U. Iljins, I. Ziemelis The Optimization of Some Parameters of a Flat Plate Solar CollectoryQT 0α glα absλ aλq iT IIIT IIδ 3δ 2x 0iλ iT Iδ 1xα rLT 0Fig. 1. The scheme of calculation:T I – temperature in the heat insulation layer, o C; T II – temperature in the absorber plate, o C;T III – temperature in the space between the glass cover and absorber plate, o C;T o – the ambient air temperature o C; δ 1 – the thickness of the heat insulation layer, m;δ 2 – the thickness of the absorber plate, m; δ 3 – the distance between the glass cover and absorber, m;λ i , λ – the heat transfer coefficients of the heat insulation material and absorber plate material,W⋅(m⋅K) -1 ; λ a – the equivalent heat transfer coefficient of the air layer between the glass cover and theabsorber plate, W⋅(m 2 ⋅K) -1 ; α gl – the contact heat transfer coefficient from the glass to air, W⋅(m 2 ⋅K) -1 ;α abs – the contact heat transfer coefficient from the absorber to air, W⋅(m 2 ⋅K) -1 ;α r – the contact heat transfer coefficient from the rear surface of the collector to the ambient air,W⋅(m 2 ⋅K) -1 ; Q – the specific power of the absorbed solar energy, W⋅m -2 ;x oi – the co-ordinate of the heat transfer medium tube, m.In compliance with the task of the investigation, the temperature distribution in the following three layers hasto be computed:T 1– air temperature in the space between the glass cover and absorber, o C;T 2– the absorber plate temperature, o C;T 3– the temperature in the heat insulation layer, o C.On the rear side of the collector where y=0, the heat convection takes place, therefore the heat flow can beexpressed by the equationλ ∂TIi= αr( TI− Ty=0 0)∂y, (3)y=0whereλ i– the heat transfer coefficient of heat insulation material, W ⋅ (m ⋅ K) -1 ;α r– the contact heat transfer coefficient from the back side surface of the collector to ambient air, W⋅ (m 2 ⋅K) -1 ;T 0– the ambient air temperature, °C.The heat convection takes place also from the front surface of the collector, where y=δ 1+δ 2+δ 3. The correspondingboundary condition for this is analogous to formula (3):− λa∂T∂yIIIy=δ1+δ2+δ3= α− T0) , (4)68 LLU Raksti 12 (308), 2004; 67-75 1-18f(TIII y=δ1+δ2+δ3whereλ a– the equivalent heat transfer coefficient of the air layer, W ⋅ (m ⋅ K) -1 ;α f– the contact heat transfer coefficient from the front side surface of the collector to ambient air, W ⋅ (m 2 ⋅ K) -1 .On the border of the heat insulation layer and the metal sheet, the temperature and heat flows are equal,which can be written as following:
U. Iljins, I. Ziemelis The Optimization of Some Parameters of a Flat Plate Solar CollectorTI= Ty= δ II1 y=δ (5)1andn∂T∂λII T− λIi = ∑qiδ(x− xoi) ,∂yy=δ∂y(6)1y=δ1i=1whereλ – the heat transfer coefficient of the metal sheet, W ⋅ (m ⋅ K) -1 ;q I– intensity of the heat absorbed by the circulating liquid, W⋅m -1 ;n – number of twines of the heat absorbing tube;x oi– co-ordinates of the twines, m;δ(x-x oi) – delta function for the point-shape absorber, m -1 .On the boundary at y=δ 1+δ 2, the heat flows are equal:∂Tλ∂yIIy=δ1+δ2+ αabs( T − T ) = QIIIIIy=δ1+δ2whereα abs– the contact heat transfer coefficient between the absorber and the air, W⋅ (m 2 ⋅K) -1 ;Q – the specific power of absorbed solar energy, W⋅ m -2 ,andαabs( TII y− TIII∂T) = −λgy= δ1+ δ 2 y=δ1+ δ 2∂III1,y=δ + δ2(7). (8)The developed problem of mathematical physics (1–8) can be solved by using the method of separating thevariables at the stated boundary conditions (2)–(8). For that the problem can be solved like the sum of aninfinitely long range in the following form:T (x, y) = T0 + A + By + ∑ Yk(y) ⋅ Xk(x), (9)kwhereA and B – constants, which will be determined later;X k(x) and Y k(y) – functions, depending only on x and y.Inserting expression (9) into equation (1) and after performing the common procedure, the problem (1–8) isdivided into two ordinary differential equations:22k′k Xk(x)= 0 and Yk(y)′′− µ k Yk(y) = 0 , (10a and 10b)X (x)′+ µwhereµ k– the constants of separation of variables (particular values).General solution of the equation (10a) is known in the form:X(x)Csin µx + Dk = k k k µ k . (11)Inserting expression (9) into the boundary condition (2) the following condition is obtained:cosx∂Xk (x)∂xx = o=∂Xk (x)∂xx = L= 0 . (12)The equality (12) is satisfied, if C k=0 andLLU Raksti 12 (307), 2004; 67-75 1-1869
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- Page 21 and 22: Ī. Vītiņa et al. Organiskā lauk
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- Page 25 and 26: Ī. Vītiņa et al. Organiskā lauk
- Page 27 and 28: I. H. Konošonoka, A. Jemeļjanovs
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