IEA Solar Heating and Cooling Programm - NachhaltigWirtschaften.at

IEA Solar Heating and Cooling Programm - NachhaltigWirtschaften.at IEA Solar Heating and Cooling Programm - NachhaltigWirtschaften.at

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IEA SHC Task 38 Solar Air Conditioning and Refrigeration Subtask C2-A, November 9, 2009 NTU number of transfer unit [-] S area [m 2 ] t time [s] T a T eq T i T m air temperature [K] equilibrium temperature [K] air temperature in the section i (i=1;9) [K] matrix temperature [K] u fluid velocity (m.s -1 ) V volume (m 3 ) w a W d humidity ratio of moist air. [Kg.Kg -1 dryair] water content of desiccant [Kg.Kg -1 desiccant] x variable [arbitrary] z coordinate in the fluid flow direction [m] Greek letters ε emissivity [dimensionless] γ i parameter used in the reduction of desiccant wheel equations [-] ∆λ parameter in the desiccant enthalpy [-] µ ratio of matrix mass over air mass [-] η cf efficiency of the counter flow heat exchanger [-] τα transmission-absorptance coefficient σ Stefan Boltzmann constant [W.K -4 m -2 ] ρ density [kg.m -3 ] λ conductivity [W.K -1 m -1 ] τ ro half period of rotation of the desiccant wheel [s] θ cylindrical coordinate or angular position [rd] Subscripts a air b buffer c condenser d desiccant eq equilibrium f fluid g glass i inlet H heat pipe page 24

IEA SHC Task 38 Solar Air Conditioning and Refrigeration Subtask C2-A, November 9, 2009 m p o reg sat matrix (sensible regenator) plate absorber outlet regeneration saturation Desiccant cooling principle A desiccant cooling installation operating under the conventional configuration (100% airchange rate), with corresponding changes in the air properties in the psychometric chart, is shown in Figure 1. 3 way valve m2 T1 Buffer 1 m1 Ti1 Heat exchanger Collectors m2 Ti2 i n m1 Tn 9 8 7 6 5 Regeneration Heat exchanger Evaporative coolers Building 1 2 3 4 Desiccant wheel Sensible heat regenerator Figure 1: Desiccant cooling system with corresponding evolution of air properties in the psychometric chart page 25

<strong>IEA</strong> SHC Task 38 <strong>Solar</strong> Air Conditioning <strong>and</strong> Refriger<strong>at</strong>ion Subtask C2-A, November 9, 2009<br />

NTU number of transfer unit [-]<br />

S area [m 2 ]<br />

t time [s]<br />

T a<br />

T eq<br />

T i<br />

T m<br />

air temper<strong>at</strong>ure [K]<br />

equilibrium temper<strong>at</strong>ure [K]<br />

air temper<strong>at</strong>ure in the section i (i=1;9) [K]<br />

m<strong>at</strong>rix temper<strong>at</strong>ure [K]<br />

u fluid velocity (m.s -1 )<br />

V volume (m 3 )<br />

w a<br />

W d<br />

humidity r<strong>at</strong>io of moist air. [Kg.Kg -1 dryair]<br />

w<strong>at</strong>er content of desiccant [Kg.Kg -1 desiccant]<br />

x variable [arbitrary]<br />

z coordin<strong>at</strong>e in the fluid flow direction [m]<br />

Greek letters<br />

ε emissivity [dimensionless]<br />

γ i parameter used in the reduction of desiccant wheel equ<strong>at</strong>ions [-]<br />

∆λ parameter in the desiccant enthalpy [-]<br />

µ r<strong>at</strong>io of m<strong>at</strong>rix mass over air mass [-]<br />

η cf efficiency of the counter flow he<strong>at</strong> exchanger [-]<br />

τα transmission-absorptance coefficient<br />

σ Stefan Boltzmann constant [W.K -4 m -2 ]<br />

ρ density [kg.m -3 ]<br />

λ conductivity [W.K -1 m -1 ]<br />

τ ro<br />

half period of rot<strong>at</strong>ion of the desiccant wheel [s]<br />

θ cylindrical coordin<strong>at</strong>e or angular position [rd]<br />

Subscripts<br />

a air<br />

b buffer<br />

c condenser<br />

d desiccant<br />

eq equilibrium<br />

f fluid<br />

g glass<br />

i inlet<br />

H he<strong>at</strong> pipe<br />

page 24

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