project for numerical methods
1
ChE 516 – Numerical Methods in Chemical Engineering Fall 2011 Project
Subject: Numerical Solutions to Energy Balance in Trombe Walls
Submitted to Dr. Shuguang Deng
In partial fulfillment of course ChE 516
By XXXXXXXX
December 8, 2011
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Table of Contents Abstract
Introduction
Problem
Assumptions
Governing Equations
Boundary and Initial Conditions
Method of Solution
MATLAB Program
Graphs and Observations
Conclusion
References
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Abstract Trombe walls are commonly used on south sides of homes to save solar energy
for transferring saved energy to the house. In this project a house in Las Cruces has
been considered whose south wall consists of a Trombe for heating the house using
solar energy. For calculating the temperature distribution along the thickness of the
wall, heat conduction in one dimension has been considered. Then, a numerical
technique for partial differential equations with finite difference scheme was
implemented. Finally, using MATLAB programming, the temperature distribution
along the thickness of the Trombe wall after 12, 24, 36, and 48 hours have been
calculated and the related plots are obtained using boundary and initial conditions.
In addition, the net amount of heat transferred to the house from the Trombe wall
during the first day and the second day have been determined.
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Introduction
Since ancient times, people have used thick walls of adobe or stone to trap the
sun's heat during the day and release it slowly and evenly at night to heat their
buildings. Today's low-energy buildings often improve on this ancient technique by
incorporating a thermal storage and delivery system called a Trombe wall. Named
after French inventor Felix Trombe in the late 1950s, the Trombe wall continues to
serve as an effective feature of passive solar design. Trombe walls are dark painted
thick masonry walls which are commonly used on south sides of passive solar homes
to absorb solar energy, store it during the day, and release it to the house during the
night, as shown in Figure 1. The idea was proposed by E. L. Morse of Massachusetts
in 1881 and is named after Professor Felix Trombe of France, who used it extensively
in his designs in the 1970s.
Trombe walls have been integrated into the envelope of a recently completed
Visitor Center at Zion National Park and a site entrance building (SEB) at the
National Renewable Energy Laboratory’s (NREL’s) National Wind Technology
Center. The High Performance Building Initiative (HPBi) at NREL helped to design
these commercial buildings to minimize energy consumption, using Trombe walls as
an integral part of their design. A typical unvented Trombe wall consists of a 4- to
16-in (10- to 41-cm)-thick, south facing masonry wall with a dark, heat-absorbing
material on the exterior surface and faced with a single or double layer of glass. The
glass is placed from ¾ to 2 in. (2 to 5 cm) from the masonry wall to create a small
airspace. Heat from sunlight passing through the glass is absorbed by the dark
surface, stored in the wall, and conducted slowly inward through the masonry. High
transmission glass maximizes solar gains to the masonry wall. As an architectural
detail, patterned glass can limit the exterior visibility of the dark concrete wall
without sacrificing transmissivity.
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Applying a selective surface to a Trombe wall improves its performance by
reducing the amount of infrared energy radiated back through the glass. The selective
surface consists of a sheet of metal foil glued to the outside surface of the wall. It
absorbs almost all the radiation in the visible portion of the solar spectrum and emits
very little in the infrared range. High absorbency turns the light into heat at the wall's
surface, and low emittance prevents the heat from radiating back towards the glass.
For an 8-in-thick (20-cm) Trombe wall, heat will take about 8 to 10 hours to reach
the interior of the building. This means that rooms receive slowly; even heating for
many hours after the sun sets, greatly reducing the need for conventional heating.
Rooms heated by a Trombe wall often feel more comfortable than those heated by
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forced air because of the large warm surface providing radiant comfort. Architects
can use Trombe walls in conjunction with windows, eaves, and other building design
elements to balance solar heat delivery. Strategically placed windows allow the sun's
heat and light to enter a building during the day to help heat the building with direct
solar gains. At the same time, the Trombe wall absorbs and stores heat for evening
use.
Properly sized roof overhangs shade the Trombe wall during the summer when
the sun is high in the sky. Shading the Trombe wall can prevent the wall from getting
hot during the time of the year when the heat is not needed. These Trombe wall
design concepts were applied to the low-energy design of the Visitor Center at Zion
National Park in Utah and to NREL’s Wind Site SEB in Colorado. Figure 2 shows
the Trombe wall locations in the NREL SEB (a), and the Zion Visitor Center (b).
a) NREL SEB b) Zion Visitor Center
Figure 2. Trombe wall design, (Torcellini and Pless, 2004).
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Trombe Wall Energy Performance
The energy performance of the Zion Visitor Center was monitored and analyzed
over a two-year period. The analysis consisted of measured electrical end uses,
Trombe wall temperature profiles, and thermographic pictures to determine the
performance of this Trombe wall (Torcellini, 2004). Similar measurements were
taken at the SEB over a one-year period.
Figure 3 shows the thermal distribution of the Zion Trombe wall at 8:30 p.m. on
December 16, 2000. The interior surface temperature is generally homogeneous,
ranging from 90-96ºF (32-36ºC). The wall temperature typically peaks between 8-9
p.m. The reduced wall temperature at the far right section of Trombe wall is due to
shading. The building shades a portion of the Trombe wall in the afternoon, resulting
in reduced interior temperatures (Torcellini and Pless, 2004).
Figure 3. Infrared pictures of a) Zion Trombe wall December 16, 8:30 p.m. and b)
NREL SEB Trombe Wall January 21, 8:00 p.m. (Torcellini and Pless, 2004).
Problem
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In this project the problem is defined as follows:
A house in Las Cruces, New Mexico, whose south wall consists of a 1-ft-thick
Trombe wall whose thermal conductivity is K = 0.40 Btu/h ft. °F and whose thermal
diffusivity is α= 4.78 * 10^6 (ft2/s) is considered. The variation of the ambient
temperature, T_out and the solar heat flux q′′ (Btu/h ft2) incident on a south-facing
vertical surface throughout the day for a typical day in January is given in Table 1 in
3-h intervals. The Trombe wall has single glazing with an absorptivity-transmissivity
product of k= 0.77 (that is, 77 percent of the solar energy incident is absorbed by the
exposed surface of the Trombe wall), and the average combined heat transfer
coefficient for heat loss from the Trombe wall to the ambient is determined to be
h_out = 0.7 Btu/hft2 °F. The interior of the house is maintained at Tin = 70°F at all
times, and the heat transfer coefficient at the interior surface of the Trombe wall is
h_in = 1.8 Btu/h ft2 °F. Also, the vents on the Trombe wall are kept closed, and thus
the only heat transfer between the air in the house and the Trombe wall is through
the interior surface of the wall. Assuming the temperature of the Trombe wall to vary
linearly between 70°F at the interior surface and 30°F at the exterior surface at 7 AM
and using the explicit finite difference method with a uniform nodal spacing of dx =
0.2 ft., determine and plot the temperature distribution along the thickness of the
Trombe wall after 12, 24, 36, and 48 h. Also, determine the net amount of heat
transferred to the house from the Trombe wall during the first day and the second
day. Assume the wall is 10 ft. high and 25 ft. long.
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Table 1. The hourly variation of monthly average ambient temperature and solar heat flux
incident on a vertical surface for January in Las Cruces, New Mexico
Assumptions
1- The heat transfer is considered as one dimensional in wall thickness direction.
2- The temperature in the house is constant at 70°F.
3- Based on finite difference scheme, the temperature in every 25 cm interval along
the wall is considered same for that interval.
4- The only heat transfer between the air in the house and the Trombe wall is through
the interior surface of the wall
Governing Equations
The governing equations describing the heat transfer, unsteady, conduction in one
dimension is as follows:
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Using energy balance for each of the internal intervals in Figure 4.:
Figure 4. The intervals for writing energy balance
Input-output+generation-consumption=accumulation (1)
𝐾𝐾𝐾𝐾 𝑇𝑇𝑚𝑚+1 𝑝𝑝 −𝑇𝑇𝑚𝑚
𝑝𝑝
∆𝑥𝑥 + 𝐾𝐾𝐾𝐾
𝑇𝑇𝑚𝑚−1 𝑝𝑝 −𝑇𝑇𝑚𝑚
𝑝𝑝
∆𝑥𝑥 = 𝜌𝜌𝐾𝐾∆𝑥𝑥𝑥𝑥 𝑇𝑇𝑚𝑚
𝑝𝑝+1−𝑇𝑇𝑚𝑚 𝑝𝑝
∆𝑡𝑡 (2)
Fo = α∆t/∆x^2 (3)
So by simplifying the equation (2) and using equation (3) it can be written for nods,
2, 3 4 and 5 as interior nods:
Tm p+1 = Fo�Tm−1
p + Tm+1 p � + (1 − 2Fo)Tm
p (4)
Energy balance for node 6 as the external node:
kq′′A + hA(Tin − T6 p + KA
T5 p−T6
p
∆x = ρA∆x/2c
T6 p+1−T6
p
∆t (5)
∆x
2
• • • • • 1
3 4 5
•
6
Tin
qsola’’
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Bi = h∆x K
(6)
Therefore using equation (6), equation (5) can be written in its final form for external
nod, 6:
T6 p+1 = 2Fo �Biout × Tout + T5
p + kq ′′
K ∆x� + (1 − 2Fo − 2BioutFo)T6
p (7)
And using energy balance around nod 1as the internal node equation (8) can derived
as follows:
AK � T2 p−T1
p
∆x � − hA�T1
p − Tin� = ρA ∆x 2
c T1 p+1−T1
p
∆t (8)
Then the equation (8) can be rearranged in the form of equation (9):
T1 p+1 = (1 − 2BiinFo − 2Fo)T1
p + 2Fo(T2 p + BiinTin) (9)
Boundary and Initial Condition
During writing equation related to each nod, all boundary conditions are
implemented. Table 1 shows the needed values for solar energy and out temperature
during the day. Also, the inner temperature of home is at 70oF whole the day.
Initial Condition:
At t=7 O’clock as an initial point the node temperatures are as follows:
T1=70
T2=60
T3=50
T2=40
12
T1=30
As the equation shows the explicit finite difference method is used for finding the
temperature distribution along Trombe wall. So, a MATLAB program is prepared
for solving the mentioned equations.
MATLAB CODE: clear all; clc % One Dimensional Unsteady Heat Transfer Simulation Using Explicit Finite Difference Method % Matlab using to solve numerically a heat transfer % Leila Karimi, New Mexico State University, November 2011. % L -m Length of 1D space % n -"" Number of nodes % del_x -m Spacing of nodes % t0 -Seconds Starting time % tmax -Seconds Ending time % k -W/(m K) Thermal conductivity - conduction ciefficient % alpha -m^2/s Diffusivity % h -W/m^2 K Convection coefficient % del_t -hour Change in time each iteration % T1 -hour Initial time %h_out average combined heat transfer coefficient for heat loss from %the Trombe wall to the ambient is determined to be h_out=0.7 Btu/(h*ft^2F)
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%h_in heat transfer coefficient at the interior surface of the %Trombe wall is h_in=1.8 Btu/(h*ft^2) %%%% Trombe Wall Properties %%%%%%%%%%%%% L= input(' Please input the thickness of the wall, (L=1) = '); del_x= input(' Please input the uniform nodal spacing, (del_x=0.2) = '); n=L/del_x+1; %n=6; T1= input(' Please input the internal surface of the wall, (T1(f)=70) = '); %T1=70 T(n)= input(' Please input the external surface of the wall, (T(n)(f)=30) = '); %T(n)=30; %del_x=0.2; k= input(' Please input conductivity coefficient,(K=0.4),= '); %k=0.4; t0= input(' Please input the minimum time (h), for this problem t0(h),(t0=7) = '); %t0=7; tmax = input(' Please input the maximum time (h), for two days=t0+48, (55) = '); %tmax=55; alpha_1 = input('Please input the thermal diffusivity, a(ft^2/s), (?= 4.78 x 10-6 ft2/s) = '); alpha=alpha_1*3600; %L=xmax-xmin; %del_x= L/(n-1); A=250; %%%%%%%% del_t should be less than 0.5*del_x^2/alpha %%%%%%%% del_t = 0.2*del_x^2/alpha ;
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T_out=30; T_in=70; h_in= input(' Please input the heat transfer coefficient of internal fluid, h_in (1.8) = '); %h_in=1.8; h_out=input(' Please input the heat transfer coefficient of external fluid, h_out (0.7) = '); %h_out=0.7; Fo=alpha*del_t/(del_x^2); B_in=h_in*del_x/k; B_out=h_out*del_x/k; ii=1 t_total=t0:del_t:tmax; T_out=zeros(ii,6) q=zeros(ii,6) for ii=1:length(t_total) t = t_total(ii); if t0<t & t<(t0+3) T_out(ii,6)=33 ; q(ii,6)=0.77*114; else if (t0+3)<=t & t<(t0+6) T_out(ii,6)=43 ; q(ii,6) =0.77*242; elseif (t0+6)<=t & t<(t0+9) T_out(ii,6)=45 ; q(ii,6) =0.77*178; elseif (t0+9)<=t & t<(t0+12) T_out(ii,6)=37 ; q(ii,6) =0; elseif (t0+12)<=t & t<(t0+15) T_out(ii,6)=32 ; q(ii,6) =0; elseif (t0+15)<=t & t<(t0+18) T_out(ii,6)=27 ; q(ii,6) =0; elseif (t0+18)<=t & t<(t0+21) T_out(ii,6)=26 ; q(ii,6) =0; elseif (t0+21)<=t & t<(t0+24) T_out(ii,6)=25 ; q(ii,6) =0; elseif (t0+24)<=t & t<(t0+27) T_out(ii,6)=33 ; q(ii,6)=0.77*114; else if (t0+27)<=t & t<(t0+30) T_out(ii,6)=43 ; q(ii,6) =0.77*242; elseif (t0+30)<=t & t<(t0+33)
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T_out(ii,6)=45 ; q(ii,6) =0.77*178; elseif (t0+33)<=t & t<(t0+36) T_out(ii,6)=37 ; q(ii,6) =0; elseif (t0+36)<=t & t<(t0+39) T_out(ii,6)=32 ; q(ii,6) =0; elseif (t0+39)<=t & t<(t0+42) T_out(ii,6)=27 ; q(ii,6) =0; elseif (t0+42)<=t & t<(t0+45) T_out(ii,6)=26 ; q(ii,6) =0; elseif (t0+45)<=t & t<(t0+48) T_out(ii,6)=25 ; q(ii,6) =0; end end end end T_out; q; for ii=0 for i=1:n T(1,i)=T1-((T1-T(n))/(n-1))*(i-1); end end T t=t_total; for ii=1:length(t) for i = 1:n if i == 1 T(ii+1,i) = (1-2*B_in*Fo- 2*Fo)*T(ii,1)+2*Fo*(T(ii,i+1)+B_in*T_in); elseif i == n
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T(ii+1,i) = 2*Fo*(B_out*T_out(ii,6)+T(ii,n- 1)+q(ii,6)*del_x/k)+(1-2*Fo-2*B_out*Fo)*T(ii,i); else T(ii+1,i) = Fo*(T(ii,i-1)+T(ii,i+1))+(1- 2*Fo)*T(ii,i); end end end %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% % Calculating the node temperatures after 12, 24, 36 and 48 hours T for i=1:6 Temp12(1,i)=T(length(t)/4,i); Temp24(1,i)=T(length(t)/2,i); Temp36(1,i)=T(78,i); Temp48(1,i)=T(length(t),i); end Temp12 Temp24 Temp36 Temp48 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% % Plotting the node temperatures after 12, 24, 36 and 48 hours Temp=[Temp12;Temp24;Temp36;Temp48];
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i=[1:1:6]; plot(i,Temp) xlabel('node number ') ylabel('Temperature (.F)') title('Temperature changes for nodes after 12, 24, 36 and 48 hours') legend('Temp12','Temp24','Temp36','Temp48',1) %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% %% % Calculating the net heat transfer to the home %heat1 is for the first and heat2 is for the second day heat1=zeros(1,length(t/2)); M=zeros(1,length(t/2)); for ii=1:length(t)/2 heat1(1,ii)=ii; M(1,ii)=h_in*A*(T(ii,1)-T_in); end heat1=trapz(heat1,M) heat2=0; for ii=length(t)/2:length(t) heat2(1,ii)=ii; M(1,ii)=h_in*A*(T(ii,1)-T_in); end heat2=trapz(heat2,M) %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%5 % Plotting the temperatures distribution in the form of surface for whole % the two days continously along the wall figure(1)
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hold on figure(2) colormap hot plot(T) surf(T); figure (gcf) xlabel('i (Node Number (Position through Wall)') ylabel('ii (Time)') zlabel('T (.F)') title('Temperature profile changes within 48 hr') shading interp colorbar
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Graphs and Observations
Input and Results:
Please input the thickness of the wall, (L=1) = 1
Please input the uniform nodal spacing, (del_x=0.2) = 0.2
Please input the internal surface of the wall, (T1(f)=70) = 70
Please input the external surface of the wall, (T(n)(f)=30) = 30
Please input conductivity coefficient,(K=0.4),= 0.4
Please input the minimum time (h), for this problem t0(h),(t0=7) = 7
Please input the maximum time (h), for two days=t0+48, (55) = 55
Please input the thermal diffusivity, α(ft^2/s), (α= 4.78 x 10-6 ft2/s) = 4.78e-6
Please input the heat transfer coefficient of internal fluid, h_in (1.8) = 1.8
Please input the heat transfer coefficient of external fluid, h_out (0.7) = 0.7
T =
70 62 54 46 38 30
T =
70.0000 62.0000 54.0000 46.0000 38.0000 30.0000
66.8000 62.0000 54.0000 46.0000 38.0000 29.0000
66.0320 61.3600 54.0000 46.0000 37.8000 50.7160
65.5917 60.8224 53.8720 45.9600 42.0232 60.6254
20
65.2710 60.3862 53.6797 46.7550 46.5310 66.8729
65.0195 60.0218 53.6361 48.0952 50.6442 71.5500
64.8134 59.7442 53.8050 49.7131 54.3155 75.3467
64.6529 59.5702 54.1745 51.4520 57.6013 78.5617
64.5448 59.5076 54.7091 53.2264 60.5635 102.4669
64.4938 59.5553 55.3723 54.9903 67.4768 114.6482
64.5006 59.7064 56.1325 57.5640 74.4138 123.0169
64.5627 59.9505 57.1336 60.6477 80.7644 129.6413
64.6752 60.3096 58.3998 63.9682 86.5164 135.2287
64.8459 60.8007 59.8954 67.3642 91.7493 140.0998
65.0833 61.4287 61.5702 70.7474 96.5423 134.8576
65.3915 62.1879 63.3774 74.0710 99.0464 134.3634
65.7691 63.0665 65.2782 76.9273 101.1147 135.1377
66.2112 64.0494 67.1657 79.4350 103.0819 136.3213
66.7104 65.1050 68.9963 81.7105 105.0004 137.6525
67.2525 66.2043 70.7609 83.8256 106.8728 139.0323
67.8223 67.3253 72.4625 85.8221 108.6953 140.4160
68.4075 68.4521 74.1070 87.7248 110.4648 113.2495
68.9987 69.5742 75.6996 89.5493 106.4737 101.4607
69.5893 70.6842 77.2444 90.1642 102.0862 94.4414
70.1751 71.7773 78.5163 89.9647 98.1729 89.4575
70.7529 72.8046 79.4582 89.3166 94.7882 85.5996
71.3026 73.7250 80.0992 88.4393 91.8561 82.4711
71.8026 74.5153 80.4924 87.4546 89.2958 79.1592
72.2388 75.1682 80.6894 86.4304 86.9002 76.6115
72.6046 75.6866 80.7334 85.3762 84.7485 74.4814
21
72.8997 76.0795 80.6526 84.3221 82.8206 72.6408
73.1277 76.3582 80.4719 83.2879 81.0849 71.0230
73.2939 76.5348 80.2123 82.2841 79.5131 69.5846
73.4045 76.6221 79.8912 81.3155 78.0816 68.2942
73.4659 76.6324 79.5222 80.3839 76.7709 66.4280
73.4848 76.5771 79.1166 79.4890 75.4249 65.0452
73.4672 76.4665 78.6832 78.6017 74.1618 63.8708
73.4187 76.3100 78.2235 77.7300 72.9916 62.8253
73.3445 76.1144 77.7421 76.8810 71.9060 61.8762
73.2485 75.8860 77.2444 76.0582 70.8950 61.0055
73.1340 75.6302 76.7355 75.2628 69.9498 60.0605
73.0042 75.3520 76.2199 74.4947 69.0345 59.2478
72.8618 75.0560 75.7013 73.7477 68.1692 58.5078
72.7092 74.7462 75.1815 73.0227 67.3526 57.8213
72.5487 74.4259 74.6627 72.3205 66.5804 57.1788
72.3820 74.0978 74.1469 71.6409 65.8481 56.5744
72.2108 73.7645 73.6359 70.9835 65.1519 56.0035
72.0364 73.4280 73.1311 70.3477 64.4886 55.3224
71.8599 73.0903 72.6338 69.7325 63.8271 54.7437
71.6825 72.7529 72.1449 69.1317 63.1915 54.2130
71.5050 72.4172 71.6639 68.5463 62.5839 53.7146
71.3281 72.0841 71.1910 67.9773 62.0025 53.2422
71.1524 71.7543 70.7269 67.4251 61.4454 52.7924
70.9783 71.4284 70.2720 66.8895 60.9108 71.0387
70.8062 71.1071 69.8268 66.3703 64.1321 79.2181
70.6363 70.7909 69.3916 66.6139 67.5969 84.2692
22
70.4691 70.4801 69.1159 67.3661 70.7348 87.9786
70.3046 70.2050 69.0388 68.3898 73.5098 90.9401
70.1551 69.9917 69.1422 69.5436 75.9718 93.4123
70.0339 69.8545 69.3924 70.7490 78.1743 95.5344
69.9499 69.7980 69.7561 71.9627 80.1612 118.5035
69.9072 69.8200 70.2058 73.1611 86.1900 129.8641
69.9057 69.9146 70.7197 75.1758 92.3190 137.5015
69.9432 70.0738 71.4499 77.7132 97.9269 143.4663
70.0159 70.3229 72.4274 80.5033 102.9920 148.4533
70.1330 70.6824 73.6217 83.3859 107.5865 152.7733
70.3049 71.1604 74.9867 86.2732 111.7838 147.0223
70.5373 71.7545 76.4787 89.1180 113.7294 146.0558
70.8308 72.4559 78.0617 91.5124 115.2724 146.3894
71.1818 73.2521 79.6307 93.5743 116.7438 147.1601
71.5844 74.1137 81.1437 95.4194 118.1931 148.1031
72.0258 75.0139 82.5928 97.1190 119.6204 149.1167
72.4917 75.9320 83.9823 98.7141 121.0194 121.6218
72.9708 76.8540 85.3186 100.2288 116.6788 109.5338
73.4546 77.7703 86.6077 100.5367 111.9598 102.2371
73.9372 78.6746 87.6260 100.0355 107.7306 96.9930
74.4148 79.5174 88.3177 99.0927 104.0441 92.8890
74.8665 80.2570 88.7126 97.9279 100.8228 89.5266
75.2707 80.8700 88.8646 96.6639 97.9846 86.6913
75.6130 81.3491 88.8255 95.3681 95.4618 83.5519
75.8867 81.6971 88.6387 94.0783 93.0611 81.0986
76.0917 81.9234 88.3383 92.7870 90.8720 79.0098
23
76.2314 82.0400 87.9451 91.5143 88.8826 77.1733
76.3115 82.0593 87.4779 90.2741 87.0670 75.5327
76.3385 81.9935 86.9534 89.0734 85.4016 74.0519
76.3186 81.8545 86.3854 87.9151 83.8660 72.0045
76.2583 81.6535 85.7852 86.7993 82.3035 70.4485
76.1634 81.4008 85.1617 85.6973 80.8317 69.1077
76.0395 81.1055 84.5166 84.6171 79.4600 67.9022
75.8917 80.7745 83.8545 83.5656 78.1799 66.7990
75.7238 80.4139 83.1807 82.5462 76.9808 65.7795
75.5393 80.0293 82.5005 81.5600 75.8536 64.8309
75.3411 79.6255 81.8181 80.6068 74.7904 63.8037
75.1321 79.2072 81.1373 79.6858 73.7563 62.9058
74.9146 78.7782 80.4610 78.7902 72.7721 62.0792
74.6908 78.3420 79.7903 77.9208 71.8372 61.3053
74.4626 77.9014 79.1267 77.0779 70.9475 60.5753
74.2316 77.4587 78.4719 76.2616 70.0992 59.8836
73.9991 77.0159 77.8272 75.4712 69.2885 59.0861
73.7661 76.5748 77.1937 74.7059 68.4846 58.3950
73.5338 76.1369 76.5724 73.9592 67.7109 57.7556
73.3029 75.7034 75.9626 73.2322 66.9695 57.1519
73.0740 75.2751 75.3647 72.5257 66.2585 56.5777
72.8478 74.8528 74.7790 71.8401 65.5758 56.0291
72.6246 74.4370 74.2060 71.1750 64.9193 55.5037
%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
24
% Calculating the node temperatures after 12, 24, 36 and
48 hours
Temp12 =
70.7529 72.8046 79.4582 89.3166 94.7882 85.5996
Temp24 =
71.3281 72.0841 71.1910 67.9773 62.0025 53.2422
Temp36 =
74.8665 80.2570 88.7126 97.9279 100.8228 89.5266
Temp48 =
72.8478 74.8528 74.7790 71.8401 65.5758 56.0291
%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
%%
% Calculating the net heat transfer to the home
%heat1 is for the first and heat2 is for the second day
heat1 =
-2.6487e+004
heat2 =
1.0749e+005
25
Figure 5. Node temperatures after 12, 24, 36 and 48 hours
26
Figure 6. Temperatures distribution along the wall during two days
Also, the results were exported to Excel and the temperature distribution along the
wall was plotted in Excel as follows:
27
Figure 7. Node temperatures after 12, 24, 36 and 48 hours using Excel
Conclusion
The results show that Trombe wall can be used for house heating efficiently. At
the beginning the house may lose some heat due to its lower temperature, but after
a time period the wall starts to work as a heating source and the all absorbed solar
energy during the day releases. According to observations during the first 12 hour
period the wall has absorbed lots of solar energy and its internal parts show energy
storage because of their high temperatures. In addition, the wall will release its
saved energy during the night; so, after 24 hours its temperature decreases. This
0
20
40
60
80
100
120
1 2 3 4 5 6 7
After 12 hours-7 PM-First day
After 24 hours-7 AM-Second day
After 36 hours-7 PM-Second day
After 48 hours-7 AM-Third day
28
operation repeats during the next days. Also, the calculated transferred net heat for
first and second day show that it takes some time the energy to be saved in Trombe
wall and 264870000 Btu heat goes out from the house through the Trombe wall
during 12 hours after beginning; while after 48 hours the 1074900000 BTU is
transferred to the house via Trombe wall.
References
P. Torcellini and S. Pless, “Trombe Walls in Low-Energy Buildings: Practical
Experiences” , 2004 , NREL/CP-550-36277, World Renewable Energy Congress
VIII and Expo Denver, Colorado, August 29–September 3, 2004.
2
Table of Contents
� Abstract
� Introduction
� Problem
� Assumptions
� Governing Equations
� Boundary and Initial Conditions
� Method of Solution
� MATLAB Program
� Graphs and Observations
� Conclusion
� References
3
Abstract Trombe walls are commonly used on south sides of homes to save solar energy
for transferring saved energy to the house. In this project a house in Las Cruces has
been considered whose south wall consists of a Trombe for heating the house using
solar energy. For calculating the temperature distribution along the thickness of the
wall, heat conduction in one dimension has been considered. Then, a numerical
technique for partial differential equations with finite difference scheme was
implemented. Finally, using MATLAB programming, the temperature distribution
along the thickness of the Trombe wall after 12, 24, 36, and 48 hours have been
calculated and the related plots are obtained using boundary and initial conditions.
In addition, the net amount of heat transferred to the house from the Trombe wall
during the first day and the second day have been determined.
4
Introduction
Since ancient times, people have used thick walls of adobe or stone to trap the
sun's heat during the day and release it slowly and evenly at night to heat their
buildings. Today's low-energy buildings often improve on this ancient technique by
incorporating a thermal storage and delivery system called a Trombe wall. Named
after French inventor Felix Trombe in the late 1950s, the Trombe wall continues to
serve as an effective feature of passive solar design. Trombe walls are dark painted
thick masonry walls which are commonly used on south sides of passive solar
homes to absorb solar energy, store it during the day, and release it to the house
during the night, as shown in Figure 1. The idea was proposed by E. L. Morse of
Massachusetts in 1881 and is named after Professor Felix Trombe of France, who
used it extensively in his designs in the 1970s.
Trombe walls have been integrated into the envelope of a recently completed
Visitor Center at Zion National Park and a site entrance building (SEB) at the
National Renewable Energy Laboratory’s (NREL’s) National Wind Technology
Center. The High Performance Building Initiative (HPBi) at NREL helped to
design these commercial buildings to minimize energy consumption, using Trombe
walls as an integral part of their design. A typical unvented Trombe wall consists of
a 4- to 16-in (10- to 41-cm)-thick, south facing masonry wall with a dark, heat-
absorbing material on the exterior surface and faced with a single or double layer of
glass. The glass is placed from ¾ to 2 in. (2 to 5 cm) from the masonry wall to
create a small airspace. Heat from sunlight passing through the glass is absorbed by
the dark surface, stored in the wall, and conducted slowly inward through the
masonry. High transmission glass maximizes solar gains to the masonry wall. As
an architectural detail, patterned glass can limit the exterior visibility of the dark
concrete wall without sacrificing transmissivity.
5
Applying a selective surface to a Trombe wall improves its performance by
reducing the amount of infrared energy radiated back through the glass. The
selective surface consists of a sheet of metal foil glued to the outside surface of the
wall. It absorbs almost all the radiation in the visible portion of the solar spectrum
and emits very little in the infrared range. High absorbency turns the light into heat
at the wall's surface, and low emittance prevents the heat from radiating back
towards the glass. For an 8-in-thick (20-cm) Trombe wall, heat will take about 8 to
10 hours to reach the interior of the building. This means that rooms receive
slowly; even heating for many hours after the sun sets, greatly reducing the need
for conventional heating. Rooms heated by a Trombe wall often feel more
6
comfortable than those heated by forced air because of the large warm surface
providing radiant comfort. Architects can use Trombe walls in conjunction with
windows, eaves, and other building design elements to balance solar heat delivery.
Strategically placed windows allow the sun's heat and light to enter a building
during the day to help heat the building with direct solar gains. At the same time,
the Trombe wall absorbs and stores heat for evening use.
Properly sized roof overhangs shade the Trombe wall during the summer when
the sun is high in the sky. Shading the Trombe wall can prevent the wall from
getting hot during the time of the year when the heat is not needed. These Trombe
wall design concepts were applied to the low-energy design of the Visitor Center at
Zion National Park in Utah and to NREL’s Wind Site SEB in Colorado. Figure 2
shows the Trombe wall locations in the NREL SEB (a), and the Zion Visitor Center
(b).
a) NREL SEB b) Zion Visitor Center
Figure 2. Trombe wall design, (Torcellini and Pless, 2004).
7
Trombe Wall Energy Performance
The energy performance of the Zion Visitor Center was monitored and analyzed
over a two-year period. The analysis consisted of measured electrical end uses,
Trombe wall temperature profiles, and thermographic pictures to determine the
performance of this Trombe wall (Torcellini, 2004). Similar measurements were
taken at the SEB over a one-year period.
Figure 3 shows the thermal distribution of the Zion Trombe wall at 8:30 p.m. on
December 16, 2000. The interior surface temperature is generally homogeneous,
ranging from 90-96ºF (32-36ºC). The wall temperature typically peaks between 8-9
p.m. The reduced wall temperature at the far right section of Trombe wall is due to
shading. The building shades a portion of the Trombe wall in the afternoon,
resulting in reduced interior temperatures (Torcellini and Pless, 2004).
Figure 3. Infrared pictures of a) Zion Trombe wall December 16, 8:30 p.m. and b)
NREL SEB Trombe Wall January 21, 8:00 p.m. (Torcellini and Pless, 2004).
8
Problem
In this project the problem is defined as follows:
A house in Las Cruces, New Mexico, whose south wall consists of a 1-ft-thick
Trombe wall whose thermal conductivity is K = 0.40 Btu/h ft. °F and whose
thermal diffusivity is α= 4.78 * 10^6 (ft2/s) is considered. The variation of the
ambient temperature, T_out and the solar heat flux q�� (Btu/h ft2) incident on a south-facing vertical surface throughout the day for a typical day in January is
given in Table 1 in 3-h intervals. The Trombe wall has single glazing with an
absorptivity-transmissivity product of k= 0.77 (that is, 77 percent of the solar
energy incident is absorbed by the exposed surface of the Trombe wall), and the
average combined heat transfer coefficient for heat loss from the Trombe wall to
the ambient is determined to be h_out = 0.7 Btu/hft2 °F. The interior of the house is
maintained at Tin = 70°F at all times, and the heat transfer coefficient at the interior
surface of the Trombe wall is h_in = 1.8 Btu/h ft2 °F. Also, the vents on the
Trombe wall are kept closed, and thus the only heat transfer between the air in the
house and the Trombe wall is through the interior surface of the wall. Assuming the
temperature of the Trombe wall to vary linearly between 70°F at the interior
surface and 30°F at the exterior surface at 7 AM and using the explicit finite
difference method with a uniform nodal spacing of dx = 0.2 ft., determine and plot
the temperature distribution along the thickness of the Trombe wall after 12, 24, 36,
and 48 h. Also, determine the net amount of heat transferred to the house from the
Trombe wall during the first day and the second day. Assume the wall is 10 ft. high
and 25 ft. long.
9
Table 1. The hourly variation of monthly average ambient temperature and solar heat flux
incident on a vertical surface for January in Las Cruces, New Mexico
Assumptions
1- The heat transfer is considered as one dimensional in wall thickness direction.
2- The temperature in the house is constant at 70°F.
3- Based on finite difference scheme, the temperature in every 25 cm interval along
the wall is considered same for that interval.
4- The only heat transfer between the air in the house and the Trombe wall is
through the interior surface of the wall
Governing Equations
The governing equations describing the heat transfer, unsteady, conduction in one
dimension is as follows:
Using energy balance for each of the internal intervals in Figure 4.:
10
Figure 4. The intervals for writing energy balance
Input-output+generation-consumption=accumulation (1)
�� ���� ��
∆� + �� ���� ��
∆� = ��∆�� �� �� ��
∆� (2)
Fo = α∆t/∆x^2 (3) So by simplifying the equation (2) and using equation (3) it can be written for nods,
2, 3 4 and 5 as interior nods:
T� �� = Fo!T�
� + T�� � " + #1 − 2Fo&T�
� (4)
Energy balance for node 6 as the external node:
kq��A + hA#T*+ − T, � + KA ./
0 .1 0
∆2 = ρA∆x/2c .1 0�� .1
0
∆5 (5)
Bi = 8∆29 (6)
∆x
2
• • • •• 1
3 4 5
•
6
Tin
qsola ’’
11
Therefore using equation (6), equation (5) can be written in its final form for
external nod, 6:
T, �� = 2Fo:Bi;<5 × T;<5 + T>
� + ?@ AA
9 ∆xB + #1 − 2Fo − 2Bi;<5Fo&T, � (7)
And using energy balance around nod 1as the internal node equation (8) can
derived as follows:
AK:.C 0 .�
0
∆2 B − hA!T � − T*+" = ρA
∆2 D c
.� 0�� .�
0
∆5 (8)
Then the equation (8) can be rearranged in the form of equation (9):
T �� = #1 − 2Bi*+Fo − 2Fo&T
� + 2Fo#TD � + Bi*+T*+& (9)
Boundary and Initial Condition
During writing equation related to each nod, all boundary conditions are
implemented. Table 1 shows the needed values for solar energy and out
temperature during the day. Also, the inner temperature of home is at 70oF whole
the day.
Initial Condition:
At t=7 O’clock as an initial point the node temperatures are as follows:
T1=70
T2=60
T3=50
T2=40
12
T1=30
As the equation shows the explicit finite difference method is used for finding the
temperature distribution along Trombe wall. So, a MATLAB program is prepared
for solving the mentioned equations.
MATLAB CODE: clear all ; clc % One Dimensional Unsteady Heat Transfer Simulation Using Explicit Finite Difference Method % Matlab using to solve numerically a heat transfer % Leila Karimi, New Mexico State University, Novemb er 2011. % L -m Length of 1D sp ace % n -"" Number of nodes % del_x -m Spacing of node s % t0 -Seconds Starting time % tmax -Seconds Ending time % k -W/(m K) Thermal conductivity - conduction ciefficient % alpha -m^2/s Diffusivity % h -W/m^2 K Convection coefficient % del_t -hour Change in time eac h iteration % T1 -hour Initial time %h_out average combined heat transfer coeffic ient for heat loss from %the Trombe wall to the ambient is determined to be h_out=0.7 Btu/(h*ft^2F)
13
%h_in heat transfer coefficient at the inter ior surface of the %Trombe wall is h_in=1.8 Btu/(h*ft^2) %%%% Trombe Wall Properties %%%%%%%%%%%%% L= input( ' Please input the thickness of the wall, (L=1) = ' ); del_x= input( ' Please input the uniform nodal spacing, (del_x=0.2) = ' ); n=L/del_x+1; %n=6; T1= input( ' Please input the internal surface of the wall, (T1(f)=70) = ' ); %T1=70 T(n)= input( ' Please input the external surface of the wall, (T(n)(f)=30) = ' ); %T(n)=30; %del_x=0.2; k= input( ' Please input conductivity coefficient,(K=0.4),= ' ); %k=0.4; t0= input( ' Please input the minimum time (h), for this problem t0(h),(t0=7) = ' ); %t0=7; tmax = input( ' Please input the maximum time (h), for two days=t0+48, (55) = ' ); %tmax=55; alpha_1 = input( 'Please input the thermal diffusivity, a(ft^2/s), (?= 4.78 x 10-6 ft2/s) = ' ); alpha=alpha_1*3600; %L=xmax-xmin; %del_x= L/(n-1); A=250; %%%%%%%% del_t should be less than 0.5*del_x^2/al pha %%%%%%%% del_t = 0.2*del_x^2/alpha ;
14
T_out=30; T_in=70; h_in= input( ' Please input the heat transfer coefficient of internal fluid, h_in (1.8) = ' ); %h_in=1.8; h_out=input( ' Please input the heat transfer coefficient of external fluid, h_out (0.7) = ' ); %h_out=0.7; Fo=alpha*del_t/(del_x^2); B_in=h_in*del_x/k; B_out=h_out*del_x/k; ii=1 t_total=t0:del_t:tmax; T_out=zeros(ii,6) q=zeros(ii,6) for ii=1:length(t_total) t = t_total(ii); if t0<t & t<(t0+3) T_out(ii,6)=33 ; q(ii,6)=0.77*114; else if (t0+3)<=t & t<(t0+6) T_out(ii,6)=43 ; q(ii,6) =0.77*242; elseif (t0+6)<=t & t<(t0+9) T_out(ii,6)=45 ; q(ii,6) =0.77*178; elseif (t0+9)<=t & t<(t0+12) T_out(ii,6)=37 ; q(ii,6) =0; elseif (t0+12)<=t & t<(t0+15) T_out(ii,6)=32 ; q(ii,6) =0; elseif (t0+15)<=t & t<(t0+18) T_out(ii,6)=27 ; q(ii,6) =0; elseif (t0+18)<=t & t<(t0+21) T_out(ii,6)=26 ; q(ii,6) =0; elseif (t0+21)<=t & t<(t0+24) T_out(ii,6)=25 ; q(ii,6) =0; elseif (t0+24)<=t & t<(t0+27) T_out(ii,6)=33 ; q(ii,6)=0.77*114; else if (t0+27)<=t & t<(t0+30) T_out(ii,6)=43 ; q(ii,6) =0.77*242; elseif (t0+30)<=t & t<(t0+33)
15
T_out(ii,6)=45 ; q(ii,6) =0.77*178; elseif (t0+33)<=t & t<(t0+36) T_out(ii,6)=37 ; q(ii,6) =0; elseif (t0+36)<=t & t<(t0+39) T_out(ii,6)=32 ; q(ii,6) =0; elseif (t0+39)<=t & t<(t0+42) T_out(ii,6)=27 ; q(ii,6) =0; elseif (t0+42)<=t & t<(t0+45) T_out(ii,6)=26 ; q(ii,6) =0; elseif (t0+45)<=t & t<(t0+48) T_out(ii,6)=25 ; q(ii,6) =0; end end end end T_out; q; for ii=0 for i=1:n T(1,i)=T1-((T1-T(n))/(n-1))*(i-1); end end T t=t_total; for ii=1:length(t) for i = 1:n if i == 1 T(ii+1,i) = (1-2*B_in*Fo- 2*Fo)*T(ii,1)+2*Fo*(T(ii,i+1)+B_in*T_in); elseif i == n
16
T(ii+1,i) = 2*Fo*(B_out*T_out(ii,6)+T(ii,n- 1)+q(ii,6)*del_x/k)+(1-2*Fo-2*B_out*Fo)*T(ii,i); else T(ii+1,i) = Fo*(T(ii,i-1)+T(ii,i+1))+(1- 2*Fo)*T(ii,i); end end end %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% % Calculating the node temperatures after 12, 24, 3 6 and 48 hours T for i=1:6 Temp12(1,i)=T(length(t)/4,i); Temp24(1,i)=T(length(t)/2,i); Temp36(1,i)=T(78,i); Temp48(1,i)=T(length(t),i); end Temp12 Temp24 Temp36 Temp48 %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% % Plotting the node temperatures after 12, 24, 36 a nd 48 hours Temp=[Temp12;Temp24;Temp36;Temp48];
17
i=[1:1:6]; plot(i,Temp) xlabel( 'node number ' ) ylabel( 'Temperature (.F)' ) title( 'Temperature changes for nodes after 12, 24, 36 and 48 hours' ) legend( 'Temp12' , 'Temp24' , 'Temp36' , 'Temp48' ,1) %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%% %% % Calculating the net heat transfer to the home %heat1 is for the first and heat2 is for the second day heat1=zeros(1,length(t/2)); M=zeros(1,length(t/2)); for ii=1:length(t)/2 heat1(1,ii)=ii; M(1,ii)=h_in*A*(T(ii,1)-T_in); end heat1=trapz(heat1,M) heat2=0; for ii=length(t)/2:length(t) heat2(1,ii)=ii; M(1,ii)=h_in*A*(T(ii,1)-T_in); end heat2=trapz(heat2,M) %%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%5 % Plotting the temperatures distribution in the fo rm of surface for whole % the two days continously along the wall figure(1)
18
hold on figure(2) colormap hot plot(T) surf(T); figure (gcf) xlabel( 'i (Node Number (Position through Wall)' ) ylabel( 'ii (Time)' ) zlabel( 'T (.F)' ) title( 'Temperature profile changes within 48 hr' ) shading interp colorbar
19
Graphs and Observations
Input and Results:
Please input the thickness of the wall, (L=1) = 1
Please input the uniform nodal spacing, (del_x=0.2) = 0.2
Please input the internal surface of the wall, (T1(f)=70) = 70
Please input the external surface of the wall, (T(n)(f)=30) = 30
Please input conductivity coefficient,(K=0.4),= 0.4
Please input the minimum time (h), for this problem t0(h),(t0=7) = 7
Please input the maximum time (h), for two days=t0+48, (55) = 55
Please input the thermal diffusivity, α(ft^2/s), (α= 4.78 x 10-6 ft2/s) = 4.78e-6
Please input the heat transfer coefficient of internal fluid, h_in (1.8) = 1.8
Please input the heat transfer coefficient of external fluid, h_out (0.7) = 0.7
T =
70 62 54 46 38 30
T =
70.0000 62.0000 54.0000 46.0000 38.0000 30.0000
66.8000 62.0000 54.0000 46.0000 38.0000 29.0000
66.0320 61.3600 54.0000 46.0000 37.8000 50.7160
65.5917 60.8224 53.8720 45.9600 42.0232 60.6254
20
65.2710 60.3862 53.6797 46.7550 46.5310 66.8729
65.0195 60.0218 53.6361 48.0952 50.6442 71.5500
64.8134 59.7442 53.8050 49.7131 54.3155 75.3467
64.6529 59.5702 54.1745 51.4520 57.6013 78.5617
64.5448 59.5076 54.7091 53.2264 60.5635 102.4669
64.4938 59.5553 55.3723 54.9903 67.4768 114.6482
64.5006 59.7064 56.1325 57.5640 74.4138 123.0169
64.5627 59.9505 57.1336 60.6477 80.7644 129.6413
64.6752 60.3096 58.3998 63.9682 86.5164 135.2287
64.8459 60.8007 59.8954 67.3642 91.7493 140.0998
65.0833 61.4287 61.5702 70.7474 96.5423 134.8576
65.3915 62.1879 63.3774 74.0710 99.0464 134.3634
65.7691 63.0665 65.2782 76.9273 101.1147 135.1377
66.2112 64.0494 67.1657 79.4350 103.0819 136.3213
66.7104 65.1050 68.9963 81.7105 105.0004 137.6525
67.2525 66.2043 70.7609 83.8256 106.8728 139.0323
67.8223 67.3253 72.4625 85.8221 108.6953 140.4160
68.4075 68.4521 74.1070 87.7248 110.4648 113.2495
68.9987 69.5742 75.6996 89.5493 106.4737 101.4607
69.5893 70.6842 77.2444 90.1642 102.0862 94.4414
70.1751 71.7773 78.5163 89.9647 98.1729 89.4575
70.7529 72.8046 79.4582 89.3166 94.7882 85.5996
71.3026 73.7250 80.0992 88.4393 91.8561 82.4711
71.8026 74.5153 80.4924 87.4546 89.2958 79.1592
72.2388 75.1682 80.6894 86.4304 86.9002 76.6115
72.6046 75.6866 80.7334 85.3762 84.7485 74.4814
21
72.8997 76.0795 80.6526 84.3221 82.8206 72.6408
73.1277 76.3582 80.4719 83.2879 81.0849 71.0230
73.2939 76.5348 80.2123 82.2841 79.5131 69.5846
73.4045 76.6221 79.8912 81.3155 78.0816 68.2942
73.4659 76.6324 79.5222 80.3839 76.7709 66.4280
73.4848 76.5771 79.1166 79.4890 75.4249 65.0452
73.4672 76.4665 78.6832 78.6017 74.1618 63.8708
73.4187 76.3100 78.2235 77.7300 72.9916 62.8253
73.3445 76.1144 77.7421 76.8810 71.9060 61.8762
73.2485 75.8860 77.2444 76.0582 70.8950 61.0055
73.1340 75.6302 76.7355 75.2628 69.9498 60.0605
73.0042 75.3520 76.2199 74.4947 69.0345 59.2478
72.8618 75.0560 75.7013 73.7477 68.1692 58.5078
72.7092 74.7462 75.1815 73.0227 67.3526 57.8213
72.5487 74.4259 74.6627 72.3205 66.5804 57.1788
72.3820 74.0978 74.1469 71.6409 65.8481 56.5744
72.2108 73.7645 73.6359 70.9835 65.1519 56.0035
72.0364 73.4280 73.1311 70.3477 64.4886 55.3224
71.8599 73.0903 72.6338 69.7325 63.8271 54.7437
71.6825 72.7529 72.1449 69.1317 63.1915 54.2130
71.5050 72.4172 71.6639 68.5463 62.5839 53.7146
71.3281 72.0841 71.1910 67.9773 62.0025 53.2422
71.1524 71.7543 70.7269 67.4251 61.4454 52.7924
70.9783 71.4284 70.2720 66.8895 60.9108 71.0387
70.8062 71.1071 69.8268 66.3703 64.1321 79.2181
70.6363 70.7909 69.3916 66.6139 67.5969 84.2692
22
70.4691 70.4801 69.1159 67.3661 70.7348 87.9786
70.3046 70.2050 69.0388 68.3898 73.5098 90.9401
70.1551 69.9917 69.1422 69.5436 75.9718 93.4123
70.0339 69.8545 69.3924 70.7490 78.1743 95.5344
69.9499 69.7980 69.7561 71.9627 80.1612 118.5035
69.9072 69.8200 70.2058 73.1611 86.1900 129.8641
69.9057 69.9146 70.7197 75.1758 92.3190 137.5015
69.9432 70.0738 71.4499 77.7132 97.9269 143.4663
70.0159 70.3229 72.4274 80.5033 102.9920 148.4533
70.1330 70.6824 73.6217 83.3859 107.5865 152.7733
70.3049 71.1604 74.9867 86.2732 111.7838 147.0223
70.5373 71.7545 76.4787 89.1180 113.7294 146.0558
70.8308 72.4559 78.0617 91.5124 115.2724 146.3894
71.1818 73.2521 79.6307 93.5743 116.7438 147.1601
71.5844 74.1137 81.1437 95.4194 118.1931 148.1031
72.0258 75.0139 82.5928 97.1190 119.6204 149.1167
72.4917 75.9320 83.9823 98.7141 121.0194 121.6218
72.9708 76.8540 85.3186 100.2288 116.6788 109.5338
73.4546 77.7703 86.6077 100.5367 111.9598 102.2371
73.9372 78.6746 87.6260 100.0355 107.7306 96.9930
74.4148 79.5174 88.3177 99.0927 104.0441 92.8890
74.8665 80.2570 88.7126 97.9279 100.8228 89.5266
75.2707 80.8700 88.8646 96.6639 97.9846 86.6913
75.6130 81.3491 88.8255 95.3681 95.4618 83.5519
75.8867 81.6971 88.6387 94.0783 93.0611 81.0986
76.0917 81.9234 88.3383 92.7870 90.8720 79.0098
23
76.2314 82.0400 87.9451 91.5143 88.8826 77.1733
76.3115 82.0593 87.4779 90.2741 87.0670 75.5327
76.3385 81.9935 86.9534 89.0734 85.4016 74.0519
76.3186 81.8545 86.3854 87.9151 83.8660 72.0045
76.2583 81.6535 85.7852 86.7993 82.3035 70.4485
76.1634 81.4008 85.1617 85.6973 80.8317 69.1077
76.0395 81.1055 84.5166 84.6171 79.4600 67.9022
75.8917 80.7745 83.8545 83.5656 78.1799 66.7990
75.7238 80.4139 83.1807 82.5462 76.9808 65.7795
75.5393 80.0293 82.5005 81.5600 75.8536 64.8309
75.3411 79.6255 81.8181 80.6068 74.7904 63.8037
75.1321 79.2072 81.1373 79.6858 73.7563 62.9058
74.9146 78.7782 80.4610 78.7902 72.7721 62.0792
74.6908 78.3420 79.7903 77.9208 71.8372 61.3053
74.4626 77.9014 79.1267 77.0779 70.9475 60.5753
74.2316 77.4587 78.4719 76.2616 70.0992 59.8836
73.9991 77.0159 77.8272 75.4712 69.2885 59.0861
73.7661 76.5748 77.1937 74.7059 68.4846 58.3950
73.5338 76.1369 76.5724 73.9592 67.7109 57.7556
73.3029 75.7034 75.9626 73.2322 66.9695 57.1519
73.0740 75.2751 75.3647 72.5257 66.2585 56.5777
72.8478 74.8528 74.7790 71.8401 65.5758 56.0291
72.6246 74.4370 74.2060 71.1750 64.9193 55.5037
%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
24
% Calculating the node temperatures after 12, 24, 36
and 48 hours
Temp12 =
70.7529 72.8046 79.4582 89.3166 94.7882 85.5996
Temp24 =
71.3281 72.0841 71.1910 67.9773 62.0025 53.2422
Temp36 =
74.8665 80.2570 88.7126 97.9279 100.8228 89.5266
Temp48 =
72.8478 74.8528 74.7790 71.8401 65.5758 56.0291
%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%%
%%
% Calculating the net heat transfer to the home
%heat1 is for the first and heat2 is for the second day
heat1 =
-2.6487e+004
heat2 =
1.0749e+005
25
Figure 5. Node temperatures after 12, 24, 36 and 48 hours
26
Figure 6. Temperatures distribution along the wall during two days
Also, the results were exported to Excel and the temperature distribution along the
wall was plotted in Excel as follows:
27
Figure 7. Node temperatures after 12, 24, 36 and 48 hours using Excel
Conclusion
The results show that Trombe wall can be used for house heating efficiently. At
the beginning the house may lose some heat due to its lower temperature, but
after a time period the wall starts to work as a heating source and the all absorbed
solar energy during the day releases. According to observations during the first
12 hour period the wall has absorbed lots of solar energy and its internal parts
show energy storage because of their high temperatures. In addition, the wall will
release its saved energy during the night; so, after 24 hours its temperature
0
20
40
60
80
100
120
1 2 3 4 5 6 7
After 12 hours-7 PM-First
day
After 24 hours-7 AM-Second
day
After 36 hours-7 PM-Second
day
After 48 hours-7 AM-Third
day
28
decreases. This operation repeats during the next days. Also, the calculated
transferred net heat for first and second day show that it takes some time the
energy to be saved in Trombe wall and 264870000 Btu heat goes out from the
house through the Trombe wall during 12 hours after beginning; while after 48
hours the 1074900000 BTU is transferred to the house via Trombe wall.
References
P. Torcellini and S. Pless, “Trombe Walls in Low-Energy Buildings: Practical
Experiences” , 2004 , NREL/CP-550-36277, World Renewable Energy Congress
VIII and Expo Denver, Colorado, August 29–September 3, 2004.