Use of the ground for heat dissipation

Use of the ground for heat dissipation

Enqy Pergamon Vol. 19, No. I. pp. 17-25, 1994 Copyright @ 19Y4 Elscvier Scicncc Ltd Printed in Great Britain. All rights reserved 03ho-5442/94 $6.0...

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Enqy

Pergamon

Vol. 19, No. I. pp. 17-25, 1994

Copyright @ 19Y4 Elscvier Scicncc Ltd Printed in Great Britain. All rights reserved 03ho-5442/94 $6.00 + 0.00

USE

OF THE

G.

GROUND

model

numerical

air heat exchangers through

temperature

of the natural

thermal

experimental

while

model multi-year investigation

which

process. data.

investigated

to calculate

is described.

the ground, the

DISSIPATION ASIMAKOPOULOS

of Meteorology, Applied Physics Department, University Ippokratous 33, 106 80 Athens. Greece (Received

Abstract-A

HEAT

M. SANTAMOuRIs,t and D.

MIHALAKAKOU,

Laboratory

FOR

ground.

The

operational

of multiple,

air is propelled

The technique model

potential limits

soil and ambient

has been performed

the cooling potential

the performance

or indoor

proposed

The cooling

I.5 March 1993)

The system consists of N parallel

ambient

of Athens,

been

of the system were

air-temperature

in

by the bulk

validated

real climatic

analyzed

measurements.

to analyse the impact

earth-toburied

was used for analysis of

successfully

of the system under

tubes,

and cooled

of superposition

has

parallel,

earth

against

conditions

using as inputs An extensive

was

to the

sensitivity

of the main design parameters

on

of the system.

INTRODUCTION

Earth-to-air heat exchangers consist of pipes buried in the ground, together with the circulation system which forces air through pipes and eventually mixes it with indoor air of a building or a greenhouse. exchangers under

Detailed are based

simulation models of the thermal on algorithms describing simultaneous

a temperature

symmetric

heat

gradient.]-’

flow into

the ground

performance of earth-to-air heat transfer of heat and mass in soils

However, most of the earlier models involve which does not take into account the natural

axially thermal

stratification of the soil. An accurate and validated model of heat transfer and moisture migration, taking into account thermal stratification in the soil, is given in Refs. 8 and 9. Cleasson”’ and Nissan” provide a complete mathematical analysis of the basic principle of superposition for the heat-transfer process. The

main

objective

of this paper

model

based

on coupled

is to develop

and simultaneous

transfer

an accurate, of heat

transient,

implicit

and mass into the soil and pipes.

The cooling potential of the system has been investigated under real climatic system sensitivity to different design parameters such as pipe lengths, depths below the surface, distances between The model incorporates a complete the soil under moisture depends

a thermal

gradient on the

stratification

gradient

conditions. of buried

The pipes

adjacent pipes, and the pipe radius has been evaluated. mathematical description of moisture migration through

from the higher

to the lower temperature

regions,

while the

redistributes moisture. The net result of the two interrelated phenomena magnitude of the temperature and moisture gradients. Natural thermal

in the

soil

is also

considered

while

appropriate

soil-boundary

applied at the ground surface. Heat transfer from several pipes was obtained principle of superposition and the analysis for a single pipe. MODELLING

OF

EARTH-TO-AIR

HEAT

Modelling of a single earth-to-air heat exchanger The thermal model is first developed for a single pipe.

+To whom

numerical

all correspondence

should

be addressed. 17

conditions

EXCHANGERS

The energy

balance

are

by using the basic

in the soil is

G. MIHALAKAKOU

18

the mass-transfer

et al

equation is

(2)

is the component

is the component

of moisture flux due to the temperature

of moisture

flux due to the moisture

gradient, and

gradient.

The initial conditions

are

T(r, y, t = 0) = ‘I;,(r), h(r, y, t = 0) = ho(r). The boundary conditions at r = R, are: T(R,,

y, t) = T(R,), h(R,, y, t) = h(R,), where R, is a large radial distance in the soil, which has been taken equal to 59 m. At this distance (R,), the temperature and moisture distributions are not influenced by the coupled and simultaneous transfers of heat and mass into the soil caused by the presence of the earth-to-air heat-exchanger system. This far-field boundary for temperature and moisture profiles in the soil and the same distance R, have been used by Schiller,4 Puri,” and Ahmed.‘* At r = R,, the heat-transfer in the soil is equal to the heat losses caused by air Aow through the pipe, i.e.

G,[%(Y) - @,,y,

t)l

= %(=,[dW)l,

(3)

where Gl= 2~~/{(l/~,h,)

+ [ln(R,lri,)/k,]}.

(4)

Here, T.(O) is the ambient air temperature. At r = R,, moisture transfer is only caused by the temperature gradient because the pipe is impervious. Therefore, the component of moisture flux due to the moisture gradient is equal to zero, i.e. 8h(R,, y, t)l& = 0; also, at y =yA, T(r, yA, t)= z(r), h(r, YA? t)=hs(r); at Y =YB, T(r7 yB7 t) = &tr)? h(r, YB, t) =h&). The soil temperature at a point in the pipe vicinity is estimated by superposition of the temperature field due to the pipe system T(r, y, t) and the undisturbed temperature field TU(z, t) due to the ground-surface temperature. Assuming a homogeneous soil of constant thermal diffusivity, the undisturbed temperature T’,(z, t) at any depth z and time t is T,(z, t) = T, -A,

exp[-z(n/365a)“*]

cos{2n/365[t

- to - z/2(365/na)“*]}.

(5)

This expression’3 can be regarded as an analytical solution of the one-dimensional, transient heat-conduction equation. The method of control-volume formulation is used to discretise Eqs. (1) and (2). Details of the numerical method can be found in Ref. 9. The time dependence was best handled by using implicit integration techniques. The basic algorithm used for the evaluation has been developed for TRNSYS, which is a transient system simulation program with a modular structure that facilitates addition to the programs of other mathematical models which are not included in the standard TRNSYS Modelling

library.

of N earth-to-air

heat exchangers

The formulas for N parallel pipes buried in the ground are obtained by superposition from the thermal analysis for a single pipe. Let Qi denote the heat transferred through pipe i, Qj the heat transferred through pipe j and Gj the single-pipe thermal conductance. Qi and Qj are equal to the rhs of Eq. (3) because both are equal to the heat losses from the air flowing through the pipe. The quantity Gij represents the coupling thermal conductance between two of the parallel pipes i and j, where i,j = 1, 2, . . . , N pipes and i #j. Theoretical results on thermal conductance theory have been taken from Claesson.“’ The temperatures of the air which flows

Use of the ground for heat dissipation

along pipe i and of pipe i are Taj(y) and T(R,, is obtained

by superposition

air temperature

dl

equation

system

I

p>,

between

fluctuation

single

pipe

thermal

due to the influence

coupling thermal conductance. while the coupling conductance

As an example, buried

we solved

at the same

the temperature while

K,(y)

and the heat fluxes Q;. The

the second

of the air along term

pipes on pipe i. The coefficients

the particular

are the single-pipe

for pipe i is equal

and

to G, [Eq. (4)],

+ 4z,z,]“*/Bj,}.

case of four parallel

z in the ground

pipes with the same length

and with equal

spacing

between

pipes and the first (or last) pipe,

and G, is the single-pipe

which

conductance,

the pipe i

is the air-temperature

pipes. The heat fluxes are Q, and Q2 for the internal thermal

the

(6)

variation

The single-pipe conductance between pipes i and j is

depth

region

between

,=, G,i’ ,#i

G;

G;, = 2n1nlk,lln{[(B,i)2

radius,

influence

the difference

t,=O’++

y

conductances, of other

The thermal

Therefore,

the air temperature

first term of the rhs of Eq. (6) expresses due to the

results.

for pipe i is

and the pipe temperature

This is a linear

y, t), respectively.

of the single-pipe

T.-T(R

19

is the same

respectively,

for the four pipes

they have the same length and radius. The equations for the difference pipe temperatures for the internal pipes 2 and 3 are, respectively,

between

and

adjacent

because

the air and the

T,~(Y) - ~W,,Y,

t) =

Q,/G

+ Q,/G

+ QJG

+ QJG,,

(7)

MY)

t) =

Q,/G

+ Q,/Gx + QJG,

+ QJGw

(8)

- W&Y,

For the first pipe 1, the temperature T,,(Y) - T,(R,,y,

difference

between

air and pipe is

t) =

QJG

+ QJG,

+ Q,/G,

+ Q,/h.

t) =

QJG, + QJG,

+ Q,lG

+ Q,/Ge

(9)

For the last pipe 4, K,,,(Y) - W,,Y,

(W

Equations (7)-(10) represent relations between the temperature of the air which flows along the pipe and the heat transferred from the pipe to the ground and to neighbouring pipes. For the same example, the air temperature at the internal pipe outlet was compared with the temperature

at an independent

pipe outlet.

For this purpose,

our thermal

model

was used to

simulate the performance of a single earth-to-air heat exchanger. The thermal performance of a plastic pipe, 0.125 m in radius and 30 m in length, buried in the ground at a depth of 1.5 m and with a spacing of 1.5 m while guiding air at a speed of 10 m/set, was simulated. The thermal model for N earth-to-air heat exchangers was used to simulate the performance of these four parallel pipes. Calculations covered the time period 1981-1990 for July and August using hourly values of the air and ground temperatures from 9 a.m. to 7 p.m. The calculated cumulative frequency distributions of the air temperatures at the single-pipe outlet and at the outlet of an internal pipe for July and August are given in Fig. 1.

MODEL

VALIDATION

An extensive set of experiments was performed to measure the temperatures of the air passing through underground pipes. Four plastic pipes of 0.125 m radius and 30 m length were buried in the ground at a depth of 1.5 m. The distance between adjacent pipes was equal to 4 m, while the air velocity in the pipes was equal to 9 m/set. The air temperatures at different points along the pipe were measured using iron-constantan thermocouples. The experiments

20

G.

MIHALAKAKOU et al

60

4

23.0

23.5

24.0

24.5

25.0

25.5

26.0

26.5

27.0

27.5

28.0

28.0

28.5

29.0

28.5

29.0

Temperature

August

0

24.0

24.5

25.0

25.5

26.0

26.5

27.0

27.5

29.5

30.0

Temperature

Fig. 1. Cumulative frequency distribution of the exit-air temperature from an independent earth-toair heat exchanger and from an internal earth-to-air heat exchanger.

44 t

Observed

temperatures

Fig. 2. Measured and predicted values of the air temperature at the outlet of an internal pipe.

Use of the ground for heat dissipation

were carried out during the summer and lasted from were recorded at lo-min intervals. The results were Fig. 2). It is seen that there is very good agreement for the air temperature at the internal pipe outlet. exceeded 0.5 “C.

ASSESSMENT

OF

THE

ENERGY

21

17 to 30 June. Data of the air temperature compared with theoretical predictions (see between the observed and predicted values The maximum observed differences rarely

POTENTIAL

OF

THE

SYSTEM

To prove that the use of earth-to-air heat exchangers can provide an effective means for cooling a number of basic parametric studies were performed. The thermal model was used to simulate the performance and assess the feasibility of using four plastic pipes of 0.125 m radius and 30 m length buried at a depth of 1.5 m. The air velocity in the pipes was again 10 m/set while the distance between adjacent pipes remained at 1.5 m. The calculations cover 1981-1990 for July and August using hourly values of air and ground temperatures from 0900 to 1900 LST. July 100

d ._ ‘c) 5‘

60

5 s e

40

23

25

27

29

31

33

35

37

39

41

Temperature

Temperature Fig. 3. Cumulative frequency distribution of the exit-air temperature heat exchanger for July and August.

from an internal earth-to-air

G.

22

M~HALAKAKOU et al

The air and ground temperatures were collected by the National Observatory of Athens network and includes ground-temperatures (available from 1917) at the ground surface over bare and short-grass-covered soils at 0.3, 0.6, 0.9, and 1.2m depths under the short-grasscovered soil. Based on these measurements, an accurate model to predict annual and daily variations of the ground temperature was developed. I7 Cumulative frequency distributions of air temperatures at the second pipe outlet for July and August are given in Fig. 3, which shows that the outlet-air temperature fluctuated between 24.1 and 28.2”C and 25.4 and 29.7”C for July and August, respectively, while the inlet-air temperatures varied between 23.2 and 40 and 25.3 and 39.3”C. The use of earth-to-air heat exchangers is an important method for space cooling.

SENSITIVITY

To determine the impact analysis was performed for lengths, soil depth, distance again to four pipes buried at 10 m/set.

ANALYSIS

of parameter variations on system performance, a sensitivity 1981-1990 for July and August. The system variables are pipe between adjacent pipes, and pipe radius. The simulations refer 1.5 m and with equal spacing of 1.5 m; the air velocity remained at

Influence of pipe length

The pipe length is a crucial variable in the design of the earth-tubes system. A sensitivity analysis has been carried out for three different values of pipe lengths (20, 30 and 40 m). Figure 4 shows the inlet-and outlet-temperature variations of the air of an internal earth-to-air heat exchanger for three pipe lengths. As can be seen, an increase of the buried pipe length results in a reduction of the exit-air temperature which, in turn, represents an increase of the potential cooling capacity of the system. Influence of pipe radius

Simulations have been performed for three different pipe radii (0.125, 0.180 and 0.250 m) while the other parameters remained unchanged. Figure 5 shows the air-temperature variation at the exit of an internal pipe for the three pipe radius and for the time period l-3 July. This figure indicates that an increase of the buried pipe radius results in a reduction in its convective heat-transfer coefficient which, in turn, increases the outlet-air temperature, thus reducing the system-cooling capacity.

0

Inlet

temperature

.L=20m

n

28.0 -

. r = 0.125 m * I = 0.250 m

32

26

-- 9

14 19 24 29 34 39 44 Time

Fig.

4. Variation

of the inlet-

tures from an internal

49 54 59 64

69

24.5

14 19 24

III1

29 34 39 44

I

49 54 59 64 69

Time (h)

(h) and exit-air

earth-to-air

III1

III 9

tempera-

heat exchanger

for

three days of July and for 20, 30 and 40 m long pipes.

Fig. 5. Variation internal

earth-to-air

of the exit-air

temperature

heat exchanger

days of July and for 0.125, radii.

0.180

from an

for the three first and 0.250m

pipe

Use of the ground

?h

0

B=Sm

.

B = 0 5

--

Fig. 6. Variation internal

heat

oB=.sm

?5

,I,

temperature

exchanger

from an at 2.5 m

buried

Fig. 7. Variation internal

IJ

IY

2-i

?Y

34

39

44

Time Fig. 8. Variation

of the exit-air

54

59

64

of soil

tram

buried

an

at 4 m

09

Time

temperature

from the

pipe buried at I.5 m

for spacing between

temperature

exchanger

depth for three days of July.

adjacent

pipes equal

Fig. 9. Variation

of the exit-air

(h) temperature

first (or last) and from an internal soil depth,

to 0.5 m. for three days of July.

Influence

heat

(h)

first (or last) and from an internal soil depth,

49

of the exit-air

earth-to-air

depth for three days of July.

Y

. B = 0.5 m

I--

of the exit-air

earth-to-air

for heat dissipation

from the

pipe buried at

for spacing between

adjacent

I .5 m

pipes equal

to l.S m, for three days of July.

depth

The soil depth is another purpose, simulations temperature variation

parameter

which has to be considered

in the system

design.

For this

were performed for 2.5 and 4 m depths. Figure 6 shows the airat the exit of an internal pipe for a soil depth equal to 2.5 m, for

distances between adjacent pipes equal to 0.5, 1.S, 2.5, and 5 m, and for the same time period (1-3 July). Figure 7 shows the air-temperature variation at the pipe outlet for 4 m depth. An

27 5

27.5

27 0 2h S I6

Zh.S

0

?6.0

?S S

25.5

25 0

?S.O

1-I 5 24 0

Z4.S

11) 0

I4

I,, I’)

21

i 10

31

39

Time Fig.

B = 1.5 m

r

27.0

IO. Variation

of the

1

I

44

49

1, 54

IJ 59

64

I

24.0 69

1)

14

1, 19

I 24

7Y

(h)

exit-air

I 34

39

Time temperature

from

the first (or last) and from an internal

pipe buried

2.5 m soil depth.

adjacent

for spacing between

equal to 0.5 m, for three days of July.

at

pipes

Fig.

11. Variation

of the

I

I

I

1,

44

49

S4

.io

64 69

(h)

exit-air

temperature

from

the first (or last) and from an internal

pipe buried

2.S m soil depth.

adjaccnr

for spacing between

cqual to 1.5 m, for three days of July.

at

pipes

G.

24 increase

of soil depth

capacity.

However,

leaves the system

again

provides

at depths

greater

performance

et al

MIHALAKAKOU

a considerable than

increase

4 m, the ground

in the potential temperature

system

cooling

stops decreasing

and

unaffected.

Influence of distance between adjacent pipes Four different

spacings

of adjacent

0.5, 1.5, 2.5, and 5 m. The depth the air-temperature respectively, distances

at the outlet

July. The overall

of 2.5 and 5 m, indicated

a reduction

of the air temperature

the air-temperature exit buried be seen,

fluctuation

and for l-3

variations

at a depth

equal

the air-temperature

at the internal

pipes were used for the simulations.

of the buried

pipes was equal of an internal

analysis,

at the internal

pipe

for distance

which was completed

that an increase

in spacing

The distances

to 1.5 m. Figures

between

or first pipe outlet.

were

8 and 9 show 0.5 and

1.5 m,

using the other

adjacent Figures

equal

at the first pipe outlet

to 0.5 and 1.5 m, respectively.

was slightly

in

10 and 11 show

at the exit of the first and last pipes and also at the internal to 2.5 m, for a spacing

two

pipes results

pipe As can

lower than the air temperature

pipe outlet.

REFERENCES

1. M. Santamouris and C. C. Lefas, Energy in Agric. 5, 161 (1986). E. A. Rondriguez, J. M. Cjudo, and S. Alvarez, Proc. CIB Meeting, Paris, France (1988). 3. A. L. T. Seroa da Motta and A. N. Younf, Proc. INTERSOL’8.5, pp. 759-770, E. Bilgen and K. G. T. Holland (1985). 4. G. Schiller, “Earth Tubes for Passive Cooling,” M.Sc. Report, L.B.L. (June 1982). 5. H. J. Levit, R. Gaspar, and R. D. Piacentini, Agric. Forest. Meteor. 47, 31 (1989). 6. V. M. Puri, ASAE Paper No 84-4537, 526, The Pennsylvania State University, University Park, PA (1986). 7. A. M. Amhmed, M. Y. Hamdy, W. L. Roller, and D. L. Elwell, Trans. ASAE 26, 200 (1983). 8. G. Mihalakakou, M. Santamouris, and D. Asimakopoulos, Clima ZOOO,ht. Conf., London (1993). 9. G. Mihalakakou, M. Santamouris, and D. Asimakopoulos, submitted to Sol. Energy (1993). 10. J. Cleasson and A. Dunand, “Heat Extraction from the Ground by Horizontal Pipes,” ISBN 91-540-3851-0, University of Lund, Sweden (1983). 11. C. Nilsson, “Preheating of Ambient Air by a System of Earth Tubes as a Heat Source for Buildings,” Research Project, Chalmers University of Technology, GGteborg, Sweden (1991). 12. A. Ahmed, “Simulation of Simultaneous Heat and Moisture Transfer in Soils Heated by Buried Pipes”, Ph.D. Dissert., The Ohio State University, Columbus (1980). 13. H. S. Carslaw and J. C. Jeager, Conduction of Heat in Solids, Oxford Science Publishers, Oxford, U.K. (1959). 14. G. Agas, T. Matsagos, M. Santamouris, and A. Argiriou, Energy Bldgs 17, 321 (1991). 15. A. Tombazis, A. Argiriou, and M. Santamouris, ht. J. Sol. Energy 9, 1 (1990). 16. M. S. Sodha, D. Buddhi, and R. L. Sawhney, Energy Cowers. Mgmt 31, 95 (1991). 17. G. Mihalakakou, M. Santamouris, and D. Asimakopoulos, Energy Bldgs 19, 1 (1992). 18. T. Tzaferis, D. Liparakis, M. Santamouris, and A. Argiriou, Energy Bldgs 18, 35 (1992). 19. H. N. Shapiro, “Simultaneous Heat and Mass Transfer in Porous Media With Application to Soil Warming With Power Plant Waste Heat,” Ph. D. Dissert, The Ohio State University, Columbus, OH (1975). 2.

NOMENCLATURE

A, = Amplitude of the surfacetemperature variation (“C) a = Thermal diffusivity of the ground (m’/sec)

B,, = Distance between pipes i and j (m) B = Distance between adjacent pipes (m) C, = Specific heat of air (J/kg”(Z)

Use of the ground for heat dissipation C, = Specific heat capacity (J/kg”(Z) Du,_, = Isothermal diffusivity of moisture in vapour form (m’/sec) D., = Thermal moisture diffusivity (m’/sec”C) D, = Isothermal moisture diffusivity (m’/sec) G, = Thermal conductance for a single pipe (W/m) G, = Thermal conductance G,, = h = h, = h,(r) = k =

(W/m’C) k, = Thermal conductivity I = I, = ti,, = Q, = r = R, =

for pipe i

(W/m) Coupling thermal conductance tween pipes i and j (W/M) Moisture content (kg of moisture/kg of moist soil) Heat-transfer coefficient (W/m%) Soil moisture at a large radial distance Soil thermal conductivity

be-

of the pipe

(W/m’C) Pipe length (m) Heat of vaporisation (J/kg) Mass-flow rate of ambient air through the pipe (kg/set) Heat transferred from pipe i to the soil (W) Radial polar coordinate (m) An arbitrarily large radial distance from the pipe axis (m)

r,, R, T T,(y)

= = = =

T(R,, y, t) 7;,(y) T,(R,, y, t) T,

= = = =

2s

Inner pipe radius (m) Outer pipe radius (m) Soil temperature (“C) Temperature of air which flows along a single pipe (“C) Temperature of the pipe (“C) Air temperature of pipe i (“C) Temperature of pipe i (“C) Mean annual ground temperature

(“C) T,(r) = Undisturbed soil temperature which is not influenced by the earth-tube system (“C) T,(z, t) = Ground-temperature at time t and depth i’ (“C) t = Time (set) f,, = Phase constant y = Axial polar coordinate (m) y, = An arbitrarily large axial distance from the pipe inlet (m) y, = An arbitrarily large axial distance from the pipe outlet (m) z = Depth below the ground surface (m) z, = Depth of the buried pipe i below the earth surface (m)

Greek characters p = Soil density (kg/m’) pm = Density of moisture

(kg/m.‘)