °F) Δh = enthalpy difference between supply and return air (J/kg, BTU/lbm) Diffuser Selection Procedure • Select and locate diffusers, divide airflow amongst diffusers
Indicator of Air DistributionQuality • ADPI = air distribution performance index • Fraction of locations that meet criteria: • -3 °F < EDT < 2 °F or -1.5 °C < EDT < 1 °C • Where, EDT = effective draft temperature • Function of V and Δt (Eqn 18.1) • EDT=(tlocal-taverage)-M(Vlocal-Vaverage) , M=7 °C/(m/s) ADPI considers ONLY thermal comfort (not IAQ)
Select Register • Pick throw, volumetric flow from register catalog • Check noise, pressure drop
Summary of Diffuser Design Procedure • Find Q sensible total for the space • Select type and number of diffusers • Find V for each diffuser • Find characteristic length • Select the diffuser from the manufacturer data
Example 18.3 • Qtot = 38.4 kBTU/hr • Δh = 9.5 BTU/lbma Note omission in text
Reading asignement • Chapter 18 • 18.1-18.2 (including 18.2)