~j)l/

NBSIR 82-2520

'A L t

'

S^p 1 4 1982 Flow Induced By Fire in A

Compartment

U.S. DEPARTMENT OF COMMERCE

National Bureau of Standards

National Engineering Laboratory

Center for Fire Research

Washington, DC 20234

September 1982

U.S. DEPARTMENT OF COMMERCE

NATIONAL BUREAU OF STANDARDS

NBSIR 82-2520

FLOW INDUCED BY FIRE IN A

COMPARTMENT

K. D. Steckler

J. G. Quintiere

W. J. Rinkinen

U.S. DEPARTMENT OF COMMERCE

National Bureau of Standards

National Engineering Laboratory

Center for Fire Research

Washington, DC 20234

September 1 982

U.S. DEPARTMENT OF COMMERCE, Malcolm Baldrige, Secretary

NATIONAL BUREAU OF STANDARDS, Ernest Ambler, Director
0S3£'C8 HI38M

A kit 3RR Y8 a30Uai/!l W0J3

TMaMTHASMOO

ivMsotS 0 ^

9«»ilnluO 0 L

ntniiniH L .W

^4.

m

& 3

3Dfl3MMOD =K> TM3MTRA<13a 2.U

•bisOnstS lo uMiuS IftnoilftM)

yiOiS^odAj lo/<0<TDii1 KrI i«im»0

KCS.OS 00 .ooicni'^sW.

, •*

S88f ^»dfn»tq»jE}

,OQi«bl«8 untoolAM ,30H3MM0D 30 TM3MTflA33a .2.U

,'ftktmA laMnJ .80AA0I8AT® 30 UA98U8 JAMO<TAiB
TABLE OF CONTENTS

Page

List of Figures Iv

List of Tables v

Abstract vlll

Nomenclature lx

INTRODUCTION 1

DESCRIPTION OF THE EXPERIMENT 1

ANALYSIS OF EXPERIMENTAL DATA 2

THEORETICAL ASPECTS 4

DISCUSSION OF RESULTS 5

CONCLUSIONS 8

ACKNOWLEDGEMENTS 9

REFERENCES 9

APPENDIX A. Summary of Experimental Results.. 23

APPENDIX B. Listings of Intermediate Results 27

APPENDIX C. Radiation Error Associated with Opening Gas

Temperature Measurements ^0

111
LIST OF FIGURES

Page

Figure 1. Experimental arrangement 10

Figure 2. Room opening configurations with dimensions In m H

Figure 3. Gas burner locations with dimensions In ra..... 12

Figure 4. Flre-lnduced flow dynamics 13

Figure 5. Doorway velocity profiles for W 0.74 m, H * 1.83 m,

Q

= 62.9 kW, and flush burner In positions A and B 14

Figure 6. Gas temperatures for W = 0.74 m, H 1.83 m,

Q = 62.9 kW, and flush burner In position A 15

Figure 7. Opening mass flow rate as a function of ventilation

parameter for fixed fire strength and flush burner

In positions A, B, and C 1^

Figure 8. Opening mass flow rate as a function of fire strength

for fixed doorway opening and fush burner in

positions A, B, and C 1^

Figure 9. Doorway mass flow rate In kg/s for raised burner In

various locations, Q

= 62.9 kW, W « 0.74 m, and

H = 1.83 18

Figure 10. Correlation of opening mass flow rate with Idealized

flow model 1^

Figure 11. Entrained mass flow rate per unit density as a function of entrainment height for fires located

away from walls

Figure 12. Entrained mass flow rate per unit density as a function of entrainment height for fires located near

centers of walls

Figure 13. Entrained mass flow rate per unit density as a function of entrainment height for fires located near

22 corners

Figure B~l, Sensor locations with dimensions in m

33
LIST OF TABLES

Page

Table A-1. Summary of experimental results

Table B-l . Key to Intermediate results 32

Table B-2. Corrections for opening thermocouples near or above

neutral plane and attendant percent changes In mass

flux 34

Table B-3. Test 10; 2/6 door, 62.9 kW, location A 35

Table B-4. Test 11; 3/6 door, 62.9 kW, location A 36

Table B-5. Test 12; 4/6 door, 62.9 kW, location A 37

Table B-6. Test 612; 4/6 door, 62.9 kW, location A 38

Table B-7. Test 13; 5/6 door, 62.9 kW, location A 39

Table B-8. Test 14; 6/6 door, 62.9 kW, location A.....

Table B-9. Test 18; 6/6 door, 62.9 kW, location A

Table B-10. Test 710; 6/6 door, 62.9 kW, location A ^2

Table B-11. Test 810; 6/6 door, 62.9 kW, location A ^3

Table B-12. Test 16; 7/6 door, 62.9 kW, location A

Table B-13. Test 17; 8/6 door, 62.9 kW, location A ^3

Table B-14. Test 22; full window, 62.9 kW, location A

Table B-15. Test 23; 2/3 window, 62.9 kW, location A

Table B-16. Test 30; 2/3 window, 62.9 kW, location A

Table B-17, Test 41; 1/3 window, 62.9 kW, location A

Table B-18. Test 19; 6/6 door, 31,6 kW, location A 30

Table B-19. Test 20; 6/6 door, 105.3 kW, location A 31

Table B-20. Test 21; 6/6 door, 158. kW, location A. 32

Table B-21. Test 114; 2/6 door, 62,9 kW, location B 33

Table B-22, Test 144; 3/6 door, 62.9 kW, location B. 34

Table B-23. Test 212; 4/6 door, 62.9 kW, location B 35

V
Table B-24, Test 242; 5/6 door, 62.9 kW, location B 56

Table B-25. Test 410; 6/6 door, 62.9 kW, location B 57

Table B-26. Test 210; 6/6 door, 62.9 kW, location B. 58

Table B-27. Test 310; 6/6 door, 62.9 kW, location B 59

Table B-28. Test 240; 7/6 door, 62.9 kW, location B 60

Table B-29. Test 116; 8/6 door, 62.9 kW, location B 61

Table B-30. Test 122; full window, 62.9 kW, location B 62

Table B-31. Test 224; 2/3 window, 62.9 kW, location B 63

Table B-32. Test 324; 2/3 window, 62.9 kW, location B 64

Table B-33. Test 220; 6/6 door, 31.6 kW, location B 65

Table B-*34. Test 221; 6/6 door, 105.3 kW, location B 66

Table B-35. Test 514; 2/6 door, 62.9 kW, location C 67

Table B-36. Test 544; 3/6 door, 62.9 kW, location C 68

Table B-37. Test 512; 4/6 door, 62.9 kW, location C 69

Table B-38. Test 542; 5/6 door, 62.9 kW, location C 70

Table B-39. Test 610; 6/6 door, 62.9 kW, location C 71

Table B-40. Test 510; 6/6 door, 62.9 kW, location C... ••••

Table B-41. Test 540; 7/6 door, 62.9 kW, location C 73

Table B-42. Test 517; 8/6 door, 62.9 kW, location C 74

Table B-43. Test 622; full window, 62.9 kW, location C 75

Table B-44. Test 522; full window, 62.9 kW, location C 76

Table B-45. Test 524; 2/3 window, 62.9 kW, location C 77

Table B-46. Test 541; 1/3 window, 62.9 kW, location C 78

Table B-47. Test 520; 6/6 door, 31.6 kW, location C 79

Table B-48. Test 521; 6/6 door, 105.3 kW, location C 80

Table B-49. Test 513; 6/6 door, 158. kW, location C...... 81

Table B-50. Test 160; 6/6 door, 62.9 kW, location AR 82

vl
Table B-51. Test 161; 6/6 door, 62.9 kW, location BR 83

Table B-52, Test 162; 6/6 door, 62.9 kW, location CR 84

Table B-53. Test 163; 6/6 door, 62.9 kW, location DR.... 85

Table B-54. Test 164; 6/6 door, 62.9 ktf, location ER. 86

Table B-55. Test 165; 6/6 door, 62.9 kW, location FR 87

Table B-56. Test 166; 6/6 door, 62.9 kV, location GR 88

Table B-57. Test 167; 6/6 door, 62.9 kU, location HR 89

Yii
Flow Induced by Fire in a Compartment

by

K.D. Steckler

J.G. Quintiere

W.J. Rinklnen

ABSTRACT

Fifty-five full-scale steady-state experiments were conducted to study the flow

Induced by a simulated pool fire in a compartment under conditions characteristic

of the developing fire. The mass flow rate through the door or window opening

and bounds on the fire plume entrainment rate are presented as a function of

opening geometry, fire strength, and fire location.

The characteristics of the measured opening flow rates are explained by a simple hydrostatic model based on temperature distribution. A good correlation

between the measured results and the Idealized flows, taking into account the

complete temperature distribution, is demonstrated.

Entrainment results for fires near walls are in reasonable agreement with results

from free-standing plume models. Except for the smallest openings, fires in

other locations entrain at a rate two to three times the rate predicted by these

models. This phenomenon is attributed to room disturbances caused by the opening

flow and is similar to the behavior of a fire plume in a cross wind.

Key Words: air flows; compartment fires; entrainment; flow rates; fire plumes;

opening flows

viii
Nomenclature

Aq Opening area

C Opening flow coefficient

Cp Specific heat

g Gravitational acceleration

Opening height

• Rate of air flow

fflg Rate of mass entrained by fire

m Rate of gas flow from room

O

mj Rate of hot layer gas mixed into air stream

•ffipj. Rate of mass entrained by a point source plume

N Height of neutral plane

Q Rate of energy release

Temperature of gas in surrounding area

Average temperature of lower gas layer

Temperature of gas on vertical centerline of room opening

T^ Average temperature of upper gas layer

T^ Temperature of gas in room

T^ Ambient temperature

V Velocity of gas in opening

Opening width

Z Vertical coordinate

Zg Entrainment height

Z^ Thermal interface height

0 Fire plume angle

p Density of gas in opening

p Density of gas in surrounding area

Si Average density of gas in lower layer

p^ Ambient density

ix
'

'

' ‘ -i:

, '., ‘\ c if

'

‘ V' '

,

' ^0^ ,

»T4'/ifln mo'a!ll ' iroil'

.:?» -.I f b-axlsc ei^a ,,3o«< '!:**»

'

W“«^S4.-afilOq '.v'x4 b0niMlHn*

•f. -:t*Jfv*as urtdiiit

. .^1,7 & :ga*trr^Ktm0;''mk' l(Jlf

i : ::S 7i.

;

- ‘:v ''..1, 1'b‘J.r A,

.* Vv"] :

^

'

:

;aot'T tsi. is«i( ^<!f »X^ai.3;||J(l'

‘

, . ' .V; ; : r '-’^ ft "'if,' N #

• ^ . :/Ik% r»t<4( pf^

! ;, '• ./..r.m In .. -"n-fp

drybiwv:^"

djasAbnooD 'it

. '•’.

I .

: ,

'

'

'

' ''J'

'

'

' :^ '"

'

' 'f- '-

:, :' |n ‘
Introduction

The flow of air and gases in room fires has a significant bearing on the

development and state of the fire. In developing fires it controls the temperature

and heat transfer and thereby influences the spread of the fire. In the fully

involved fire stage, after flashover, the rate of air flow is known to control the

rate of fuel mass loss, i.e. , the ventilation controlled fire. Simple theories have

been developed (Kawagoe , Thomas et al ) for buoyancy driven flows in fully develO oped compartment fires, and by Rockett^ and others for the developing (smaller) fire

period. The latter model serves as a basis for more elaborate systems (zone) models

which predict the entire developing fire process (e.g., Emmons^).

Until now there has been no systematic experimental study of fire induced

flows. This has been due in part to the difficulty of making accurate and sufficient velocity measurements to arrive at a mass flow rate for a door or window. The

present study has addressed this problem using a steady-state full-scale fire

experiment with sufficiently accurate velocity instrumentation and automated data

collection. The focus of the study is the "small" fire characteristic of the

developing fire stage. The results will show the effect of fire strength and

location on flow rate through door and window openings. Also, an estimate of insltu cl L r entrainment rate by the fire plume will be presented. The objective is to

determine the characteristics of these flows and to evaluate existing room fire flow

theories dealing with opening and entrainment flows.

Description of the Experiment

The steady-state flow experiments were conducted in the room shown in Fig. 1.

The lightweight walls and ceiling were covered with a ceramic fiber insulation board

to establish near-steady conditions within 30 minutes following Ignition of the

30 cm diameter porous plate diffusion burner. The burner was supplied with commercial grade methane at a fixed rate.

* Superscripts in the text refer to references at the end of this report.

- 1 -
Movable bidirectional velocity probes and bare-wire thermocouples within the

room opening measured the velocities and temperatures of the opening flows on a twodimensional grid of 28 to 144 points depending on the size of the opening, A fixed

array of aspirated thermocouples in the front corner of the room measured the gas

temperature profile. A similar array of bare-wire thermocouples (not shown)

measured the near-ambient temperature profile within the larger well-vented area

outside the room. The locations of these stationary thermocouples were chosen to

permit the computation of the static pressure differences which drive the opening

flow. The facility and instrumentation are more fully described in a report by

Steckler^.

Forty-five experiments were conducted representing different fire strengths

(31,6, 62.9, 105,3, and 158 kW), the door and window openings shown in Fig. 2, and

the fire locations shown in Fig, 3, Ten additional experiments were conducted on

selected configurations to examine the repeatability of the experiments and to

determine the effect of ambient temperature on the results.

A nalysis of Experimental Data

The steady flow induced by a fire in a compartment was viewed in terms of the

model illustrated in Fig, 4. Air flows into the room at a rate m , shears or

di

I entrains some gas from the hot upper layer at a rate m,, and mixes with it in the ' 3 I lower layer. The fire plume entrains gas from the lower layer and "pumps" it to the

upper layer at a rate m^. Similar mass transport into the upper layer due to

natural convection by the heated lower walls may be possible but will be considered

negligible under these thermally stratified conditions. Under steady conditions the

mass flow rate through the opening from the upper layer (m ) equals the fuel flow

8

rate plus m . a Opening mass flow rates were determined by Integrating the local mass velocities (pv) over the area of the opening either above or below the zero-velocity or

j neutral plane level (N), The local velocity (v) was obtained from the bidirectional
probe data and the local density (p) was established from the opening temperature

data and Ideal gas law. Representative velocity profile data are Illustrated in

Fig, 5. Typical opening temperature data are included in Fig. 6. For clarity, only

the centerline temperatures within the opening (T^) are shown. Nevertheless, this

profile is representative of most off-centerline profiles as well.

To evaluate the in-situ entrainment of the fire plume, the rate of mass

entrained and the vertical entrainment height (Zg) must be determined. In the

context of the room-fire flow model shown in Fig, 4 the entrainment takes place over

the vertical distance between the top of the burner and the thermal Interface at

Z^. This interface was estimated from the room temperature profile data (T^,) as the

position of rapid temperature change between the lower and upper portions of the

room, A typical room temperature profile is Included in Fig, 6, This profile

illustrates that diffusion and mixing often preclude a sharp designation for Z^,

Consequently, the entrainment height could only be determined within _+ 8 to _+ 50

percent accuracy. The fire plume angle (0) shown in Fig. 4 was not measured but

qualitative changes in 0 with fire location were noted.

The rate of entrainment by the fire plume over Zg cannot be directly determined, Therefore, we adopted the approach presented by Qulntiere et al^. Referring

to Fig. 4, if one defines a lower-layer control volume as the region between the

floor and Z^^, excluding the fire plume, then under steady conditions the fire plume

entrainment rate is given by

ra=fii+A. (1)

e a j

Any overall heated-lower-wall entrainment effects are ignored in this equation.

Although the opening flow rate (m ) was known, the available data permitted only an

Si upper-bound estimate for . This was found through an energy balance on the lower

layer which neglects heat transfer between the lower room surfaces and gas. Since

these surfaces will be hotter than the gas, the energy balance yields the upper

limit

(ra . ) = m

j max a - ( 2 )
m <m <m +(m.)

a — e — a j max

where T Is the mean upper layer temperature, T. Is the mean lower layer temperature, and is the ambient temperature. Consequently,

(3)

In computing were selected from the room temperature profile data

and was taken as the average of the gas temperature measured outside the room

(T3).

Complete listings of experimental data and results are presented in Appendices

A and B,

Theoretical Aspects

The primary elements governing the flow induced by fire in a room are the

phenomena of flow across an opening and the entrainment of air by the fire. An

examination of the relationships describing these elements will show their dependence on the relevant variables. Also, these theoretical results will provide a

basis for understanding and discussing the experimental results.

Flow Through a Vertical Opening

The temperature difference between the room (T_) and its surroundings (T_)

creates a pressure difference which causes the flow at the opening. The application

of Bernoulli's equation and hydrostatic principles along with the assumption of

horizontal streamlines starting from rest leads to a formulation for the rate of

mass flow from the room^.

H Z

% = /° [(2g/T^) / (1/T^ - l/T^)dZ'] dZ (4). 51 T" N N

A corresponding equation holds for the flow rate into the room. Since the case of

steady-state small fires is being considered, the inflow rate equals the outflow

rate and only Eq. (4) is necessary for this discussion. By approximating the

temperature to be independent of position, Eq. (4) reduces to

m = 2/3(2g)^''^Cp^A Hy^[(T /T )(1-T /T

g aoo ar ar o

(5)

-4-
This form shows the functional dependence on the ventilation (geometric) para1/2 meter )» and N. A practical upper limit results for "large" fires or

small openings when is uniform over the entire opening and in the range of

500 - 1500 K^»2.

m = 2/3(2g)^^^Cp A H^^^f(T /T ) « 0.52 A (6) max a 00 ar oo

3

where f(T^/T^) «= 0,21 for 0.2 ^ T^/T^ 0,6, 1,2 kg/m , and the flow coefficient (C) is 0,7.

Fire Plume Entrainment

A complete theory for the entrainment of air into free symmetric fire plumes

does not exist. An ideal model results from the theory of a weakly buoyant point

O source of heat as given by Zukoski et al ,

m = 0.210 p (g/c p T (7) pt p'^00 OO'' ^

This shows the dependence on the ambient density (p„)» the heat source (Q), and

height (Z), Data and empirical models on the entrainment into free plumes by

Zukoski et al * and McCaffrey » show deviations from the point source ideal of

up to ^ 50 percent. Disturbances in the ambient air contribute to this deviation

and a wind effect (i.e. , 0 < 90° in Fig. 4) will Increase the rate of entrain6 8 meat * . All of these effects will be present in room fires due to the presence of

walls and flows through openings. In any case, the ideal point source formula can

serve as a useful reference to the in-situ fire entrainment rates measured.

Discussion of Results

During an experiment the ambient temperature in the test facility was very

close to the outdoor temperature. Although T^ varied little during a given 2-hour

experiment, it varied between 5°C and 35°C over the full course of experiments.

Experiments were repeated on selected configurations on different days to determine

the effect of T^ on results. Opening flow rates changed 3 percent or less

-5-
for changes less than 2°C, 5 percent or less for 10°C changes, and 11.5 percent

or less for 19°C changes. Negligible changes in produced negligible changes in

the measured opening flow rates. When considering subsequent figures showing

opening flow rate versus either or Q, bear in mind that was not controlled

and, consequently, tolerances of 12 percent or less should be assumed when comparing

results

.

Opening mass flow rates for the three floor-level burner locations and

Q

= 62.9 kW are shown in Fig. 7 as a function of Differences between inflow

and outflow rates represent experimental error since the fuel rate was negligible

compared to the opening flow rate. As expected, the smallest opening flows are in

good agreement with the ventilation limit described by Eq. (6). The results for the

larger openings follow curves characteristic of the explicit temperature and N/Hq

dependence of Eq. (5). Average upper gas temperatures (T^) ranged between 270 and

288°C for the smallest windows and between 109 and 172°C for the widest doorways.

The ratio N/H^ increased with (or decreasing T^) from 0.45 to 0.59. The

opening flow rates are highest for the room-center fire location, lower for the

back-wall center position, and lowest for the corner position. This order reflects

the decreasing effect of the door jet and the role of nearby walls in restricting

flow to the fire plume.

Figure 8 shows flow rate through a fixed door opening increasing with fire

strength (Q). As Q increased from 31.6 to 158 kW, the upper layer temperature

increased from 85°C to 289°C, N/H^ decreased from 0.58 to 0.54, Zg decreased 6 cm or

4 to 6 percent, and the opening flow increased by 54 to 68 percent. These results

are reasonably consistent with Eqs. (5) and (6).

Opening flows for other fire locations are shown in Fig. 9. These experiments

were conducted with a fixed door opening, fixed fire strength, nearly constant T^,

and the face of the burner 30 cm above the floor. Opening flows are greatest with

the fire just inside the doorway and decrease as the fire is moved back along the

room centerline. This behavior is attributed to the door jet "wind effect" reported

-6-
by Quixitiere et al^; namely, that fire plume entrainment is increased as the plume

is blown over by the door jet.

Figure 10 presents the opening flow rates versus the static-pressure flow model

given by Eq, (4) divided by the flow coefficient (C). The slope of the line

represents the average outflow coefficient, C = 0.73, for all 55 experiments. This

compares to 0.68 suggested by the water-kerosene analog experiments of Prahl and

1

Emmons . The correlation shown in Fig. 10 indicates that opening flow rates can be

predicted within ~ 7 percent given N, T^, T^, T^^, and C = 0.73. Although N is based

on the opening velocity profiles. Fig. 6 suggests that it can be estimated from

Tq. Consequently, it appears that opening flow rates could be determined from

temperature measurements alone.

Equation (7) shows that fire plume entrainment rate is a function of the

density of the surrounding gas For an enclosure fire, this is the density of

the lower gas layer (p„). In our experiments, changes in configuration and T

resulted in T^ ranging from 17°C to 157°C and consequently, ranging from 1.22 to

O 0.82 kg/m . To account for this variation, entrainment rates are presented in

Figs. 11, 12, and 13 on a per unit density basis (m /p^). Likewise, the point

source and empirical models are included as m /p . 0 00 The entrainment results shown in Fig. 11 for fires located away from walls are

affected by the wind associated with the air flow through the opening. Consistent

C Q with the results of others *

, the wind enhances the entrainment rate by as much as

three times the free-standing plume model predictions. However, the room fire

results are in agreement with the free-burn models when the wind effect is small and

the fire plume in the room remains nearly vertical (e.g., the smallest window data

point). In fact, Quintiere et al^ found that the point source plume model gave good

agreement with inclined wind-blown plume results if an effective entrainment length

of Zg/sin 0 were used in Eq. (7).

The entrainment rates for fire plumes adjacent to walls or in a corner might be

expected to be diminished from their free-burn values due to interference from the

- 7-
walls. For Idealized point source plumes, the method of reflections would suggest

(l/n)th the entrainment rate of an nQ source in which n=2 for a wall and 4 for a 90°

corner. This is not the case of a circular burner tangent to vertical surfaces. In

Q

fact, Zukoski et al found that the entrainment rate of a circular burner next to a

vertical wall is nearly identical to the same fire without the wall. Within the

scatter of the data, the results shown in Fig. 12 for room fires near walls are

consistent with free-plume predictions. It appears that the wall orients the plume

vertical but does not inhibit its perimeter for entrainment significantly. The case

of the corner fire is a more severe geometry and some interference by the walls is

obvious in Fig. 13.

Free-burn plume or wind-blown plume models seem sufficient for predicting the

results within the uncertainty limits assigned to the derived entrainment rates.

Any other effects, such as those due to less buoyant wall plumes in the lower region

of the compartment, must lie within the uncertainty of these data at most.

Conclusions

A systematic experimental study of flows Induced by a simulated pool fire in a

compartment under conditions typical of the developing fire has been completed. The

characteristics of the measured opening flow rates can be explained by a simple

hydrostatic model based on temperature distribution. Indeed, a good correlation

between the measured results and the idealized flows, taking into account the

complete temperature distribution, has been demonstrated.

Fire plume entrainment results for fires located near a wall or corner are in

reasonable agreement with results from free-standing plume models. Except for small

openings, entrainment rates for fires in other locations are two to three times the

rates predicted by these models. The higher rates are attributed to the "wind

effect" brought about by the opening flow. Earlier work^ Indicates that the point

source model can predict the wind-blown plume results if an effective entrainment

length of Zg/sln 9 is used.

-8-

1
Acknowledgements

We are grateful to Armstrong World IndustriGs for their partial support of this

I project through the National Bureau of Standards Research Associate Program. We are

|j indebted to cooperative-education interns Cho Sze, Wendy Wussow, and Adalberto

I Madlonado for their assistance with the experiments and data reduction.

References

1. Kawagoe, K. , Fire Behavior in Rooms, Report No. 27, The Building Research

Institute, Ibaraka, Japan, September 1958.

2. Thomas, P.H. , Heselden, A.J.M. and Law, M., Fully-Developed Compartment

Fires—Two Kinds of Behavior, Technical Paper No. 18, Fire Research Station,

Borehamwood, England, October 1967.

3. Rockett, J.A., Fire Induced Gas Flow in an Enclosure, Combustion Science and

Technology 12, 165 (1976).

4. Emmons, H.W., The Prediction of Fires in Buildings, Seventeenth Symposium

(International) on Combustion, p. 1101, Pittsburgh, PA, The Combustion

Institute, 1978.

5. Steckler, K.D. , Fire Induced Flows Through Room Openings - Flow Coefficients,

Technical Research Report, Armstrong World Industries, Lancaster, PA, May 1981.

6. Quintiere, J.G. , Rinkinen, W.J. and Jones, W.W. , The Effect of Room Openings on

Fire Plume Entrainment, Combustion Science and Technology 26, 193 (1981).

7. Quintiere, J.G. , DenBraven, K. , Some Theoretical Aspects of Fire Induced Flows

Through Doorways in a Room-Corridor Scale Model, NBSIR 78-1512, National Bureau

of Standards (U.S.), October 1978.

8. Zukoski, E.E. , Kubota, T. and Centegen, B., Entrainment in Fire Plumes, Fire

Safety Journal 3, 107 (1981).

9. Zukoski, E.E., Kubota, T. and Centegen, B., Entrainment in the Near Field of a Fire Plume, NBS-6CR-81-346, National Bureau of Standards (U.S.), August 1981,

10. McCaffrey, B.J. , Purely Buoyant Diffusion Flames; Some Experimental Results,

NBSIR 79-1910, National Bureau of Standards (U.S.), October 1979.

11. McCaffrey, B.J. , Momentum Implications for Buoyant Diffusion Flames, in

preparation, 1982.

12. Prahl, J. and Emmons, H.W. , Fire Induced Flows Through an Opening, Combustion

and Flame 25, 369 (1975).

- 9-
MOVABLE

BIDIRECnONAL

VELOCITY

PROBES

AND

THERMOCOUPLES

[

!

10

Fig.

1.

Experimental

arrangement.
0.24 0.36 0.49 0.62

WINDOW OPENINGS

Fig 2. Room opening configurations with dimensions

in m.

11
2.80

2.80

1.40

aio

/ / / / 7’7 'Z

NEAR FLUSH RAISED

Fig. 3. Gas burner locations with dimensions in m.

12
13

Fig.

4.

Fire-induced

flow

dynamics.
DOORWAY VELOCITIES

CENTER BURNER CORNER BURNER

Fig. 5. Doorway velocity profiles for W = 0.74 m,

H = 1.83 m, Q = 62.9 kW, and flush burner in

pSsitions A and B.

14
ROOM

DOOR

OPENING

CONNECTED

SPACE

15

Fig.

6.

Gas

temperatures

for W=

0.74

m, H

=1.83

Q=

62.9

kW,

and

flush

burner

in

position A
I I I \ I 0 0.5 1.0 1.5 2.0 2.5

Fig. 7. Opening mass flow rate as a function of ventilation

parameter for fixed fire strength and flush burner

in positions A, B, and C.

16
0.8

0.7

0.6

0.5

c/>

CO

C9

0.1

1 “1 1

1 1

DOOR

Wo = 0.74m “

Ho = 1.83m •

“ i

8

°

— • Q

o

4

•o

B

— h

—

—

Solid symbols - outflow

Open symbols > inflow

o Room center

Burner Center back wall

. A Back corner i__ I 1 \ \ 60 120

Q(kW)

180

Fig. 8. Opening mass flow rate as a function of fire strength

for fixed doorway opening and flush burner in positions

A, B, and C.

17
9. Doorway mass flow rate in kg/s for raised burner in

various locations, Q

= 62.9 kW, W = 0.74 m, H = 1.83 m,

and = 6.5 ± 0.5“C. ° °

18
T

T

T

T 8

»—8a o

-Q

rner 9

kW

CD • 3 • '3

,n CM 0)

(U >>0 rH

T) T3 I—

O (U II •H B CO •H O'

cw1 & CO IW • o Pj 'O 1—

rH c 3

y-i • ^ cO u 00

T3 CD T3

m

0) 1 3 rH N CO CO •HrH a

or

n) o 12

a> »• o

TJ PQ CO

•rt CJ^ • 1 u • m C CM O U < (U t-H •H CD IS .V CU II <: u vO

CU

a O' • +J C CU rH

CO o u T3 cn

•H 3

*J CD 3 II & •H 1—

o CD O CD cy 1—

O 4G

4-1 a, 6 O Tj tU c m 1 CD 3 m •H

CO

O

C

B CU cd u ;2 GO J-i o 3 C C CU 01 o

•H c CO 0 c u • CU

CU 3 CL5 a. 3- T3 o U CU CU ^ O X

M-l CD 'H o 3 •' CD cw

rH pL< I—

c C4-I O 3 o 9^ •H w B 4J u • • 3

CO CO •' CO 3 I—

-H

O

m

CU

O X) 3 u ^ 1 •H 6 rH 13 o

CJ CD)

Q

O

CD 3

J-i o1—

GO

•H

(s/3)|) 3iV)l MOU SSVN 9NIN3dO

19
ega • • 0

CO 0

f-4 "3 o 1 M-lO a

CO co l-l •H • (U 4J CO c O i“H l-l C r-( 3 D eg U3

<4-1 s

T3

eg

B (U o CO CO C4 •H

eg cu egV4

4J eg • «c •H Se CO CO eg > c 0

cu T3 •3 •a 0) c

4J 1-1 4J eg •w a c o 1 3 >H •

CO cu cu * a CO •rl >>

CU M-l 3

4J

eg

u

a 0 0

>4^ 0 & •3 o 4J I—1 1 U-l bO •H o

CO (U

CO

eg

M e 4J V c c

T3

cu

B 3 C ti ,3 •H •H

eg eg .c

l>i V4 CO

4-1 4J 3 c C rH w 0) 4-1

GO

•H

pH

20
m

4-t x: 3

bO S

•H !-i 01 O X O

T3

+Jc 1 0)ec

•H

cO

>-i >-l 4-1 (U C 3

0) 33

M-lo

4= c CO o 3

•H rH

4J <4-1 Oc • • 3 CO

<+4 o

cd -e m

to cn

4J • 3

•H

W S m tH M C iH O

<u 3 O & 33

+j <4-4 1 •H O _ c3 S1 y U (U •> (U 4-1 U a 3 3 3 3

(UO >-4 4-> 3

tO 3 X }-i 33 t3 & 3 3 o M 1—1 14-1 3 3 U 3 w 3 w O

<0

O

M S i-H I5O

'O

W t3

0) 3 3 3 U -H

•H •H 15

CO <4-1

}-4 1 4J (-1 3W oM <4-1

00

•H

21
Fig.

13.

Entrained

mass

flow

rate

per

unit

density

as

a

function

of

entrainment

height

for

fires

located

near

corners.

Symbols:

flush

burner,

A

-

doorways,

A

-

windows;

raised

burner,

A

-

doorway.
Appendix A. Summary of Experimental Results

23
Table

A-1.

Summary

of

Experimental

Results

0^

fd ^ X

9 w» 5.S

<d ^ c u 8 0

<U H O •HO. w

^ 6

O CC

CL cn e (d

0) o

H

. <D 60 ^ > O < hJ

oi CJ H o

0>

«4-t o cd kJ a 05 e «

0) c I

• <u 6C CL > o. < P

05 4=H

a Cd

05 1-1

< flH

c ^O fO

05 (d 60 M U -H

•H O

Pt. hJ

O-^

00o^o

d

vO

<s

cs

sr NO -4* NO

Ov NO

f-t 00

ON fO 00 o o o

no 00 cN fO m ON

CN CN CO

CM cn no oCO

nO vO ON

oiTi 00

^4“ \o

CO

CO 00 ON

C MT iH On NO in On ON O ON NO

CO CM CM CO O iH O On COCM o

O so CO CO

00 00

CM iH CM

00 nO »0 iH CM CM

Ml 00 CO CO CO r>. CO hs r*«. r*- CO rH CM U

C5 u

CM CM CM CM rM CM tH fH CM CO CO CO iH fH iH pH iH pH iH

4J d o c o o o O O o o o o o o O O O d d O C

CM b£ *H \ +1 +1 +1 +1 +1 +1 +1 +1 +1 +1 +1 +I +1 +1 +1 +1 +1 +1 +1 +1 +1

' *H CM g CM

iH <15 w r*» •*3* NO NO fH fH CO CO CO ON o rv fH

Cd PS m 00 00 ON ON On o o o o rs 00 ON ON ON fH fH CO t d o o o C o O rH iH rH rH o o o o o o d rH pH pH

Cd ON fH SO CM CM pH so CO CM pH m *a* CO ON ' in CO so GO U 0 ON fH CO CO m so SO m in 00 o 00 00 in so CO CM m so 0 PS in LO m m in in in in m in in <r Mf in m in m in in

pj d o O o o o o o o o o o o o o o o d d o o

U /-s pH 00 m CO CO o in so CM so 00 CO so

Cd (0 m in m so CM NO NO CM o pH PN. NO o o pH CM 00 o CO m

pc CM CO 'O m in m SO so SO so CO CO pH SO NO CM CM CO ^ *e 6C • pc d o o o o o o O o o o o o o o O o d d o o <<<<<<<<<<<<<<<<<<

ON

CMNO

On on On On On On On

CMSO

ON ON

CM CM NO NO

CO O

in 00

On On ON

u o >

cd •d o o o

u U U U u u u U U u u u 6 -o »o u U u u U

60 3 CM o o o o o o O o o o o •H c c c o o 0 o 0

c 60 o o o o o o O o o 0 o rs •H •H •H o o 0 0 0

•H •H • a o Q Q o Q O Q Q Q Q IS IS Q Q o Q Q

c U-t 60 pH

0) c •H so so NO nO so so sO so NO so so pH CO CO CO NO vO so so sO a 0 *v„. *»««», 3 *«»%. •*»««. o o CM CO •4* in so so NO so 00 pH CM CM pH sO sO NO CM CO

4/6

Door
Table

A-1.

(continued)

01ua

4J

4J /-s C U 8 0

0) (U

H 0 •H a ^ B 1^M

0)

y-i >b O 03 hJ a cA a nJ S o

E-t

u • 0) 00 ^ > o < hJ

0)

O CO

oi

O

H o a (A §H. (U bO & > 0- <

CO 3 O fa so so os CM SO LTl 00 Os CO CO o CM so o sf C Eh 0 os 00 00 r*. r>. Os fa fa fa CO o r^ so m to CO

fa fa fa fa fa fa fa CM CM fa CM CM fa fa fa fa fa fa fa

(U 4=

aO

•HU

COUO

tJ '

0)a

CO

U

•H rH < fa

C ^O CO

CO bO

bCC

0) :s

i-4 O' ^ 4J w W

cuu co

•H

4J

COU ^ bO D CM C bC

•H ‘H • to ^ bO

q; c ‘H

fa

O fa

OO

CM 00 fa uo OS CO vO VO CO so so 00 so 00

mm so LO so

m so so <r sO so so p^ p^ p^ p^ p^ o o o o o o o o o o o o O o o o o o o o o o o o o o o o o d d o o o o o o o

C^

H CM CM o o

CO CM

o^ a^ 00

CM CM CM oCM

fa 00 fH SO

iTj CO UO CO

•*0’ Mf

O lO CM

UO vO vD

CO vO fa m CO Mj- Os as

CM CM

Mh CO p^ p> CO r>. p^ rN p> p^ CO fH. CO CO P^ P>. P^ fa

(D 4J

CM fa fa fa CM fa fa fa fa fa CM fa CM fa CM fa fa fa fa

u

d o o c OO o o o o dd

C c o o o OO

C

fa bO fa x-s •H N B

+i +1 +1 +1 +1 +1 +1 +1 +1 +1 +1 +1 +1 +1 +1 +1 +i +1 +l fa OJ o fa p^ CO os p> r««. p^ fa CO OS o so so SO fa

CO IX CO CO CO CO CO CO CO CO CO o o fa CM CM CM CM CO t fa fa fa fa fa fa fa fa fa fa fa fa fa fa fa fa fa fa fa

so so 00 fa so CM os fa o so 00 o SO os CM fa CO 0 SO so so so 00 UO CTs fa 00 CM so SO p^ p>. p^ as os « m uO lO m lO m m <r m m m m UO m m m lO m lO d o o o o o o o o o d d O o o o o o o

(A 4J

O CM OS OS CM iT» to P^

m CM CO o 00 fa 00

m OS

(A CO CA 00 < CO

O

mmO nO* 00 00 p««. CO

CO Pi « '

CO vT -3“ <p lO CO CM CM CO in CM CO CO Mf Mfmm

.0 bO S X

dO o o o O o O

O o d

d o o o o o o o

PQ PQ pq fa PQ p:) o u o a o

OS

CM

OS 0> 0> OS o^

so sO sO

CM

sO

as

CMso

CJs CMOS OS

CM CM sO sO sO sO sO

Uoop

so

SO

UooQ

sO

00 5o

^3C

CO CO sO sO

CM CM so sO

UOOP

sO

CM

Uoop

so

SO

'oa

9/s
Table

A-1.

Ccontlnued)

OS X

00 6 ^ o CM CM NO CM 'O' cn 00 'O o o 00 00 NO 'a' C (0 00 r>. ON CM in 00 NO m NO 00 m 00 cn 'a* *H '

o o O 1^ o o iH o o o o o o iH O

X •>-) 60 ^ *e O o O o o o d d o o o o o O o

0)u

o

iJ

4J flj c u 8 0

0) 0) H 0 •HO-

•S5 B

u

Q>

M-iO <fl

O. (A 6 Cd

0) o

H

u

• Oj

CtO IS > o < hJ

(U o m

•-J a CO a cd

<U C I H

}-l . 0) CO a

> p. < ^3

O

H O

3 O

(U H

COc ^ dj :s M O'

4J W CO

o 'd' ON 00 00

CN m CO

cn cn

fO P>. 00 NO m CM CO miH cA ^ rCM CM CM CM ^ GO

CM CM

00m0000

CM

Cn

00

CM

VO O

CO ON

On on <r CM oiTi

IM rs. cn m cn cn rs u

(U rH iH iH CM CM CM rH rH rH rH CM rH

•u d O C O C o d d O o O O o O O

cMX

00 *H +1 -rl +1 +1 -H +1 •H +i +1 +1 +1 +1 +1 •H +1 •H ^a &

d) o NO NO ON NO o o NO On ON NO ON NO

Cd s CM CM o CM CM CM CM 'O cn 'O CM rH O CM E iH iH «—

1

rH rH rH iH iH rH rH rH iH rH rH

cd CM CM 00 o CO 00 ON CO in NO m 00 o

CJ 0 NO in CO in rH m CO ON in NO NO 00 00 00 On o X in in NO in m in in in m in in in in

rH ij

Cd z d o o o O o d d o o o o o o O

to 4J ^ 00 rH NO r>. rH o r>« CM r- CO 00 rH in CO

CO Cd CO CO CM o rH ON On in CM NO 00 ON •O 00

cd Pi « <r (O rH CO m NO in •o •<r 'd' •o m in s o o o O o o d d o o o o o o o

U o ^

•H rH <

c ^o CO

•H

4J • u u CJ CJ CJ CJ otf peS oi pH &

Fire Loca (Fig < A nJ Q U4 o X

ON ON ON ON vO

00

ON ON

CM CM vO vD

CM CM SO NO

ON

CM

NO

ON ON ON

o O IS cd •o 0 o

u /-S G c '3 U u u u u u u u u u M

00 0 CM •H •H c G O o o 0 o o o o 0 o 0

c 00 3 S •H •H O o o o o 0 o o o o o

•H *H • :s G G G G G G G G G G G

c IM oo rH rH

Q) c •H rH rH CO CO NO NO so NO NO NO NO NO so NO NO a o 3 3 's„. •OiNfc *•>„ "•»«.» •'•n. o o CM rH NO NO ‘O NO NO NO NO NO NO NO NO R

denotes

"raised"

burner
APPENDIX B. LISTINGS OF INTERMEDIATE RESULTS

The steady-state temperature, velocity, mass inflow, and mass outflow

results are presented in Tables B-3 to B-57. A key to these tablea is

presented in Table B-1 and Figure B-1. The opening velocity and temperature

results represent averages of 60 readings or scans taken at 5 second intervals, Room temperatures were recorded following each scan of the opening

sensors. Since the bidirectional probe array was shifted at least 6 and up to

18 times during a test, room temperatures represent averages of from 360

readings for the narrowest opening to 840 readings for the widest.

Accuracy of Temperature Results

Temperatures were measured with thermocouples formed by welding the

overlapping ends of 0.254 mm chromel and 0.254 mm alumel wires. Junction

diameters were approximately 0,51 mm. The limits of error associated with the

thermocouple wires and data recording system were found to be 1°C. These

limits do not include installation errors; e.g,, radiation error.

The thermocouple junctions which were used to measure the gas temperatures within the heated room were located within stainless steel tubes to form

aspirated thermocouples similar to the type described by Newman and

Croce . The limits of error associated with these units, including

radiation error, are estimated at +1/-3°C,

Superscripts in text refer to references at the end of this appendix.

27
The bare thermocouple junctions located within the opening were also

subject to radiation error. Error due to conduction along leads was minimized

by placing the leads in a horizontal (near Isothermal) plane. The radiation

error or difference between the opening gas temperature (T), and the thermocouple temperature (T^), is a function of T^ and the gas velocity (v) , At

locations in the inflow not near the neutral plane, the gas must be at ambient

temperature (T^), For the 55 flow experiments, the difference (T^ - T^)

at these locations ranged between -1 and -9®C, Near or above the neutral

plane, the difference or correction can be positive or negative depending on

the net radiative and convective heat transfer between the junction and its

environment. Table B-2 lists estimates of the range of the correction as a

function of T^. and v. These corrections are based on the heat transfer

analysis presented in Appendix C and selected experimental data representing

the full range of fire strengths, locations, and opening geometries. Tlie low

limit is based on the assumption that the maximum total radiation incident

upon a thermocouple near or above the neutral plane is equal to the maximum

total radiation incident upon any thermocouple in the cold inflow plus

radiation from the hot gas plume outside the opening. The high limit assumes

that the thermocouple is completely shielded from the hot environment and

views only an ambient environment. Consequently, the corrections in Table B-2

tend to be worst-case values. This is confirmed in part by a few Independent

corrections, also listed in Table B-2, which were obtained by extrapolating

opening temperature data from nearby 0,51 mm and 0.051 mm diameter thermocouples to "zero diameter" following the procedure outlined by Lee . The

jf 1°C error associated with the thermocouple wire and recording system has

been included in the corrections displayed in Table B-2.

28
Since the local mass flux (pv) varies at the listed temperature

uncertainties have a small effect on the opening mass flow rates. Table B-2

includes the uncertainty in mass flux associated with the listed temperature

uncertainties. In general, the effect is less than 2 percent.

Accuracy of Velocity Results

Opening velocities were determined with bidirectional velocity probes

B3 previously described by McCaffrey and Heskestad . The low sensitivity of

these devices to the angle of incidence of the flow required that care be

taken to allign the probe head parallel with the flow. Smoke-trace experiments indicated that the streamlines through the opening tended to be

horizontal at the mid-place of the jamb's depth. Consequently, probe heads

were located in the mid-plane of the jamb with their axes horizontal.

The velocity of the gas past the probe is given by the expression

V = C(Re)(p^Tj"^''^(2ApT)^^^ (B-1)

where C(Re) is a calibration factor which varies with Reynolds number

(Re), p^ is the density of air at T^, Ap is the pressure difference across the

probe head, and T is the absolute temperature of the gas. C(Re) is known

within 5 percent for Re between 40 and 3800 ; i.e. , for cold flow velocities

between 0.04 and 3.8 m/s. The differential pressures were measured with

Datametrics Model 570 transducers and Model 1014A electronic manometers.

Commercial products are neither endorsed nor necessarily recommended by the

National Bureau of Standards.

29
Because of limited primary standards, the manufacturer reports known system

accuracies as 0.1 percent at 1 torr, 5 percent at 10 torr, and 10 percent at

— 5 B4

10 torr . The manufacturer also states that the system appears linear

throughout this range. These accuracy figures are consistent with the 2

percent accuracy reported by McCaffrey for measurements made with these

-2 -3

systems at 6.2 x 10 and 1.7 x 10 torr. Since opening gas temperatues were

known within 5 percent for v > 0.1 m/s (see Table B-2), the maximum possible

error associated with v due to uncertainties in C(Re), Ap, and T is 10

percent. For v < 0.1 m/s, the maximum possible error is at least 13 percent. Nevertheless, velocities in this regime constitute a small fraction of

the results and account for less than 1.5 percent of the opening mass flow in

any given experiment.

Accuracy of Mass Flow Results

Based on the accuracies of C(Re), Ap, and T, and provided the streamlines

were normal to the opening at the measurement points, the maximum error

associated with the mass flow results is expected to be approximately 10

percent. Differences between experimental inflow and outflow rates are

consistent with this figure. For a given experiment involving a doorway or

the largest window, mass inflow and outflow rates are within 5 percent of

their average value. This deviation Increases to 8 percent for the smaller

window configurations.

30
References

Bl. Newman, J.S, and Croce, P.A., A Simple Aspirated Thermocouple for Use in

Fire, Journal of Fire and Flammability 10, 326 (1979).

B2, Lee, B.T., Thermocouple Size and Temperature Measurement in Room Fires,

Memorandum, Center for Fire Research, National Bureau of Standards

(U.S.), May 1977.

B3. McCaffrey, B.J. and Heskestad, G. , A Robust Bidirectional Low Velocity

Probe for Flame and Fire Applications, Combustion and Flame 10, 326

(1976).

B4. Datametrics Inc., Datametrics Barocel Vacuum/Pressure Measurement Systems

and Accessories, Bulletin No. 2005, Datametrics, Inc., Wilmington, MA.

B5. McCaffrey, B.J. , A Portable, Stable Low Differential Pressure Calibration

Source, Memorandum, Center for Fire Research, National Bureau of

Standards (U.S.), October 1976.

31
Table B-1

Key to intermediate results

(see Fig. B-1)

Temperature (“C)

>K

>K

>k 18

T3

0) iJ <U o a Room

21 0) cS C Cl

. / / /

20 C CO 0 140.14 \ 144. 16 ; 144. 12 c 19 u

18

17 32.36 144.37

16 31.03 143.69

15 3G.32 142.87 t 14 142.34

13 140.84

12 138.31

11 133.43

10 121.29

9 103.21

Opening (looking into room)

->1 AX K88. 5S

76.83

142.68

132.77

110.32

92.55

83.98

60.23

44.52

33.43

35.98

34.47

33. 17

142.72

139.86

138.98

137.30

132.96

103.57

39.27

33.51

32.77

32.30

32.81

142.00

136.93

135.85

133.26

131.71

108.43

42.86

33.58

32.14

32. 18

32.39

140.99

136.55

134.20

132.38

129.03

107.57

45.71

33. 14

31.84

31.75

31.98

141.63

137. 14

134.63

132.63

129.85

111.05

42.06

32.38

31.38

31.58

31.31

141.11

137.91

135.70

133.03

130.40

107.64

35.15

31.37

30.93

30.70

30.91

142.61

^

soffit

139.53

i

137.24

128.54

115.47

83.06

41.20 ^ 33.23 T

30.27

30.22

29.95

AZ

sill

6 65.06 ^ 32.43 32.44 32.02 31.31 31.55 30.89 30.15 y 5 56.40 o 33.01 .32 . 45 31.81 31.38 31.04 30.70 30.18 ' 7 f f 4 53.54 ^ 32.80 32.24 32.04 31.26 31.62 30.88 30.25

3 52.00 y 32.83 32.23. 31.72 31.35 31.02 30.57 30.05

2 51.74 J(C 32.85 32.34 32.41 31.70 31.94 31.25 30.50

> ^ / r / >• /

VELOCITY, (m/s) (looking into room)

soffit 0 .- 0 .- 0 .- 0. 0. 0. 0 . 0

.- - 0 . 17 0. 2.22 2. 15 2.11 2.07 2.11 2. 13 2.26 0.

16 0. 1.79 1.63 1.51 1.48 1.49 1.58 1.84 0.

15 0. 1.44 1.41 1.28 1.23 1.27 1.37 1.62 0.

14 0. 1.15 1.12 1.04 1.02 1.05 1.14 1.29 0.

13

j.

0- 0.76 0.84 0.78 0.77 0.79 0.84 0.92 0.

12

i 0:

0.27 0.45 0.47 0.48 0.51 0.49 0.33 0.

11 -0.47 -0.47 -0.43 -0.39 -0.40 -0.51 -0.46 0.

10 T 0. -0.87 -0.73 -0.68 -0.66 -0.66 -0.73 -0.85 0.

9 0. -1.04 -0.84 -0.77 -0.75 -0.78 -0.87 -1.06 0.

8 0. -1.16 -0.95 -0.88 -0.87 -0.86 -0.96 -1.19 0.

7 0. -1.28 -1. 10 -1.05 -1.03 -1.06 -1.14 -1.38 0.

6 sill 0 . -1.46 -1.43 -1.43 -1.44 -1.43 -1.46 -1.50 0.

5 —>. 0 — -• 0. • 0. • - 0. - 0. • - 0.- - 0. - 0.- - 0.

4 0. 0. 0. 0. 0. 0. 0. 0. 0.

3 0. 0. 0. 0. 0. 0. 0. 0. 0.

2 0. 0. 0. 0. 0. 0. 0. 0. 0.

1 0. 0. 0. 0. 0. 0. 0. 0. 0.

A

Lleft jamb

1^

AX

right jamb
Fig. B-1 Sensor locations with dimensions

in m.

0.14

o Thermocouple locations • Thermocouple and

velocity probe locations

33
Table B-2

Corrections for opening thermocouples near or above

neutral plane and attendant percent change in mass flux

T-T^

[ra"(T) - m"(T^)]/m"(T^)

T

^

t (°C)

V

(m/s)

< 0.1 0.1 - 0.6 0.6 - 1.2

'

> 1.2

< 50 -20/+2°C

+3 .3/-0.4%

-14/+2"C

+2.2/-0.4%

50 - 100 -11/+4°C

+1.5/-0.5%

-14/+4“C

+2.2/-0.5%

-9/+4“C

+l.l/-0.5%

-2/+4“C

+0.4/-0.5%

100 - 150 -8/+rc (-5®C)*

+l.l/-0.9%

-5/+6‘*C

+0.8/0. 7%

-9/+T’C (+1“C)*

+l.l/-0.8%

-2/+6“C (+2°C)*

0.2/-1.2%

150 - 200 -5/+ll®C (+6“C)*

+0.5/-l.l%

-2/+10“C

+0.2/-1.0%

200 - 250 -1/+15*C

0. 1/1.4%

-5/+13°C (+5,+3°0*

0.5/-1.2%

> 250 -4/+16“C

+0.4/1. 5%

-3/+16°C

+0.3 /-I. 4%

Corrections obtained by linear extrapolation of 0.51 mm and 0.051 mm

diameter thermocouple data to "zero diameter".

34
Table B-3

Test 10; 2/6 door, 62.9 kW, location A

TEMPERATURE (°C)

>K21

20 184.79

19 192.98

18 193. 14

17 26.96 193.06 194.06 192.72 190.92

16 25.89 191.98 189.87 187.63 188.93

15 25.32 190.51 183.95 182.60 183.96

14 190.75 182.86 182.03 181.62

13 190.24 186.03 180.88 179.99

12 189.25 171.64 179.12 178.27

11 188.24 154.79 172.49 173.26

10 187 . 13 115.69 129.20 146.42

9 184.70 31.14 32.71 44.93

8 177.23 28.67 26.68 26.68

7 135,48 27.46 27.60 26.47

6 96.70 27.53 26.68 26.60

5 82.38 26.81 26.41 25.73

4 71.90 27.28 25.95 26. 14

3 67.72 27.98 28.08 26.79

2 65.52 28.54 27.54 27.98

)K

>k VELOCITY

18 0 . 0 . 0 . 0 . 0 . 17 0 . 3.30 3.12 3.17 0 . 16 0 . 2.80 2.62 2.77 0 . 15 0 . 2.55 2.38 2.57 0 . 14 0 . 2.33 2.17 2.31 0 . 13 0 . 2.03 1.85 1.93 0 . 12 0 . 1.63 1.54 1.58 0 . 11 0 . 1.27 1.18 1.24 0 . 10 0 . 0.62 0.59 0.70 0 . 9 0 . -0.64 -0.58 - 0.53 0 . 8 0 . - 1.01 -0.91 - 1.02 0 . 7 0 . - 1.25 - 1.18 - 1.37 0 . 6 0 . - 1.47 - 1.33 - 1.43 0 . 5 0 . - 1.55 - 1.45 - 1.67 0 . 4 0 . - 1.62 - 1.53 - 1.71 0 . 3 0 . - 1.70 - 1.64 - 1.85 0 . 2 0 . - 1.77 - 1.71 - 1.87 0 .

1 0 . 0 . 0 . 0 . 0 . >K

>u

AX = 0.067 m

AZ = 0.114 m

Z = 0.912 m

nOutflow rate = 0.247 kg/s

Inflow rate = 0.255 kg/s

Outdoor temperature = 21.9-23.9°C

35
Table B-4

Test 11; 3/6 door, 62.9 kVJ, location A

TEMPERATURE ( C) *

21

20

19

13

17 28.79

159.39

165.81

165.97

166. 19 164.49 164. 13

16 28. 12 165.44 161.46 160.01

15 27.54 164.34 154.71 158.32

14 164.51 151.84 156.96

13 163.99 150.87 156.67

12 163.07 136.59 153.11

11 162.02 114.66 136.90

10 160.11 55.21 77. 13

9 150.69 33.29 31.40

8 113.62 29.98 30.08

7 83.38 29.41 30.38

b 71.28 29.67 30.35

5 64.89 29.33 29.76

4 61.07 29.21 30. 10

3 58.52 30.51' 30.88

2 56.44 30.66 31.35

>f<

VELOCITY

>k 18 0. 0. 0.

17 0. 2.90 2.76

16 0. 2.47 2.20

15 0. 2. 18 2.00

14 0. 1.96 1.76

13 0. 1.65 1.49

12 0. 1.30 1.20

11 0. 0.93 0.88

10 0. -0.03 0.25

9 0. -0.70 -0.62

8 0. -0.96 -0.83

7 0. -1.10 -1.00

6 0. -1.21 -1.11

5 0. -1.28 -1.18

4 0. -1.34 -1.25

3 0. -1.40 -1.33

2 0. -1.46 -1.37

1 0. 0. 0.

5K

AX = 0.065 m

AZ = 0.114 m

Z = 0.940 m

nOutflow rate = 0.357 kg/s

Inflow rate = 0.358 kg/s

Outdoor temperature = 24.6-25.8°C

36

163..61 163..13 163.,12

159.,84 160,,33 160.,83

156..00 156.,45 160.,40

156.,42 156.,50 157.,81

153..83 154.,77 158.,05

152..66 152.,59 154.,34

140.,63 141.,49 140.,77

95..96 102.,89 102.,02

30..86 31..48 31.,48

29..83 28..78 28..81

30,. 14 29..75 27..94

30,.25 29,.01 28..66

28,.99 28,.60 27..48

29,,51 28,.39 28,.24

30,.76 30,.41 28,. 18

31,, 15 30,.57 29,.69

0. 0. 0 . 0.

2.69 2.74 2.82 0.

2. 17 2.20 2.41 0.

1.93 1.98 2.23 0.

1.72 1.78 2.05 0.

1.42 1.49 1.71 0.

1.15 1.20 1.37 0.

0.87 0.92 1.02 0.

0.36 0.43 0.42 0.

-0.61 -0.60 -0.68 0.

-0.81 -0.84 -1.00 0 . -0.98 -1.01 -1.20 0.

-1.07 -1.13 -1.29 0.

-1.16 -1.21 -1.40 0 . -1.21 -1.28 -1.49 0.

-1.30 -1.32 -1.55 0.

-1.32 -1.37 -1.57 0.

0. 0. 0. 0.
Table B-5

Test 12; 4/6 door, 62.9 kW, location A

TEMPERATURE (°C)

He21

20 136.57

19 141.75

18 141.71

17 23.92 141.97 139.40 139.63 139.99 139.23 139.92

16 22.65 141.37 135.78 137.41 135.24 136.25 137.40

15 21.90 140.83 129.47 135 . 16 133.63 133.65 137. 16

14 140.85 115.54 134.26 131.56 132.93 135.79

13 140.53 116.78 133.36 130.29 131.47 134.83

12 139.99 103.87 131.48 126.60 128.69 131.13

11 138.74 85.28 97.49 110.53 107.84 107.81

10 132.77 45.55 42.04 53.71 56.45 53.73

9 97 . 12 26.84 24. 18 24.74 23.80 24.99

8 70 , 13 24.56 23.64 23.54 23.23 23.07

7 58.28 25.02 23.93 24.29 24.00 23.38

6 53.40 24.96 23.79 23.90 23.73 22.80

5 49.76 23.95 23.39 23.05 22.71 22.99

4 47.34 23.91 23.40 22.85 22.75 22.42

3 45.23 24.80 24. 18 24.27 23.97 23.25

2 43.83 25.43 24.32 24.29 24.32 23.81

H<

H<

. VELOCITY (m/s)

>k 18 0 . 0 . 0 . 0 . 0 . 0 . 17 0 . 2.67 2.53 2.51 2.51 2.62

16 0. 2.24 1.98 1.92 1.96 2. 18

15 0 . 1.96 1.75 1.70 1.74 1.97

14 0 . 1.63 1.53 1.45 1.54 1.79

13 0 . 1.34 1.27 1.19 1.25 1.52

12 0 . 1.06 0.97 0.95 0.97 1.25

11 0 . 0.73 0.70 0.72 0.72 0.82

10 0 . -0.22 -0.20 0.07 0. 13 0. 17

9 0 . -0.73 - 0.64 -0.58 -0.62 -0.71

8 0 . - 0.92 -0.77 -0.72 -0.75 -0.92

7 0 . -0 . 96 -0.85 -0,81 -0.86 - 1.03

6 0 . - 1.03 - 0.95 -0.91 - 0.96 - 1.14

5 0 . - 1,08 - 1.01 - 0.96 - 1.03 - 1.23

4 0 . - 1.15 - 1.06 - 1.03 - 1.07 - 1.34

3 0 , - 1.17 - 1.11 - 1.07 - 1.12 - 1.40

2 0 . - 1.20 - 1.14 - 1.09 - 1.15 - 1.40

1 H<

>K

0 . 0 . 0 . 0 . 0 . 0 .

AX = 0, 098 m

AX = 0. 114 m

Z = 0. 971 m

nOutflow rate

Inflow rate = 0.454 kg/s

Outdoor temperature = 18.7-20.0 C

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

37
Table B-6

Test 612; 4/6 door, 62.9 kV^/, location A

TEMPERATURE (°C)

»21

20 130.80

19 135.82

18 136.09

17 14.92 136.08 132.18 132.57 132.65 132.48 131.39

16 135.63 132.13 130.77 128.37 127.45 127.61

15 135.10 122.36 128.92 128.35 128.29 127.87

14 13.63 135.25 114.44 129.50 127.38 126.71 125.14

13 134.79 103.68 129.24 127.39 126.68 115.00

12 133.73 96.46 125.62 122.11 122.14 116.43

11 131.73 71.98 89.51 98.02 102.53 92.48

10 13.02 119.43 26.93 28.31 41.26 31.36 37.83

9 80.92 16.28 15.57 15.38 15.06 17.28

8 58.12 15.37 15.03 14.95 14.14 14.89

7 47.84 16.82 16.29 16.40 15.62 13.09

6 12.48 42.08 16.90 16.48 16.70 14.69 12.88

5 38.26 17.11 15.67 14.67 13.72 12.48

4 36.04 18.05 16.39 14.95 13.06 12.22

3 34.06 16.43 15.89 15.98 15.77 15.03

2 « 13.55 33.64 16.32 16.64 16.56 15.86 15.33

« VELOCITY

18 0.00 0.00 0.00 0.00 0.00 0.00 0.00

17 0.00 2.62 2.12 2.49 ' 2.50 2.66 0.00

16 0.00 2.31 2.02 1.96 2.01 2.25 0.00

15 0.00 1.99 1.56 1.75 1.81 2.05 0.00

14 0.00 1.74 1.59 1.53 1.62 1.78 0.00

13 0.00 1.41 1.17 1.23 1.28 1.39 0.00

12 0.00 1.11 0.98 0.96 0.99 1.22 0.00

11 0.00 0.68 0.59 0.73 0.75 0.80 0.00

10 0.00 - 0.28 -0.23 0.11 -0.23 0.20 0.00

9 0.00 -0.65 -0.50 -0.58 -0.60 -0.68 0.00

B 0.00 -0.84 -0.72 -0.71 -0.76 -0.85 0.00

7 0.00 - 1.03 -0.80 -0.86 -0.88 - 1.02 0.00

6 0.00 - 1.09 -0.94 -0.92 -0.98 - 1.15 0.00

5 0.00 - 1.15 -0.93 -0.97 - 1.02 - 1.21 0.00

4 0.00 - 1 . 16 - 1.04 - 1.00 - 1.08 - 1.33 0.00

3 0.00 - 1.19 - 1.00 - 1.05 - 1.09 - 1 .40 0.00

2 0.00 - 1.21 - 1.08 - 1.06 - 1.15 - 1.41 0.00

1 0.00 0.00 0.00 0.00 0.00 0.00 0.00

•»«

AX = 0.098 m

AZ = 0.114 m

Z = 0.981 m

nOutflow rate * 0.467 kg/s

Inflow rate = 0.463 kg/s

38
Table B-7

Test 13; 5/6 door, 62.9 kW, location A

TEMPERATURE (° C )

>k21

20 125.84

19 130.24

18 130.13

17 24.07 130.41 125.07 125.69 124.65 124.86 128. 14 127.54 129.41

lb 23.30 129.95 123.01 123.23 122.70 121.38 121.67 124.91 127.16

15 22.81 129.58 114.68 124.26 121.70 121.28 122.88 123.05 127.28

14 129.58 102.94 123.84 121.59 119.41 120.30 122.24 124.35

13 129.26 94. 15 123.26 119.64 117.87 119.80 122.03 122.56

12 128,61 79.73 114.61 113.97 112.06 112.98 114.92 114.36

11 126.28 47 . 10 61.58 77.36 83.08 92.04 87.50 79.47

10 106.81 35.94 32.73 36.68 42.82 45.79 43.88 41.44

9 72.78 26.51 24.65 25.00 25 . 16 24.74 24.11 25.55

3 58 .. 30 26.30 24.27 24 . 19 24.33 24. 10 24.05 25.62

7 51.69 26.09 24.45 24.77 24.92 25. 18 24.26 24.89

6 48.51 27. 16 24.34 24.47 24.76 24.69 24.36 24.60

5 45.68 24.39 24.30 24.20 23.99 23.95 23,66 24.56

4 43.65 24.35 24.20 24.05 23.83 23.85 23.93 24. 13

3 41.52 25.60 24.81 25.26 25.48 25.50 25.07 25.25

2 40.31 26.96 25 . 10 ' 25.28 25.36 25.65 25.99 25.52

VELOCITY

18 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 17 0 . 2.50 2.38 2.41 2.35 2.31 2.35 2.55 0 . 16 0 . 2.07 1.84 1.77 1.72 1.75 1.87 2.03 0 . 15 0 . 1.77 1.61 1.53 1.50 1.55 1.61 1.84 0 . 14 0 . 1.46 1.42 1.32 1.27 1.33 1.44 1.60 0 . 13 0 . 1.11 1.12 1.04 1.03 1.03 1.12 1.39 0 . 12 0 . 0.77 0.79 0.79 0.83 0.85 0.89 1.07 0 . 11 0 . 0.29 0.43 0.50 0.55 0.58 0.58 0.61 0 . 10 0 . - 0.37 -0.36 -0.30 -0.21 -0. 16 -0. 18 -0. 18 0 . 9 0 . - 0.66 - 0.61 -0.56 - 0.56 -0.56 -0.62 -0.66 0 . 8 0 . - 0.72 -0.73 -0.67 -0.65 -0.68 -0.74 -0.74 0 . 7 0 . - 0.84 -0.77 - 0.73 - 0.74 -0.75 -0.84 -0.92 0 . 6 0 . - 0.88 -0.86 - 0.81 - 0.80 -0.82 -0.90 - 0.95 0 . 5 0 . - 0.98 - 0.91 - 0.86 -0.85 -0.87 -0.96 - 1.10 0 . 4 0 . - 1.03 - 0.97 - 0.91 -0.90 -0.91 -0.97 - 1.20 0 . 3 0 . - 1.04 - 0.98 -0.93 -0.91 -0.93 - 1.02 - 1.22 0 . 2 0 . - 1.06 - 1.02 -0.92 - 0.93 -0.95 - 1.04 - 1.26 0 .

1 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 .

AX = 0.086 m

AZ = 0.114 m

Z = 1.010 m

nOutflow rate = 0.527 kg/s

Inflow rate = 0.519 kg/s

Outdoor temperature = 18.2-21.7°C

39
Table B-8

Test 14; 6/6 door, 62.9 kW, location A

TEMPERfiTURE ( Oc ) *

21

20 125.15

19 129.26

13 129.32

1 ? 30.33 129.63 130.72 130.90 129.89 128.58 128.31 129.03 126.27

IS 29.52 129. 19 129.78 127.61 125.52 124.36 124.03 125.26 125.77

15 28.89 128.77 122.47 128.61 123.65 122.18 122.80 125.54 121.84

14 128.80 110.68 127.12 122.93 120.48 122.11 123.94 117.94

13 123.37 98.79 124.68 120.67 117.03 119.81 120.70 88.35

12 127.28 90.43 110.16 109.72 108.55 107.08 107.95 83.81

11 122.82 58.65 64.71 74.71 75.98 68.06 53.01 47.93

10 95.27 41.10 38.97 44.48 43.44 35.85 31.69 33.87

9 66.22 33.70 32.97 33.34 31.61 30.56 29.71 29.99

8 56.60 33. 13 32.14 32.16 30.88 30.12 29.50 29.59

7 51.77 33.75 32.82 32.72 31.90 31.06 29.88 29.00

6 48.99 33.61 32.29 32.53 31.75 30.71 29.67 28.85

5 46.75 32.69 32.02 31.48 30.57 29.98 29.42 28.71

4 45.70 32.97 31.70 31.54 30.66 29.95 29.22 28.87

3 44.34 35.64 32.84 . 33.34 32.84 32.27 31.37 29.48

2

>k 44.20 36. 19 32.90 33.43 33.40 32.96 31.29 30.06

>K

>k 13

VELOCITY ( m/ s )

0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 17 0 . 2.39 2.25 2. 18 2.15 2.21 2.34 2.42

16 0 . 1.94 1.73 1.66 1.62 1.67 1.75 1.95

15 0 . 1.61 1.51 1.43 1.37 1.45 1.54 1.62

14 0 . 1.27 1.26 1.16 1.15 1.24 1.32 1.34

13 0 . 1.10 0.96 0.94 0.91 0.88 0.97 0.83

12 0 . 0.83 0.73 0.76 0.76 0.70 0.71 0.67

11 0 . 0.33 0.32 0.35 0.39 0.37 0.25 0.22

10 0 . -0.37 -0.31 -0.20 -0.20 -0.33 -0.40 -0.34

9 0 . - 0.62 -0.49 -0.45 -0.47 -0.51 -0.59 - 0.57

3 0 . -0.73 -0.59 -0.55 -0.60 -0.64 -0.70 -0.69

7 0 . -0.82 -0.69 -0.62 -0.64 -0.70 -0.78 -0.76

6 0 . -0.89 -0.76 -0.72 -0.73 -0.76 -0.85 -0.89

5 0 . -0.94 -0.79 -0.73 -0.74 -0.77 -0.88 -0.91

4 0 . -0.99 -0.85 - 0.79 -0.77 -0.80 -0.91 - 1.00

3 0 . - 1.03 -0.89 -0.76 -0.79 -0.83 -0.95 -0.85

2 0 . - 1.07 - 0.93 - 0.84 -0.82 -0.86 -0.99 -0.86

1 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . >K

>K

AX " 0 . 106 ra AZ = 0.114 m

Z = 1.027 m

nOutflow rate = 0.571 kg/s

Inflow rate = 0.554 kg/s

Outdoor temperature — 27.2-29.6°C

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

40
Table B-9

Test 18; 6/6 door, 62.9 kW, location A

TEMPERATURE ( C)

>k21

20 126.71

19 130.73

18 130.73

17 31.92 131.15 131.55 129.99 129.20 131.22 129.93 130.03 129.85

16 31.09 130.76 127.87 127.95 124.85 125.45 126.88 127.44 128.35

15 30.56 130.47 121.69 127.16 123.94 123.77 124.43 126.60 126. 17

14 130.56 105.43 127.46 122.09 121.97 124.97 126.25 119.93

13 130. 18 95.32 124.04 120. 17 119.30 120.65 121.25 96.77

12 129. 17 86.24 109.63 109.18 109.20 108.42 108.89 89.67

11 124,79 57.06 63.61 76.73 77.37 65.69 56. 12 58.39

10 97.62 42 . 95 39.89 43.93 43.32 35.60 33.39 40.24

9 68,20 34.60 33.92 34. 16 33.25 32.33 31.70 34.59

0 59.05 34.32 33.21 33.08 32.94 32.37 31.39 34.77

7 54.36 34.64 33.69 33.96 34.05 33.11 32.02 32.49

b 51.62 35.09 33.50 33.53 33,94 33.21 31.73 32.11

5 49 . 33 33.35 32.86 32.93 32.77 32 . 23 31.52 32.05

4 43.11 33.65 32.83 32.52 32.70 32.41 3 1 . 36 31.58

3 4S . 77 35.52 33.79 34.59 35.22 34.72 33.96 32.52

2 46 . 9

37.32 34.24 '34.66 35.23 35.08 33.97 33.46

>k

>K 18

VELOCITY

0. 0. 0. 0. 0. 0. 0. 0.

17 0. 2.42 2.28 2.23 2.24 2.29 2.31 2.47

16 0. 1.93 1.75 1.67 1.62 1.66 1.77 1.97

15 0. 1.59 1.50 1.41 1.39 1.48 1.53 1.64

14 0. 1.27 1,25 1.16 1.15 1.22 1.32 1.31

13 0. 0.99 0.93 0.92 0.90 0.83 0.88 0.84

12 0. 0,79 0.72 0.72 0.71 0.67 0.67 0.65

11 0. 0.28 0.31 0.38 0.39 0.33 0,24 0.30

10 0. -0.36 -0.30 -0,22 -0.24 -0.36 -0.44 -0.17

9 0. -0.59 -0.47 -0.44 -0.47 -0.52 -0.57 -0 . 47

0 0. -0.71 -0 . 59 -0 , 53 -0.56 -0.60 -0.70 -0.45

7 0. -0.80 -0.67 -0.64 -0.64 -0.72 -0.80 -0.72

6 0. -0.86 -0.75 -0.70 -0.71 -0.74 -0.88 -0.78

5 0. -0.94 -0.80 -0.75 -0.73 -0.79 -0.87 -0.98

4 0. -0.97 -0.85 -0.78 -0.77 -0.79 -0.93 -1.08

3 0, -1.06 -0.89 -0.82 -0.80 -0.85 -0.93 -1.17

2 0. -1.08 -0.93 -0.84 -0.82 -0.86 -0.99 -1.20

1 0. 0. 0. 0. 0, 0. 0. 0.

5i<

>k

AX = 0.106 m

AX = 0.114 m

Z = 1.026 m

nOutflow rate = 0.567 kg/s

Inflow rate = 0.553 kg/s

Outdoor temperature = 28.9-29.4°C

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

41
Table B-10

Test 710; 6/6 door, 62.9 kW, location A

TEMPERATURE (°C)

21

20 107.75

19 109.83

18 109.78

17 13.38 109.78 102.48 104.06 105.99 107.58 107. 14 106.58 107.61

18 109.81 97.71 104.43 102.22 104.08 102.80 104.56 106.76

15 109.84 75.08 101.42 102.05 102.95 102. 19 103.78 106.00

14 11.82 109.53 59.10 102.60 99.60 100.57 99.75 102.33 104.43

13 108.96 55.61 97.81 97.70 98.74 98.62 99.90 99.12

12 106.61 54.25 81.31 85.05 88.62 86.96 89.58 90.31

11 92.82 26.43 44.76 45.60 57.80 59.31 62.50 65.42

10 11.70 65.77 15.64 15.73 18.90 26.19 23.56 24.81 26.66

9 49.50 12.73 12.77 12.91 14.85 14.33 14.61 15.96

8 40.21 12.69 11.99 12.17 12.62 13.51 13.48 13.78

7 35.71 13.61 12.80 13.05 14.32 14.86 14.75 13.36

8 10.82 32.89 13.48 12.49 13.08 14.13 15.01 14.67 13.36

5 30.10 18.47 13.01 12.84 13.17 13.10 13.12 12.35

4 28.03 14.19 12.68 12.88 12.76 13.35 12.98 12.18

3 26.04 10.90 12.09 12.30 13.21 13.56 14.09 14.07

2 12.20 25.48 12.15 12.79 12.90 13.15 14.02 14.24 14.05

•» VELOCITY

1r 18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

17 0.00 2.38 2.30 2.30 2.24 2.27 2.28 2.36 0.00

16 0.00 1.93 1 .81 1 .68 1.67 1.70 1.78 2.01 0.00

15 0.00 1.56 1.55 1.47 1.42 1.47 1 .57 1.73 0.00

14 0.00 1.19 1.30 1.20 1.22 1.25 1.33 1.66 0.00

13 0.00 0.92 1.04 0.95 1.01 1.03 1.05 1 .30 0.00

12 0.00 0.72 0.81 0.86 0.86 0.81 0.85 0.98 0.00

11 0.00 0.29 0.44 0.40 0.48 0.51 0.51 0.58 0.00

10 0.00 -0.42 -0.38 -0.33 -0.22 -0.26 -0.26 -0.19 0.00

9 0.00 -0.60 -0.54 -0.51 -0.45 -0.50 -0.56 -0.52 0.00

a 0.00 -0.73 -0.62 -0.61 -0.60 -O.SO -0.64 -0.73 0.00

7 0.00 -0.80 -0.72 -0.70 -0.72 -0.73 -0.79 -0.89 0.00

6 0.00 -0.86 -0.75 -0.75 -0.75 -0.76 -0.83 -0.99 0.00

5 0.00 -0.88 -0.79 -0.76 -0.78 -0.78 -0.87 - 1 .07 0.00

4 0.00 - 0.93 -0.83 -0.79 -0.80 -0.82 -0.91 - 1.11 0.00

3 0.00 - 1.01 -0.87 -0.84 -0.83 -0.87 -0.95 - 1.18 0.00

2 0.00 - 1.04 -0.93 -0.88 -0.86 -0.86 -0.96 - 1.19 0 . 00'

1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

AX = 0.106 m

AZ = 0.114 m

Z = 1.016 m

nOutflow rate = 0.643 kg/s

Inflow rate = 0.605 kg/

s

42
Table B-11

Test 810; 6/6 door, 62.9 kW, location A

I TEMPERATURE ( 0-)

21

20 113.01

19 116.10

18 116.16

17 15.05 116.13 111.80 111.98 112.17 111.13 111.64 111.71 112.15

16 115.90 111.64 112.15 108.80 110.45 109.55 112.04 110.40

15 115.79 106.94 109.09 108.51 106.41 107.91 109.51 106.77

14 13.42 115.79 74.66 110.81 107.30 106.46 107.56 111.91 102.44

13 115.35 68.25 106.77 105.19 102.23 105.00 108.30 94.82

12 113.64 66.77 89.36 88.37 88.51 92.36 96.86 90.45

11 102.21 35.98 49.14 56.60 57.88 54.47 57.99 53.92

10 12.51 66.32 18.30 18.69 26.14 24.59 18.15 16.70 21.08

9 47.67 15.13 15.75 15.28 15.34 15.09 15.81 18.45

8 39.68 14.59 14.29 14.40 14.80 14.85 15.15 15.96

7 35.60 16.02 15.74 15.57 15.91 15.89 14.83 14.27

6 12.21 33.04 16.06 15.38 15.75 18.62 15.98 14.63 13.96

5 30.64 17.01 15.64 15.01 15.15 14.69 14.15 13.66

4 28.95 16.98 16.16 15.50 15.79 14.68 13.98 13.13

3 27.23 15.49 15.34 15.41 15.74 15.95 15.89 15.95

2

« 13.71 27.53 15.26 15.34 15.93 16.62 16.25 16.35 15.98

*

jt VELOCITY

If 18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

17 0.00 2.35 2.28 2.21 2.20 2.23 2.25 2.42 0.00

16 0.00 2.01 1.81 1.69 1.64 1.71 1.81 2.01 0.00

15 0.00 1.70 1.57 1.43 1.41 1.47 1.55 1.63 0.00

14 0.00 1 . 12 1.27 1.23 1.19 1.25 1.37 1.38 0.00

13 0.00 0.98 0.93 0.96 0.94 0.95 1.02 1.24 0.00

12 0.00 0.81 0.78 0.70 0.69 0.77 0.80 0.95 0.00

11 0.00 0.33 0.37 0.43 0.41 0.42 0.45 0.49 0.00

10 0.00 -0.44 - 0.32 -0.18 -0.25 -0.36 -0.43 -0.17 0.00

9 0.00 -0.62 -0.49 -0.48 -0.47 -0.53 -0.57 -0.38 0.00

8 0.00 -0.74 -0.63 -0.57 -0.58 -0.61 -0.68 - 0.62 0.00

7 0.00 -0.85 -0.72 -0.68 -0.67 -0.71 -0.80 -0.71 0.00

6 0.00 -0.88 -0.80 - 0.73 -0.73 -0.76 -0.85 -0.80 0.00

5 0.00 -0.94 -0.82 - 0.78 -0.75 -0.79 -0.88 -0.93 0.00

4 0.00 - 0.94 - 0.85 -0.79 - 0.79 - 0.82 -0.92 - 1.06 0.00

3 0.00 -0.97 - 0.83 -0.81 -0.79 -0.85 -0.94 - 1.21 0.00

2 0.00 - 1.00 - 0.89 -0.85 - 0.82 -0.87 -0.97 - 1.23 0.00

1 **0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

AX = 0. 106 m

AZ = 0. 114 m

z = 0. 019 m

nOutflow rate = 0. 616 kg/s

Inflow rate = 0,,593 kg/s

43
Table B-12

Test 16; 7/6 door, 62.9 kW, location A

TEMPERATURE

*

21

20 116.35

19 119.95

18 119.93

1? 28.41 120.26 117.26 115.60 118. 16 116.54 116.29 117.26 117.27 118.16 118.69

16 27.11 119.72 112.14 115.00 114.93 112.34 112.99 114.49 115.24 115.78 118.91

15 26.29 119.49 103.35 115.60 114.71 111.24 109.84 110.35 110.96 114.52 118.01

14 119.33 80.74 113.13 113.99 110.07 108.14 109. 14 109.95 112.79 116.28

13 118.53 64.85 103.66 107.61 103.35 101.68 101.93 106. 17 109.65 107.72

12 115.03 51.00 78.22 78.82 84.94 87.06 88.71 89.05 93.26 89.64

11 95.06 38.75 36.67 45.32 53.66 57.42 57.79 55.75 54.40 46.19

10 64.41 34.39 30.70 32.52 35.12 36.49 36.71 36.21 33. 18 30.89

9 52.72 30.83 28.91 28.79 29.73 29.31 28.71 27.23 27.44 28.68

8 48 . 25 29.66 27.83 27.96 28.24 28.09 28.09 27.66 27.29 27.65

7 45.60 31.35 28.33 28.68 29. 12 28.85 28.41 27.53 27.49 26.70

6 43.66 30.90 27.79 28.05 28.70 28.56 28.49 28.09 27.57 26.61

5 41.60 28.92 28.48 28.41 28.11 27.87 27.75 26.85 26.77 26. 19

4 40.31 29.49 28. 14 27.86 27.77 27.81 27.90 27.77 27.11 26.27

3 38.75 32.61 28.69 29.48 29.66 29.55 29.16 28.88 29.06 27.46

2

H< 37 . 79 32.90 28.57 29.26 29.65 29.63 29.89 29.96 29.34 28.49

>»<

>K IS

VELOCITY

0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0

17 0. 2.31 2.25 2.22 2.16 2. 12 2.10 2.09 2.13 2.31 0

16 0. 1.85 1.71 1.62 1.57 1.53 1.48 1.57 1.63 1.79 0

15 0. 1.45 1.49 1.47 1.29 1.24 1.23 1.32 1.42 1.57 0

14 0. 1.03 1.14 1.11 1.04 1.02 1.05 1.12 1.21 1.42 0

13 0 . 0.65 0.80 0.74 0.84 0.88 0.89 0.91 0.94 1.21 0

12 0. 0.38 0.58 0.56 0.65 0.66 0.68 0.71 0.74 0.81 0

11 0. -0. 10 -0. 13 0. 13 0.25 0.29 0.32 0.32 0.29 0.28 0

10 0. -0.39 -0.39 -0.33 -0.28 -0.24 -0.25 -0.26 -0.30 -0.31 0

9 0. -0.52 -0.47 -0.45 -0.41 -0.42 -0.47 -0.49 -0.50 -0.43 0

8 0 . -0.64 -0.59 -0.54 -0.51 -0.50 -0.53 -0.54 -0.56 -0.59 0

7 0. -0.70 -0.61 -0.60 -0.58 -0.58 -0.59 -0.64 -0.70 -0.73 0

6 0. -0.78 -0.69 -0.65 -0.64 -0.63 -0.63 -0.66 -0.71 -0.84 0

5 0. -0.84 -0.73 -0.66 -0.67 -0.65 -0.66 -0.70 -0.79 -0.93 0

4 0. -0.89 -0.76 -0.73 -0.70 -0.69 -0.68 -0.72 -0.77 -0.99 0

3 0. -0.89 -0.84 -0.73 -0.73 -0.71 -0.71 -0.75 -0.86 -1.07 0

2 0. -0.94 -0.82 -0.73 -0.73 -0.71 -0.72 -0.74 -0.84 -1.06 0

1 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0 *

AX = 0.095 m

AZ = 0.114 m

Z = 1.048 m

nOutflow rate = 0.637 kg/s

Inflow rate = 0.594 kg/s

o Outdoor temperature = 21.5-25.6 C

44
Table B-13

Test 17; 8/6 door, 62.9 kW, location A

TEMPERATURE (^C) *

21

20 106.23

19 109.22

18 109.25

17 22.93 109.66 108.03 107.83 107.05 107.63 107.27 108.69 107.66 108. 18 107.63

16 22.11 109.25 100.91 105.09 106. 12 103. 14 103.21 103. 18 103.39 104.04 107.11

15 21.68 109.08 84.89 106. 12 104.08 101.26 99.33 101.45 101.70 105.21 104.87

14 108.92 56.83 101.59 104.76 98.98 97. 18 98.63 100.26 101.55 96.65

13 107.86 51.86 90.50 92.89 88.21 88.40 91.23 93.21 95.61 80.72

12 101.20 35.74 56.56 61.54 67.82 66.79 68.92 70.28 58.27 56.22

11 74.70 28.77 31.50 37.90 42.58 43.93 41.53 35.35 31.69 31.93

10 50 . 20 27.23 26.22 27.71 31.04 29.30 27.00 24.77 24. 18 28.33

9 42.60 24.39 23.87 24.07 24.52 24.24 24.01 23. 17 23.20 25.23

8 39.66 24.72 23.44 23.47 23.31 23.70 23.70 23.44 22.62 25.31

7 37.84 25.21 23.95 24. 16 24.05 24.23 24.43 23.74 23.35 22.63

6 36.55 25.73 23.80 23.84 23.58 24. 14 24.30 24.07 22.80 22.88

5 35.01 23.84 23.56 23.39 22.96 23. 15 23.41 22.80 22.74 21.87

4 33.98 24.03 23.47 23.33 22.79 23.33 23.41 23. 18 22.16 22.22

3 32.63 24.83 23.91 24.38 24.46 24.79 25.03 24.72 24.73 22.83

2 32.74 24.56 24.65 24.51 24.74 25.00 25.43 25. 14 24.51 24. 14

>K

>k VELOCITY

>K 18 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.

17 0. 2.31 2.33 2. 16 2. 12 2. 19 2. 13 2.09 2.22 2.39

16 0. 1.71 1.74 1.69 1.50 1.48 1,47 1.51 1.70 1.73

15 0. 1.23 1.42 1.35 1.22 1.21 1.21 1.28 1.35 1.41

14 0. 0.82 1.00 0.95 0.99 0.96 0.98 1.03 1.07 1.16

13 0. 0.61 0.72 0.72 0.76 0.77 0.79 0.76 0.79 0.84

12 0. 0.22 0.42 0.45 0.54 0.51 0.52 0.51 0.44 0.50

11 0. -0.20 -0.09 0. 14 0.24 0.24 0.23 0. 14 -0. 10 0. 12

10 0. -0.37 -0.35 -0.29 -0.22 -0.23 -0.29 -0.36 -0.40 -0. 18

9 0. -0.48 -0.45 -0.43 -0.40 -0.43 -0.41 -0.45 -0.48 -0.32

8 0. -0.57 -0.52 -0.50 -0.47 -0.47 -0.50 -0.52 -0.59 -0.38

7 0. -0.63 -0.59 -0.57 -0.55 -0.57 -0.56 -0.60 -0.66 -0.63

6 0. -0.68 -0.62 -0.62 -0.59 -0.58 -0.61 -0.65 -0.73 -0.73

5 0. -0.74 -0.63 -0.62 -0.61 -0.61 -0.61 -0.65 -0.73 -0.87

4 0. -0.78 -0.67 -0.65 -0.64 -0.62 -0.64 -0.68 -0.77 -0.95

3 0. -0.83 -0.71 -0.66 -0.63 -0.63 -0.67 -0.70 -0.80 -1.00

2 0. -0.86 -0.78 -0.70 -0.65 -0.65 -0.68 -0.73 -0.83 -1.03

1 >K

>K

0. 0. 0. 0. 0. 0. 0. 0. 0. 0.

AX = 0.111 m

AZ = 0.114 m

Z = 1.065 m

nOutflow rate = 0.701 kg/s

Inflow rate = 0.653 kg/s

Outdoor temperature = 18.6-18.9 C

A5

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0
Table B-IA

Test 22; full window, 62.9 kW, location A

TEMPERATURE (°C)

21

20 140.14

19 144.16

13 144.12

17 32.36 144.37 142.68 142.72 142.00 140.99 141.63 141.11 142.61

16 31.03 143.69 132.77 139.86 136.93 136.55 137.14 137.91 139.53

15 30.32 142.87 110.32 138.98 135.85 134.20 134.63 135.70 137.24

14 142.34 92.55 137.30 133.26 132.38 132.63 133.03 128.54

13 140.84 88.98 132.96 131.71 129.03 129.85 130.40 115.47

12 138.31 60.23 103.57 108.43 107.57 111.05 107.64 83.06

11 133.48 44.52 39.27 42.86 45.71 42.06 35.15 41.20

10 121.29 38.43 33.51 33.58 33.14 32.38 31.37 33.23

9 103.21 35.98 32.77 32. 14 31.84 31.38 30.93 30.27

8 88.56 34.47 32.30 32. 18 31.75 31.58 30.70 30.22

7 76.88 33. 17 32.81 32.39 31.98 31.31 30.91 29.95

6 65.06 32.43 32.44 32.02 31.31 31.55 30.89 30.15

5 56.40 33.01 32.45 31.81 31.38 31.04 30.70 30.18

4 53.54 32.80 32.24 32.04 31.26 31.62 30.88 30.25

3 52.00 32.83 32.23 31.72 31.35 31.02 30.57 30.05

2

>x 51.74 32.85 32.34 32.41 31.70 31.94 31.25 30.50

>K VELOCITY

18 0. 0. 0. 0. 0. 0. 0. 0. 0.

17 0. 2.22 2.15 2.11 2.07 2.11 2.13 2.26 0.

16 0. 1.79 1.63 1.51 1.48 1.49 1.58 1.84 0.

15 0. 1.44 1.41 1.28 1.23 1.27 1.37 1.62 0.

14 0. 1.15 1.12 1.04 1.02 1.05 1.14 1.29 0.

13 0 . 0.76 0.84 0.78 0.77 0.79 0.84 0.92 0.

12 0. 0.27 0.45 0.47 0.48 0.51 0.49 0.33 0.

11 0. -0.47 -0.47 -0.43 -0.39 -0.40 -0.51 -0.46 0.

10 0. -0.87 -0.73 -0.68 -0.66 -0.66 -0.73 -0.85 0.

9 0 . -1.04 -0.84 -0.77 -0.75 -0.78 -0.87 -1.06 0.

8 0. -1.16 -0.95 -0.88 -0.87 -0.86 -0.96 -1.19 0.

7 0. -1.28 -1.10 -1.05 -1.03 -1.06 -1.14 -1.38 0.

6 0. -1.46 -1.43 -1.43 -1.44 -1.43 -1.46 -1.50 0.

5 0. 0. 0. 0 . 0. 0. 0. 0. 0.

4 0. 0. 0. 0. 0. 0. 0. 0. 0.

3 0. 0. 0 . 0. 0. 0. 0. 0. 0.

2 0. 0. 0. 0 . 0. 0. 0. 0. 0.

1 0. 0. 0. 0. 0 . 0. 0. 0. 0.

>K

AX = 0.106 m

AZ = 0.114 m

Z = 1.145 m

nOutflow rate = 0.465 kg/s

Inflow rate = 0.462 kg/s

Outdoor temperature = 25.7-27.5°C

46
Table B-15

Test 23; 2/3 winddw, 62.9 kW, location A

TEMPERATURE (°C) *

21

20 172.59

19 178.70

18 178.89

17 27.74 179.06 174.93 175.04 173.66 173.85 174.54 172.62 173.53

16 26.66 178.27 165.41 167.75 166.88 168.23 168.54 166.76 171.88

15 26.06 177.20 147.67 167.91 166.64 164.39 166.01 164.54 166. 16

14 177. 16 119.11 154.51 150.39 145.64 147.27 143.72 141.19

13 176.02 45.20 50. 15 45.60 44.56 44.95 39.88 41.85

12 173.82 32.30 23.88 29.57 29.98 29.77 28.33 29.78

11 170.82 29.17 27.75 27.83 28.08 27.83 27.11 26.32

10 165. 18 26.99 27.04 27.31 27.89 27.58 26.52 26. 14

9 151.19 27.40 27.33 27.60 27.76 27.00 26.64 26.28

3 127.64 27.54 27.45 28.01 28. 16 27.65 26.71 26.50

7 105. 18 26.65 26.98 27. 10 27.43 26.73 26.42 25.99

6 87. 16 26.91 27.20 27.71 27.94 27.33 26.42 26.08

5 79.96 27.71 27.35 27.54 27.82 27. 17 26.81 26.20

4 77.47 27. 19 27. 19 27.55 27.78 27.44 26.65 26.20

3 76.39 27.04 27.11 27.08 27.40 26.83 26.59 26. 13

2

>K 76.44 27.13 27.12 27.45 27.81 27.44 26.73 26.33

)K VELOCITY

18 0. 0. 0. 0. 0. 0. 0. 0. 0.

17 0. 2.15 2.09 2.02 2.01 2.06 2.10 2.22 0.

16 0. 1.68 1.49 1.39 1.38 1.40 1.47 1.75 0.

15 0. 1.29 1.16 1.09 1.07 1.12 1.20 1.42 0.

14 0. 0.81 0.76 0.73 0.70 0.76 0.78 0.86 0.

13 0. -0.42 -0.43 -0.40 -0.39 -0.41 -0.48 -0.94 0.

12 0. -0.83 -0.78 -0.73 -0.73 -0.74 -0.76 -0.91 0.

11 0. -1.20 -1.02 -0.96 -0.96 -0.98 -1.00 -1.20 0.

10 0. -1.51 -1.50 -1.46 -1.45 -1.49 -1.48 -1.53 0.

9 0. 0. 0. 0. 0. 0. 0. 0. 0.

8 0. 0. 0. 0. 0. 0. 0. 0. 0.

7 0. 0. 0. 0. 0. 0. 0. 0. 0.

6 0. 0. 0. 0. 0. 0. 0. 0. 0.

5 0. 0. 0. 0. 0. 0. 0. 0. 0.

4 0. 0. 0. 0. 0. 0. 0. 0. 0.

3 0. 0. 0. 0. 0. 0. 0. 0. 0.

2 0. 0. 0. 0. 0. 0. 0. 0. 0.

1 H<

>1<

0. 0. 0. 0. 0. 0. 0. 0. 0.

AX = 0.106 m

AZ = 0.114 m

Z = 1.358 m

nOutflow rate = 0.306 kg/s

Inflow rate = 0.299 kg/s

Outdoor temperature = 22.1-23.9*^0

47
Table B-16

Test 30; 2/3 window, 62.9 kW, location A

TEMPERATURE (°C) *

21

20 in. 90

19 1 ?8.77

18 1

?’ 9.02

17 26.90 179.56 175.54 171.58 172.40 171.83 172.93 172.11 174.25

16 26.88 179.00 170. 19 168.08 168.70 167.96 168.38 168.51 169.58

15 26.24 177.99 161.29 165.99 165.57 164.82 166.03 166.27 164. 10

14 177.99 127. 12 143.89 147.29 143.07 140.80 144.14 124.28

13 176.73 35.87 42.68 45.00 43.61 37.78 36.60 40.97

12 174.35 29.66 29.79 29.61 29.54 28.71 29.34 28.49

11 170.73 28.88 29.07 29.00 28.39 27.77 27.02 26.74

10 163.24 28.53 28.20 27.77 27.32 26.58 26.55 25.99

9 143.73 28.62 28.35 28. 16 27.36 27.05 26.31 26.11

8 128.74 28.63 28.37 27.79 27.37 26.49 26.49 25.53

7 103.21 28.03 27 . 99 27.79 26.79 26.48 25.74 25.67

6 89 . 30 28.04 28 . 38 28.78 27.32 26.38 26. 19 25.18

5 81.13 28.22 27.86 27.61 26.87 26.79 26. 12 25.83

4 78.80 27.81 27.89 27.11 26.91 26.26 26.21 25. 18

3 77.75 27.67 27.31 27.08 26.30 26.33 25.75 25.53

2

>k 78.33 27.76 27.68 26.93 26.77 26.22 26.11 25. 14

>k

>K 13

VELOCITY

0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 17 0 . 2.22 2 . 10 2. 10 2.11 2.16 2.11 2.31 0 . 16 0 . 1.74 1.52 1.44 1.43 1.47 1.54 1.78 0 . 15 0 . 1.27 1.08 1.04 1.04 1.09 1.13 1.23 0 . 14 0 . 0.80 0.69 0.68 0.70 0.72 0.76 1.13 0 . 13 0 . -0.45 -0.36 -0.38 -0.42 -0.51 -0.52 -0.54 0 . 12 0 . -0.84 -0.76 -0.75 -0.75 -0.77 -0.81 -0.98 0 .

1

1

0 . - 1.12 -0.96 - 0.95 -0.96 -0.98 - 1.01 - 1.27 0 . 10 0 . - 1.52 - 1.50 - 1.41 - 1.51 - 1.48 - 1.58 - 1.54 0 . 9 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 8 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 7 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 6 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 5 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 4 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 3 0. 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 2 0. 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 .

1 0. 0 . 0. 0 . 0 . 0 . 0 . 0 . 0 .

x<

AX = 0.106 m

AZ = 0.114 m

Z = 1.357 m

nOutflow rate = 0.309 kg/s

Inflow rate = 0.298 kg/s

Outdoor temperature - 23.0°C
Table B-17

Test 41; 1/3 Window, 62.9 kW, location A

TEMPERATURE (°C)

21

20

19

18

17 16.35

261.06

274.01

273.92

273.76 264.01 260.49 259.49 260.15 263.54 256.85 256.06

16 16.46 272.21 260.95 256.77 255.46 256.53 258.39 252.33 252.99

15 16.35 263.75 252.64 249.77 246 . 48 245.24 252.02 246.21 249.36

14 270.07 231.79 194.71 182.65 193.13 193.43 188.89 203.22

13 269.20 131.64 71.03 57.81 47.79 49.95 58.45 118.00

12 266.35 36.35 23.29 21.91 21.38 22.07 19.99 24. 13

11 265.13 24.41 24.20 25.32 25.51 25.80 24.08 22. 19

10 262.98 21.43 22.17 21.80 21.75 21.39 20.58 19.53

9 252.93 15.79 15.77 16.21 16.10 15.50 14.97 14.35

8 215.07 16.06 15.94 15.83 15.69 15.53 14.63 14.90

7 171.64 16.34 16.39 17.33 17.33 17.02 17.32 16.70

6 163.76 16.59 16.64 17.62 17.98 17.70 18.23 18.75

5 159.62 15.37 15.52 15.94 15.83 15.02 14.30 13.47

4 153.96 15.68 15.67 15.67 15.41 15.18 14.02 13.58

3 149.33 15.92 16.26 16.56 16.30 15.51 14.92 14.05

2 144.53 16.83 17.15 16.87 16. 10 15.86 14.79 14.31

>K

>k

18

VELOCITY (m/s)

0. 0. 0. 0. 0. 0. 0. 0. 0

17 0. 2.04 1.94 1.92 1.94 1.95 1.96 2.09 0

16 0. 1.55 1.44 1.42 1.43 1.44 1.43 1.54 0

15 0. 1.25 1.15 1.14 1.15 1.17 1.15 1.25 0

14 0. 0.90 0.69 0.66 0.72 0.75 0.72 0.81 0

13 0. 0.35 “0.24 “0.21 “0.21 “0.23 “0.23 0.24 0

12 0. “0.62 “0.65 -i0.65 “0.64 “0.63 “0.65 “0.66 0

11 0. “0.86 “0.80 “0.78 “0.78 “0.78 “0.79 “0.84 0

10 0. “1.11 “1.04 “1.05 “1.08 ”1.09 -1.08 “1.12 0

9 0. 0. 0. 0. 0. 0. 0. 0. 0

8 0. 0. 0. 0. 0. 0. 0. 0. 0

7 0. 0. 0. 0. 0. 0. 0. 0. 0

6 0. 0. 0. 0. 0. 0. 0. 0. 0

5 0. 0. 0. 0. 0. 0. 0. 0. 0

4 0. 0. 0. 0. 0. 0. 0. 0. 0

3 0. 0. 0. 0. 0. 0. 0. 0. 0

2 0. 0. 0. 0. 0. 0. 0. 0. 0

1 0. 0. 0. 0. 0. 0. 0. 0. 0

>f<

AX = 0.106 m

AZ = 0.051 m

Z = 1.579 m

n Outflow rate = 0.126 kg/s

Inflow rate = 0.108 kg/s

Outdoor temperature = 13.0 - 15.0°c

49
Table B-18

Test 19; 6/6 door, 31.6 kW, location A

TEMPERATURE (O^) *

21

20

19

18

1 ? 30.26

83.48

86 . 12

86. 10

86.51 88.21 87.03

16 29.74 86.18 87.28 85.85

15 29.31 85.93 83.87 84.94

14 85.98 80.54 84.45

13 85.75 67.29 82.92

12 85.15 69.72 75.48

11 82.92 43.60 51.36

10 68.57 36. 17 34.92

9 49.71 32.68 31.91

8 44.26 32.64 31.31

7 41.64 33.01 31.92

6 40 . 13 33.17 31.50

5 39 . 04 32.22 31.50

4 38.57 32.21 30.98

3 38.00 33.27 31.89

2 37.70 33.26 31.73

>k

>k

>k 18

VELOCITY (m/s)

0 . 0 . 0 . 17 0 . 1.78 1.66

16 0 . 1.45 1.27

15 0 . 1.21 1.09

14 0 . 1.05 0.95

13 0 . 0.72 0.70

12 0 . 0.62 0.55

11 0 . 0.19 0.25

10 0 . -0.30 -0.24

9 0 . -0.47 -0.38

8 0 . -0.55 -0.45

7 0 . -0.60 - 0.53

6 0 . -0.65 -0.58

5 0 . -0.69 - 0.60

4 0 . -0.75 -0.64

3 0 . - 0.80 - 0.68

2 0 . -0.83 -0.72

1 0 . 0 . 0 . >«

88.13 86.01 85.61 86.37 84.21

86.03 83.66 83.63 83.57 83.90

84.01 82.38 82.27 84.08 82.21

84.38 81.03 82.58 82.91 80.55

81.42 77.88 80.65 81.67 62.92

73.74 72.77 71.24 72.16 59.57

55.95 50.76 45.69 39.77 36.09

36. 19 35.27 31.94 30.21 31.92

31.85 31.23 29.79 29.35 29.43

31.23 30.76 29.89 29. 19 29.36

31.77 31.45 30.13 29.47 29.04

31.52 31.06 30.13 29. 19 29.02

30.91 30.50 29.45 29.08 28.86

30.98 30. 14 29.56 28.91 29.09

31.99 31.35 30.45 30. 14 29.31

31.88 31.50 30.86 29.97 29.79

0 . 0 . 0 . 0 . 0 . 0 . 1.65 1.65 1.68 1.71 1.80 0 . 1.24 1.19 1.24 1.28 1.45 0 . 1.03 1.04 1.11 1.15 1.23 0 . 0.87 0.85 0.94 0.98 1.00 0 . 0.69 0.62 0.59 0.66 0.53 0 . 0.50 0.51 0.45 0.47 0.44 0 . 0.27 0.26 0.18 0. 10 0.06 0 . -0.23 -0.23 -0.28 -0.32 -0.25 0 . -0.35 -0.37 -0.39 -0.44 -0.46 0 . -0.43 -0.42 -0.46 -0.51 -0.51 0 . -0.50 -0.50 -0.53 -0.61 -0.62 0 . -0.53 -0.55 -0.57 -0.65 -0.69 0 . -0.57 -0.56 -0.60 -0.68 -0.72 0 . -0.57 -0.60 -0.62 -0.71 -0.76 0 . -0.62 -0.63 -0.67 -0.75 - 0.72 0 . - 0.64 -0.65 -0.68 -0.77 -0.53 0 . 0 . 0 . 0 . 0 . 0 . 0 .

AX = 0.106 m

AZ = 0.114 m

Z = 1.040 m

nOutflow rate = 0.461 kg/s

Inflow rate = 0.430 kg/s

Outdoor temperature = 27.8-30.2°C

50
Table B-19

Test 20; 6/6 door, 105.3 kW, location A

TEMPERATURE (°C)

21

20

19

18

17 37.22

177.83

183.96

183.96

184.21 181.53 180.18 181.84 181.47 183.58 183.04 177.56

16 35.38 183.48 176.26 177.07 172.32 176.06 174.77 178.80 178.85

15 34.35 182.79 161.69 175.41 175. 17 171.46 172.70 176. 14 171.85

14 182.89 135.86 176.68 169.53 170.96 169.97 176.71 165.87

13 182.21 115.05 172.14 171.85 164.62 166.94 172.81 130.09

12 180.28 99.14 154.99 149.66 155.00 155.17 158.17 128.03

11 172.11 73.59 87.13 104.52 108.62 115.35 103.40 83.08

10 130.31 50.06 51.00 56.67 64.04 60.48 46.77 54.25

9 93.55 41.09 38.28 39.09 39.80 37.69 36. 16 38.71

8 79.27 38.77 37.31 37. 13 37.81 36.62 35.35 41.09

7 72.15 41.47 37.73 38.27 38.68 38.36 36.48 36.21

6 67.72 39.85 37.62 37.77 38.63 37.89 36.05 36.40

5 63.81 38.11 36.46 37.93 37.06 36.38 35.39 35.91

4 61.44 37.95 37.13 36.41 37.17 36.68 35.18 35.56

3 58.89 45. 19 38. 17 38.71 39.98 40.25 39.64 37.28

2 57.54 43.91 38.43 '39.15 39.92 40.41 39.57 38.30

>K VELOCITY (m/s)

18 0. 0. 0. 0. 0. 0. 0. 0.

17 0. 2.91 2.77 2.72 2.67 2.64 2.71 2.95

16 0. 2.36 2.11 1.98 1.96 1.98 2.10 2.39

15 0. 1.93 1.88 1.78 1.69 1.70 1.81 2.00

14 0. 1.47 1.59 1.46 1.42 1.46 1.60 1.59

13 0. 1.07 1.15 1.11 1.12 1.13 1.18 1.05

12 0. 0.83 0.92 0.89 0.94 0.93 0.91 0.94

11 0. 0.43 0.50 0.60 0.57 0.58 0.56 0.47

10 0. -0.38 -0.31 -0.23 -0.11 -0.20 -0.35 0.08

9 0. -0.65 -0.56 -0.57 -0.52 -0.54 -0.62 -0.59

8 0. -0.82 -0.71 -0.65 -0.64 -0.67 -0.76 -0.50

7 0. -0.89 -0.81 -0.78 -0.75 -0.78 -0.89 -0.91

6 0. -1.00 -0.89 -0.83 -0.83 -0.85 -0.97 -0.90

5 0. -1.06 -0.95 -0.89 -0.84 -0.89 -1.00 -1.14

4 0. -1.14 -1.01 -0.93 -0.90 -0.93 -1.05 -1.26

3 0. -1.14 -1.07 -0.95 -0.92 -0.97 -1.08 -1.32

2 0. -1.24 -1.08 -0.97 -0.93 -0.96 -1.12 -1.41

1 0. 0. 0. 0. 0. 0. 0. 0.

>K

>k

AX = 0.106 m

AZ = 0.114 m

Z = 1.001 m

nOutflow rate s 0.630 kg/s

Inflow rate = 0.618 kg/s

Outdoor temperature = 27.2-32.2°C

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

51
Table B-20

Test 21; 6/6 door, 158 kW, location A

TEnPERftTURE (°C) *

21

20 235.73

19 244.89

13 245.00

17 39.04 244.83 250.84 243.97 238.46 240.36 235.17 237.17 241.92

16 36.44 243 . 96 240.58 230.59 227.08 227. 13 227.22 231.02 236.99

15 35 . 14 242.58 217.55 237.27 224.83 224.03 219.94 225.04 234.95

14 243.09 177.87 231.70 222.62 219.51 221.55 229.64 218.65

13 242 . 4? 150.35 231.52 219.68 214.11 211.64 220.08 206.17

12 240.25 134.89 201.05 198.71 196. 15 197.48 205.00 181.20

11 232.32 99.39 126.06 139.07 137.86 139.14 138.42 129.66

10 171.86 67.22 61.01 73.47 83.29 83.58 66. 18 73.29

9 117.47 45.02 43.06 44.70 44.35 38.99 39.63 40.70

8 99.58 45.46 40.43 40.76 40.84 38.93 36.56 43.85

7 90.55 45.72 42.09 42.30 41.77 39.98 38.90 37.43

6 85.08 47.05 40.85 41.51 41.42 40.86 37.91 36.20

5 79.31 41.16 41.08 39.11 38.59 36.76 36.71 36.34

4 75.20 43. 19 39.61 39.04 38.25 37.74 35.97 35.31

3 70.64 49.27 41.29 , 41.38 42.51 41.58 42.28 39.52

2 68.83 54.92 41.62 42.14 41.94 43.08 42.54 40.28

>K 18

VELOCITY ( m/ s )

0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 17 0 . 3.56 3.34 3.20 3. 17 3. 18 3.24 3.51

16 0 . 2.86 2.55 2.41 2.33 2.39 2.53 2.85

15 0 . 2.37 2.27 2. 10 2.00 2.07 2.19 2.42

14 0 . 1.83 1.91 1.72 1.70 1.77 1.93 1.88

13 0 . 1.30 1.49 1.37 1.37 1.33 1.49 1.73

12 0 . 1.08 1.14 1.13 1.13 1.13 1.17 1.37

11 0 . 0.59 0.73 0.72 0.68 0.71 0.78 0.80

10 0 . -0.24 -0.26 -0. 17 0.04 0. 16 -0.20 0.24

9 0 . -0.75 -0.63 -0.56 -0.53 -0.57 -0.63 -0.67

3 0 . -0.90 -0.78 -0.69 -0.67 -0.70 -0.81 -0.56

7 0 . - 1.05 -0.91 -0.82 -0.80 -0.87 -0.96 - 1.03

6 0. - 1.15 -0.99 -0.92 -0.90 -0.95 - 1.06 - 1.08

5 0. - 1.25 - 1.08 -0.97 -0.95 - 1.00 - 1.10 - 1.32

4 0. - 1.31 - 1.13 - 1.03 - 1.02 - 1.05 - 1.17 - 1.48

3 0. - 1.43 - 1.22 - 1.10 - 1.06 - 1.09 - 1.21 - 1.59

2 0. - 1.47 - 1.25 - 1.12 - 1.11 - 1.14 - 1.27 - 1.66

1 0. 0 . 0. 0. 0 . 0 . 0 . 0 .

>i<

>K

AX = 0.106 in AZ = 0.114 m

Z = 0.978 m

nOutflow rate = 0.606 kg/s

Inflow rate = 0.679 kg/s

Outdoor temperature z 27.7-29.8°C

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

52
Table B-21

Test 114: ,2/6 door, i62.9 kW, location B

TEMPERftTURE *

21

20 234.03

19 250.70

18 250.80

17 33.93 250.27 227.42 242.43 240.96

16 248.93 222.28 235.36 237.01

15 246.27 224.75 241.87 232. 10

14 31,91 246.20 226.08 235.05 229.84

13 241.58 209.48 199.72 203.60

12 200.48 141.59 139.43 147.79

11 127.29 98.82 111.83 107.00

10 31.39 107. 13 58.57 74. 10 80.95

9 97.57 35. 17 35.58 38.35

8 90.70 34.36 33.81 35.39

7 84.59 35.45 35.95 35.64

6 31.30 77.70 35.38 35.31 36.01

5 72.81 36.99 36.40 35.18

4 71.05 35.92 36.03 35.79

3 68.76 36.25 36.69 39. 15

2 31.39 67 . 67 • 36.45 36.21 41.50 *

>k VELOCITY (m/s)

>K 18 0. 0. 0. 0. 0

17 0. 3.03 3.02 3. 10 0

16 0. 2.80 2.65 2.72 0

15 0. 2.48 2.40 2.42 0

14 0. 2.44 2.09 2.12 0

13 0. 1.88 1.61 1.63 0

12 0. 1.38 1.11 1.17 0

11 0. 0.72 0.67 0.61 0

10 0. -0.11 0.21 0.24 0

9 0. -0.54 -0.59 -0.58 0

8 0. -0.78 -0.79 -0.83 0

7 0. -0.98 •••1.01 -1.01 0

6 0. -1.14 -1.14 -1.10 0

5 0. -1.25 -1.25 -1.21 0

4 0. -1.37 -1.34 -1.25 0

3 0. -1.45 -1.44 -1.15 0

2 0. -1.51 -1.49 -0.90 0

1 0. 0. 0. 0. 0

»<

AX = 0.067 m

AZ = 0.114 m

z ~ 0.956 m

nOutflow rate = 0.205 kg/s

Inflow rate = 0.201 kg/s

53
Table B-22

Test 144; 3/6 door, 62.9 kVI, location B

TEMPERATURE (°c) *

21

20 204.80

19 217.57

18 217.73

17 31.54 217.43 190.92 216.05 211.42 212.98 210.57

16 216 . 16 180. 15 210.23 205.46 203.08 214.95

15 214.05 184.81 214.58 204.59 197.66 202.67

14 30. 19 212.61 157.11 208 . 40 195.78 185.94 203.86

13 199.57 124.54 128.88 125.61 133.39 136 . 19

12 110.55 88.81 92.81 88.66 90.67 86.45

11 84.11 51.90 65.38 71.90 72.66 65.76

10 29.83 75.23 43.43 42.78 46.74 44.21 43.62

9 69.77 33.56 33.00 32.75 32.70 35.83

8 65.20 33 . 15 32.46 32.18 31.82 32.44

7 60.78 33.91 33.85 33.48 32.90 34.82

6 29.73 57.54 33.82 33.56 33.46 32.84 32.81

5 55.26 35.13 34.84 34.09 32.67 34.08

4 54.55 35 . 13 34.55 33.66 32.70 33.88

3 53.35 34.48 34.74 34.22 33.31 37.31

2 * 29.75 52. 13 34.74 34.48 34.07 33.75 34.74

*

*

18

VELOCITY (m/s)

0 . 0 . 0 . 0 . 0 . 0 . 0

17 0 . 2.72 2.70 2.74 2.77 2.85 0

16 0 . 2.36 2.36 2.26 2.21 2.34 0

15 0 . 2.06 1.97 1.88 1.85 1 . 99 0

14 0 . 1.83 1.68 1.52 1.54 1.72 0

13 0 . 1.35 1.16 1.06 1.05 1.18 0

12 0 . 0.93 0.80 0.58 0.58 0.73 0

11 0 . 0.33 0.44 0.40 0.33 0.27 0

10 0 . -0.22 -0.28 -0.19 -0.26 -0.22 0

9 0 . -0.48 -0.49 -0.53 -0.56 -0.51 0

8 0 . -0.65 - 0.67 -0.64 -0.72 -0.68 0

7 0 . -0.83 - 0.79 -0.81 -0.88 -0.76 0

6 0 . -0.95 - 0.93 -0.89 -0.97 -0.94 0

5 0 . - 1.06 - 1.00 -0.99 - 1.03 -0.89 0

4 0 . - 1.15 - 1.10 - 1.05 - 1.11 -0.98 0

3 0 . - 1.22 - 1.12 - 1.13 - 1.19 -0.57 0

2 0 . - 1.24 - 1.17 - 1.14 - 1.22 -0.86 0

1 *

*

0 . 0 . 0 . 0 . 0 . 0 . 0

AX = 0. 065 m

AZ = 0. 114 m

Z = 1. 017 m

nOutflovv' rate == 0.,283 kg/s

Inflow rate == 0.,289 kg/s

54
Table B-23

Test 212; 4/6 door, 62.9 kW, location B

TEMPERfiTURE (°c)

21

20 185.90

19 195.44

18 195.60

17 25.91 195.63 165.66 194.28 191.53 190.39 190.36

16 194.66 157.66 191.85 185.44 186.11 187.20

15 192.25 129.62 188.85 175.41 168.99 183.02

14 24.44 188.26 130.14 152.88 144.23 145. 16 157.37

13 130.28 76.61 79.23 75.63 79.22 79.46

12 73.14 53.13 64.69 64. 16 63.97 55.07

11 62.65 40.81 49.91 51.78 44.07 42 . 56

10 24. 12 56.62 30.82 32.20 30.23 29.69 29.98

9 52.31 27.56 27.46 26.79 26.08 26 . 60

8 48.88 27.55 26.54 26.34 26.58 26.56

7 46.48 28.24 28.42 27.98 27.40 28.07

6 24. 10 45. 13 28.80 28. 13 27.54 28.04 27.97

5 43.95 30.43 29.29 27.78 26. 12 25.72

4 43.48 30.89 28. 16 27.44 27.08 25.82

3 42.39 29.31 29.72 28.57 27.42 26.87

2

>l< 24.37 41.89 29.25 29.23 28.94 28.43 27.03

>K

Jk 18

VELOCITY (m/s)

0. 0. 0. 0. 0. 0.

17 0. 2.51 2.48 2.54 2.58 2.65

16 0. 2. 14 2. 10 1.98 1.92 2.05

15 0. 1.75 1.68 1.53 1.54 1.80

14 0. 1.65 1.29 1.20 1.17 1.37

13 0. 0.99 0.78 0.69 0.71 0.83

12 0. 0.61 0.57 0.47 0.46 0.45

11 0. 0. 13 0.30 0.28 0. 17 0. 17

10 0. -0.27 -0.23 -0.29 -0.31 -0.29

9 0. -0.42 -0.40 -0.42 -0.45 -0.47

8 0. -0.56 -0.53 -0.53 -0.56 -0.58

7 0. -0.73 -0.64 -0.64 -0.70 -0.76

6 0. -0.84 -0.75 -0.73 -0.77 -0.83

5 0. -0.88 -0.77 -0.76 -0.83 -0.91

4 0. -0.97 -0.86 -0.84 -0.88 -0.94

3 0. -1.00 -0.86 -0.84 -0.92 -1.05

2 0. -1.07 -0.92 -0.89 -0.95 -1.05

1 >k

>k

0. 0. 0. 0. 0. 0.

AX = 0. 098 m

AZ = 0. 114 m

z = 1. 038 m

nOutflovi’ rate = 0.,351 kg/

Inflow rate = 0.,357 kg/s

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

55
Table B-2A

Test 242; 5/6 door, 62.9 kW, location B

TEMPERATURE (°c) *

21

20 187.91

19 198. 16

18 198.22

1? 30.90 198.26 167.49 194.45 190.49 190.74 192.94 192.61 193.99

16 196.77 157.68 192.44 184.00 181.72 178.94 185. 14 192.64

15 192.81 104.65 189.72 175.66 165.68 154.77 172.03 174.46

14 29.42 174.35 83.22 137.46 114.78 109.15 106.04 121.07 130.55

13 89.76 66.03 73.56 72. 19 70.45 69.33 68.60 62.51

12 67.76 55.89 59.95 64.91 66.60 62.39 60.43 54.50

11 60.19 42. 12 44.77 51.95 53.45 50.37 43.27 46.48

10 28.87 56.75 38.11 37.59 39.90 39.60 34.88 32.88 33.29

9 54.56 35.00 34. 13 33.90 32.74 31.75 30.56 31.04

8 52.64 35.44 33.76 32.89 32.60 31.52 30.95 29.71

7 50.64 35. 19 34. 14 33.76 32.77 32.37 31.37 30.35

6 28.81 48.98 35.98 34.44 33.70 33.47 32.54 31.79 29.77

5 47. 18 35.17 34.54 33.64 32.22 31.33 30.24 30.41

4 46.23 36.83 34.65 32.96 32.42 31.11 30.52 23.99

3 44.71 36.05 36.44 35.76 34.36 33.41 31.68 30.50

2 *29. 12 44. 13 36.43 36.47 35.50 34.76 33.41 32.33 30.75

* VELOCITY (m/s)

18 0. 0. 0. 0. 0 . 0. 0. 0. 0

17 0. 2.31 2.32 2.32 2.35 2.38 2.43 2.49 0

16 0. 1.88 1.90 1.80 1.74 1.73 1.82 1.93 0

15 0. 1.32 1.45 1.34 1.33 1.32 1.42 1.56 0

14 0. 1.12 1.08 0.97 0.92 0.93 1.04 1.30 0

13 0. 0.57 0.48 0.42 0.42 0.43 0.47 0.52 0

12 0 . 0.31 0.34 0.35 0.33 0.33 0.32 0.33 0

1

1

0. -0.09 0. 14 0.31 0.29 0.26 0. 17 0.23 0

10 0. -0.25 -0.22 -0.10 -0.10 -0.19 -0.25 -0.18 0

9 0. -0.37 -0.35 -0.34 -0.33 -0.36 -0.39 -0.40 0

8 0 . -0.50 -0.43 -0.42 -0.42 -0.44 -0.50 -0.54 0

7 0. -0.65 -0.57 -0.52 -0.53 -0.56 -0.63 -0.72 0

6 0 . -0.71 -0.62 -0.58 -0.58 -0.62 -0.71 -0.80 0

5 0. -0.79 -0.67 -0.62 -0.62 -0.66 -0.75 -0.90 0

4 0. -0.83 -0.72 -0.67 -0.67 -0.71 -0.80 -0.97 0

3 0. -0.89 -0.77 -0.72 -0.73 -0.77 -0.87 -1.03 0

2 0. -0.96 -0.81 -0.76 -0.75 -0.80 -0.91 -0.98 0

1 0. 0. 0. 0. 0. 0. 0. 0. 0

>K

AX = 0.,086 m

AZ = 0..114 m

Z = 1,,034 m

nOutflow rate = 0.378 kg/s

Inflow rate = 0.383 kg/s

56
Table B-25

Test 410; 6/6 door, 62.9 kW, location B

1 TEMPERATURE C

"^ C ) #

21

20 173.18

19 181.54

18 181.74

17 22.82 181.12 175.62 181.39 174.91 176.06 178.11 177.07 178.71

16 179.74 157.13 179.55 169.80 165.94 164.26 169.59 172.29

15 175.33 74.62 170.15 149.35 145.90 133.75 144.98 151.47

14 21 . 16 139.35 54.31 87.92 74.98 73.39 69.86 89.81 71.49

13 64.68 48.41 56.23 56.33 56.39 53.20 49.57 43.54

12 51.07 37.95 42.94 49.82 52.39 48.57 45.39 40.70

11 44.95 31.93 32.53 37.62 42.33 37.66 33.69 34.73

10 20.92 41.59 28.09 28.80 30.24 29.60 26.58 24.67 27.28

9 39.60 24.96 24.75 25.02 23.67 22.97 22.95 24.37

8 38.02 24.92 24.10 23.25 23.26 22.23 22.85 23.91

7 36.68 24.97 23.85 24.02 23.85 23.38 22.44 20.95

B 20.62 35.55 25.54 24.57 24.06 24.03 23. 15 21 .85 20.80

5 34.06 26.44 23.61 23.33 22.93 22.41 21.18 20.54

4 33.25 27.64 24.52 23.82 23.21 22.21 21.54 20.10

3 32.33 28.27 25.33 25.70 25.72 25.37 24.47 24.30

2 * 21.27 33.09 26.41 26.17 26.23 26.19 25.86 25.69 23.92

« VELOCITY ( m/ s )

18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 17 0.00 2.31 2.17 2.23 . 2.23 2.31 2.35 2.40 0 . 16 0.00 1 .80 1.73 1.64 1.56 1.55 1.63 1.77 0 . 15 0.00 1.21 1 .26 1 .21 1.22 1.18 1.24 1.43 0 . 14 0.00 0.93 0.90 0.80 0.76 0.75 0.86 0.94 0 . 13 0.00 0.73 0.62 0.57 0.52 0.53 0.51 0.57 0 . 12 0.00 0.34 0.40 0.42 0.41 0.40 0.37 0.36 0 . 11 0.00 - 0.09 0.06 0.28 0.24 0.22 0.18 0.20 0 . 10 0.00 -0.24 - 0.22 -0. 13 -0.14 -0.16 -0.27 -0.04 0 . 9 0.00 - 0.36 -0.33 -0.31 -0.35 -0.37 -0.40 -0.35 0 . 8 0.00 - 0.47 -0.42 -0.40 -0.44 -0.45 -0.52 -0.40 0 . 7 0.00 - 0.59 -0.52 -0.50 -0.54 - 0.55 -0.59 -0.30 0 . 6 0.00 - 0.68 - 0.58 -0.55 -0.58 -0.59 -0.70 -0.60 0 . 5 0.00 - 0.73 -0.62 -0.59 -0.61 -0.60 -0.66 -0.79 0 . 4 0.00 - 0.76 - 0.65 -0.60 -0.61 -0.61 - 0.73 -0.86 0 . 3 0.00 -0.78 -0.65 -0.62 -0.61 -0.65 - 0.72 -0.94 0 . 2 0.00 -0.81 - 0.63 - 0.59 -0.61 -0.65 -0.77 -0.98 0 . 1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . ««

AA = 0 . 106 m

AZ = 0.114 m

Zn = 1.035 m

Outflow rate = 0.454 kg/s

Inflow rate = 0.431 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

,00

57
Table B-26

Test 210; 6/6 door, 62.9 kW, location B

TEMPERATURE (°c) *

21

20 178.40

19 187.20

18 187.47

17 32.69 187.59 155.46 186.49 181.48 182.47 187.16 188.08 187.28

1

6

186.22 112.84 184.38 176.10 171.02 171.90 176.92 184.26

15 102.47 81.40 181.34 162.80 157.94 146.46 159.98 166.77

14 30.50 156.45 67.61 120.23 98.51 94.49 92.04 107.89 115.53

13 81.12 60.29 68 . 15 67.89 69.90 67.39 66.75 63.74

12 65.47 50.98 58 . 17 61.28 62 . 13 62.38 61.16 57.83

11 59.56 40.60 45.62 49.63 51.21 48.70 46.58 48.06

10 29.92 55.60 36.69 38.92 38 . 19 35.21 36.61 34.63 37.07

9 52.75 33.56 33.82 32.87 34.03 33.68 34.87 35.29

8 50.78 33.73 32.74 31.93 32.33 33.84 33.85 33.97

7 49.26 33.86 33.41 32.89 34.61 34.94 35.54 34.68

6 29.97 48.23 34.58 33.46 32.82 33.36 35 . 14 34.83 34.08

5 46.89 36.12 33.42 32.67 33.88 33.90 34.36 34.42

4 46 . 13 40.28 33.29 32.71 32.66 33.83 33.69 33.70

3 45 . 13 35.23 35.45 35.06 35.89 35.72 35.56 34.58

2

>K 30.45 45.60 34.75 35.70 35.70 35.76 36.52 35.36 35.11

>K

>K VELOCITY (m/ s )

18 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 17 0 . 2.11 2.09 2 . 15 2.21 2.28 2.33 2.36

16 0 . 1.65 1.73 1.66 1.59 1.59 1.67 1.81

15 0 . 1.22 1.24 1.17 1.20 1.18 1.26 1.45

14 0 . 1.05 0.95 0.84 0.80 0.82 0.89 1.12

13 0 . 0.69 0.54 0.50 0.48 0.46 0.48 0.54

12 0 . 0.38 0.41 0.40 0.39 0.35 0.33 0.34

1

1

0 . -0.08 0.26 0.28 0.22 0.21 0 . 16 0 . 13

10 0 . -0.25 -0.14 -0 . 15 -0.22 -0.23 -0.31 -0.23

9 0 . -0.36 -0.31 -0.32 -0.34 -0.36 -0.39 -0.40

8 0 . -0.48 -0.43 -0.41 -0.45 -0.43 - 0.49 -0.54

7 0 . -0.62 -0.52 -0.52 -0.52 -0.54 -0.61 -0.70

6 0 . -0.70 -0.60 -0.57 -0.59 -0.60 -0.68 -0.81

5 0 . -0.73 - 0.62 -0.60 -0.60 -0.62 - 0.72 -0.87

4 0 . - 0.66 - 0.68 -0.63 -0.63 - 0.65 - 0.76 -0.92

3 0 . -0.82 -0.70 -0.64 -0.64 -0.68 -0.82 -0.97

2 0 . -0.91 -0.73 -0.65 -0.66 -0.72 -0.86 -0.93

1 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . *

AX = 0. 106 m

AZ - 0.114 m

Z = 1.040 m

nOutflow rate = 0.439 kg/s

Inflow rate = 0.440 kg/s

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0
Table B-27

Test 310i 6/6 door, 62.9 kW, location B

1 TEMPERATURE (“o )

21

20 170.24

19 177.74

IS 177.90

17 21.46 177.28 164.75 174.68 171 . 13 176.42 170.58 174.06 173.44

16 175.73 135.21 172.96 165.21 163.36 158.05 163.64 168.90

15 170.89 67.97 164.31 142.93 142.17 125.32 142.95 144.07

14 20.24 126.07 47.50 78.72 69.89 68 . 04 65.51 72.41 65.44

13 60.06 39.86 48.74 52.25 53.16 50.01 47.62 43.11

12 48.42 31.77 37.08 45.27 49. 19 44.70 41.89 38.65

11 42.82 27.76 30.80 34.79 37.61 35.83 30.49 31.64

10 20.00 39.50 25.08 24.82 28.36 27.68 25.98 24.16 25.44

9 37.53 21.06 22.00 22.81 22.93 22.35 23.10 24.84

9 36.09 21.40 21.05 21.95 21.97 21.99 22.21 23.82

7 34.86 21.46 21.42 21.71 22. 16 22.10 22.86 22.59

6 19.70 33.95 22.25 21.11 22.22 22.47 22.51 22.37 22.22

5 32.65 22.34 20.88 20.92 21.50 21.33 22.09 23.05

4 31.87 23.21 21 .09 21.78 21.64 21.64 21.62 22.03

3 30.82 23.69 22.83 23.14 23.87 23.69 24.69 24.58

2 20.14 31 .09 23.31 23 . 42. 24.84 24.97 25.07 24.84 24.66

L VELOCITY

r 18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 17 0.00 2.33 2.25 2.30 2.34 2.34 2.39 2.42 0 . 16 0.00 1.76 1.76 1.69 1.62 1.60 1.69 1.78 0 . 15 0.00 1 . 17 1.31 1 .24 1.22 1.17 1.24 1.39 0 . 14 0.00 0.98 0.90 0.82 0.77 0.77 0.83 0.92 0 . 13 0.00 0.72 0.63 0.58 0.53 0.52 0.50 0.50 0 . 12 0.00 0.31 0.41 0.44 0.42 0.37 0.32 0.30 0 . 11 0.00 -0.16 0.20 0.28 0.22 0.23 0.08 0.09 0 . 10 0.00 -0.26 -0.18 -0.13 -0.15 -0.23 -0.28 - 0.20 0 . 9 0.00 -0.36 -0.33 -0.31 -0.31 -0.35 -0.38 - 0.35 0 . B 0.00 -0.43 - 0.40 -0.41 -0.40 -0.43 -0.47 - 0.46 0 . 7 0.00 -0.56 -0.51 -0.49 -0.50 -0.53 -0.57 -0.58 0 . 6 0.00 - 0.64 - 0.55 - 0.56 -0.55 - 0.58 -0.64 -0.66 0 . 5 0.00 - 0.69 -0.63 -0.60 -0.59 -0.61 -0.67 -0.71 0 . 4 0.00 - 0.75 -0.64 -0.61 -0.61 -0.64 -0.72 -0.81 0 . 3 0.00 -0.82 - 0.71 -0.65 - 0.63 - 0.68 -0.74 -0.89 0 . 2 0.00 -0.85 - 0.73 -0.64 - 0.64 -0.69 -0.77 -0.89 0 . 1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 .

= 0.106 in AZ = 0.114 m

Zn = 1.045 m

Outflow rate = 0.462 kg/s

Inflow rate = 0.435 kg/s

00

00

00

00

00

00

,00

00

00

,00

,00

,00

,00

,00

,00

.00

.00

.00

59
Table B-28

Test 240; 7/6 door, 62.9 kVI, location B

TEMPERATURE ("C) *

21

20 172.86

19 180.82

18 181.17

17 30.96 181.31 132.39 181.50 178.42 178.54 177.29 177.56 179.96 177.73 177.19

16 179.53 104.88 179.76 177.63 167.74 166.47 159.04 160.01 171.92 144.69

15 173.63 64.94 169.95 149.44 140.06 138. 16 125.88 126. 15 154.45 121.43

14 29.06 119.06 59.25 85.20 79.93 77.62 68.34 71.48 73.32 72.37 58.81

13 66.18 55.38 58.04 59.66 62.24 62.86 60. 17 58.30 54.96 53.66

12 57 . 40 46.77 48.93 52.40 56.07 54.36 54.82 52.94 50.99 50.63

1

1

52.86 40.61 40.36 42.24 44.84 45.49 43.92 42.35 41.65 47.30

10 28.61 49.90 37.40 37.42 38.72 38.89 36.80 34.51 34. 12 34.35 42.22

9 47.91 34.59 33.71 33.32 32.88 32. 13 31.34 31.46 31.18 37.54

8 46.53 34. 14 32.74 32.39 32.48 31.66 31.21 30.93 30.66 34.65

7 45.20 34.72 33.51 34.04 33. 14 33.58 32.95 32.94 31.95 34.97

6 28.64 44.26 35.90 33.94 33.74 34.02 33.23 32.85 32.31 31.88 33.28

5 42.95 34. 15 32.64 32.55 32.30 32.44 31.75 31.60 30.66 31.68

4 42. 19 35.25 32.47 32.83 32.73 31.86 31.34 31.13 30.84 30.91

3 41.38 34.82 34.92 34. 17 34.08 34.25 33.60 33.09 32.00 33. 18

2 28.81 42.01 34.39 35.01 35.23‘ 35.58 34.60 33.94 32.95 32.29 33.39

>K

H< VELOCITY (m/s)

18 0. 0. 0. 0. 0. 0. 0. 0. 0. 0.

17 0. 1.92 2.00 2.08 2.07 2.07 2.08 2. 17 2.24 2.31

IG 0. 1.48 1.59 1.53 1.46 1.47 1.46 1.47 1.60 1.45

15 0. 0.58 1.13 1.06 1.07 1.09 1.07 1.08 1.18 1.05

14 0. 0.78 0.83 0.75 0.71 0.69 0.70 0.73 0.77 0.84

13 0. 0.31 0.58 0.58 0.54 0.53 0.52 0.51 0.51 0.55

12 0. 0.31 0.40 0.42 0.41 0.39 0.38 0.36 0.32 0.35

11 0. -0.05 0. 13 0.24 0.22 0.20 0.16 0. 10 0.04 0.17

10 0. -0.-23 -0.20 -0.08 -0. 13 -0. 17 -0.24 -0.29 -0.31 0.04

9 0. -0.34 -0.29 -0.28 -0.27 -0.32 -0.36 -0.37 -0.42 -0. 10

8 0. -0.43 -0.39 -0.36 -0.37 -0.38 -0.42 -0.46 -0.53 -0.25

7 0. -0.55 -0.48 -0.46 -0.46 -0.47 -0.51 -0.56 -0.64 -0.42

S 0. -0.59 -0.55 -0.51 -0.50 -0.50 -0.54 -0.60 -0.70 -0.61

5 0. -0.65 -0.57 -0.52 -0.51 -0.51 -0.58 -0.64 -0.74 -0.65

4 0. -0.69 -0.62 -0.55 -0.53 -0.55 -0.60 -0.67 -0.78 -0.79

3 0. -0.72 -0.62 -0.58 -0.55 -0.60 -0.64 -0.75 -0.83 -0.67

2 0. -0.82 -0.68 -0.60 -0.59 -0.60 -0.65 -0.74 -0.86 -0.65

1 *

>k

0. 0 . 0. 0. 0. 0. 0. 0 . 0. 0.

AX = 0. 095 m

AZ = 0. 114 m

Z =

n

1. 032 m

Outflow rate = 0.,483 kg/s

Inflow rate = 0.,464 kg/s

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

60
Table B-29

Test 116; 8/6 door, 62.9 kV7, location B

TEMPERATURE (° C ) *

21

20 164.41

13 172.01

18 172.13

17 30.56 172.04 173.79 174.92 170 . 13 165.97 166.92 168.20 169.74 169.43 171.75

16 169.88 128.53 172.89 158.71 152.84 151.24 150.32 149.41 157.48 166.61

15 159 . 15 102.27 147.21 119.49 116.20 106^11 102.27 93.90 126.84 110.76

14 29.37 86 . 20 57.29 69.55 68 . 18 71.11 63 . 10 64.77 60.74 60 . 17 50.71

13 58 . 12 49.81 50.88 53.83 55 . 19 54 . 16 53.84 51.60 49.76 46.38

12 52.21 44.35 45.82 49.39 50.57 47.97 48. 13 47.67 43.71 43 , 14

11 4Q . 46 40.50 40.78 43.78 44.42 44.07 42.95 38.25 37.38 39.23

10 29.03 45.78 38.46 38,95 39.79 39.90 35.69 35.03 33.81 33.56 35.07

9 44 . 15 34 . 17 33.79 34.65 33.85 32.79 31.80 31.51 31.38 32.27

n 43 . 03 33.81 32.90 32.77 32.64 31.76 31.63 30.87 30.70 30.76

7 42.00 34.06 33.62 33.66 33.34 32.88 32.52 32.38 32 . 10 31.57

6 28.97 41.33 34.64 33.50 33.61 33.42 32.53 32.73 32.07 31.49 30.78

5 40.31 36.38 34.42 34.27 34.08 33.64 33. 19 32.79 32.02 30.92

4 39.75 37 . 13 34 . 12 34.07 34 . 12 33.37 33.04 32.52 31.70 30.87

3 39.12 33.89 34.94 34.63 34.42 33.84 33.54 33.00 32.22 31.42

2 *

29 . 19 39.56 33.85 34.78 34 . 59

' 34.68 34.00 33.63 33 . 13 32.31 31.26

VELOCITY (m/ s )

18 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 17 0 . 2.08 1.97 1.90 1.91 1.99 2.00 2.03 2. 10 2 . 17 0 . 16 0 . 1.49 1.49 1.40 1.35 1.36 1.32 1.30 1.40 1.45 0 . 15 0 . 1.07 0.90 0.90 0.93 0.91 0.91 0.89 0.95 0.99 0 . 14 0 . 0.73 0.72 0.68 0.65 0.63 0.62 0.61 0.62 0,70 0 . 13 0 . 0.36 0.35 0.34 0.33 0.33 0.32 0.33 0.32 0.34 0 . 12 0 . 0.20 0.25 0.25 0.24 0.24 0.21 0.24 0. 15 0.27 0 . 11 0 . -0.07 0.04 0 . 18 0.20 0. 18 0. 13 -0.08 -0. 14 - 0.07 0 . 10 0 . -0.21 -0 . 16 -0 . 10 - 0 . 10 -0.20 - 0.28 -0.26 - 0.33 - 0.22 0 . 9 0 . -0.27 -0.29 - 0.28 - 0.28 -0.31 - 0.35 -0.40 -0.41 -0.34 0 . 8 0 . -0.36 - 0.35 - 0.34 - 0.35 -0.40 - 0.44 -0.42 -0.50 -0.47 0 . 7 0 . - 0.45 - 0.41 - 0.42 -0.40 -0.43 - 0.47 - 0.51 -0.55 -0.59 0 . 6 0 . - 0.51 - 0.45 - 0.43 - 0.44 - 0.48 -0.52 - 0.54 -0.62 -0.67 0 . 5 0 . - 0.56 -0.48 - 0.45 - 0.44 - 0.47 - 0.51 - 0.57 -0.63 -0.74 0 . 4 0 . - 0.65 - 0.53 - 0.49 - 0.48 -0.53 -0.59 - 0.59 -0.69 -0.74 0 . 3 0 . - 0.70 -0.56 - 0.53 - 0.52 - 0.57 - 0.60 -0.66 - 0.71 - 0.79 0 . 2 0 . - 0.77 - 0.61 - 0.60 - 0.58 - 0.62 - 0.65 -0.65 -0.75 - 0.74 0 .

1 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . >x

AX = 0.111 ra AZ = 0.114 m

Z = 1.071 m

nOutflow rate = 0.491 kg/s

Inflow rate = 0.513 kg/s

61
Table B-30

Test 122; full window, 62.9 kW, location B

TEMPERATURE (°C) *

21

20 185.09

19 195. 14

18 195.02

17 29.30 194.91 169.83 197.24 189.60 192.30 193.70 193.88 195. 12

16 193.34 118.70 192.63 181.70 18 1 . 79 180.02 182.50 192. 17

15 189. 18 85.25 189.45 166.25 163.95 148.54 158.51 178.60

14 28. 16 157.38 67. 18 101.04 92.09 90.86 86.76 96.99 104.49

13 80.31 50.09 62.75 66.23 68.32 63.93 60.03 55.09

12 67 . 79 37.50 43.36 48.44 49.25 43.30 39.53 35.64

11 61.42 34. 16 34.28 34.73 33.53 32.31 31.48 31.48

10 27.86 55.77 33.77 33.24 32.88 32.47 32. 12 31.71 30.44

9 52.01 30.95 31.00 30.59 30.33 29.86 29.15 28.78

8 50.04 30.62 30.62 30.22 29.98 29.48 29.06 28.13

? 48.79 30.52 30.58 30.41 30.23 30.00 29.48 29.35

6 27.78 48.33 31.18 31.89 31.81 30.70 30.02 29.92 28.53

5 47.46 30.57 31.14 30.72 30.33 29.65 29.07 28.49

4 47.03 30.60 30.53 29.45 29.66 28.74 23.95 27.29

3 46. 14 30.08 29.51 29.36 28.87 28.67 28.01 27.65

2

>K 27.81 46.42 30. 16 29.98 29.40 29.06 28.69 28.32 26.99

>k VELOCITY (ro/s)

18 0. 0. 0. 0. 0. 0. 0. 0. 0

1? 0. 2. 12 2.07 2. 10 2. 12 2. 17 2.25 2.30 0

16 0. 1.58 1.65 1.58 1.52 1.49 1.58 1.72 0

15 0. 1.29 1.13 1.12 1.10 1.08 1.11 1.39 0

14 0. 0.89 0.76 0.72 0.67 0.66 0.73 0.86 0

13 0. 0.38 0.46 0.46 0.43 0.40 0.33 0.34 0

12 0. -0. 16 -0.07 0.12 0. 12 -0.09 -0.19 -0.20 0

11 0. -0.32 -0.34 -0.33 —0 . 36 -0.39 -0.43 -0.47 0

10 0. -0.48 -0.43 -0.43 -0.44 -0.47 -0.53 -0.61 0

9 0. -0.68 -0.56 -0.54 -0.54 -0.57 -0.65 -0.78 0

8 0. -0.80 -0.65 -0.63 -0.64 -0.66 -0.74 -0.86 0

7 0. -0.97 -0.84 -0.84 -0.81 -0.82 -0.87 -0.97 0

6 0. -1.07 -1.06 -1.03 -1.06 -1.05 -1.04 -1.01 0

5 0. 0. 0. 0. 0. 0. 0. 0. 0

4 0. 0. 0. 0. 0. 0. 0. 0. 0

3 0. 0. 0. 0. 0. 0. 0. 0. 0

2 0. 0. 0. 0. 0. 0. 0. 0. 0

1 >K 0. 0. 0. 0. 0. 0. 0. 0. 0

AX = 0. 106 m

AZ = 0. 114 m

Z = 1. 214 m

nOutflow' rate = 0.358 kg/s

Inf low rate = 0.352 kg/s

62
Table B-31

Test 224; 2/3 Window, 62.9kw, location B

TEMPERATURE (°C) *

21

20 206.28

19 217.46

18 217.18

17 28.92 216.80 215.69 211.38 209.53 209.40 208.86 207. 15 205. 13

16 215.29 190.07 208 . 49 199.97 199.06 191.79 197.40 205.21

15 210.91 123.16 194,92 183.52 176.49 156.64 171.79 186.49

14 27.23 196.71 57.41 96,29 109.21 106.68 103. 13 107.46 85.95

13 111.57 33.44 32.63 34.71 33.99 33.31 32.06 31.24

12 86. 14 32.66 31.71 31.60 31.90 30.70 29.71 28.84

11 78.49 31.45 30.87 31.07 30.93 30.60 29.45 28.82

10 26.37 73.65 31.29 31.13 31.02 30.89 30.47 29.62 28. 17

9 69.05 28.57 28.60. 28.34 28.08 28.02 26.49 26.39

8 64.45 28.52 28.49 28.08 27.83 26.76 26.21 25.67

7 60.83 29.03 28.63 28. 10 27.82 27.84 26.36 26.25

6 26. 19 58.88 29.96 29,62 28.28 28.06 27.11 26.74 25.82

5 57.22 31.27 34.44 30.82 29.79 29.95 29.08 27.42

4 56.79 28.91 28,30 28.13 28.12 27.36 27.68 26.08

3 56.05 28.38 28.33 28.07 27.81 27.64 26.49 26.44

2

>K 26.36 56.79 28.69 28 . 43 27.98 27.92 27.03 26.67 25.85 *

18

VELOCITY (m/s)

0. 0. 0. 0. 0. 0. 0. 0.

17 0. 2. 17 1.95 2.00 2.05 2.03 2.06 2. 15

16 0. 1.64 1.53 1.41 1.36 1.32 1.43 1.63

15 0. 1.13 0.98 0.99 0.98 0.92 0.95 1.22

14 0. 0.30 0.45 0.48 0.44 0.44 0.49 0.35

13 0. -0.48 -0.37 -0.35 -0.34 -0.32 -0.47 -0.53

12 0. -0.61 -0.53 -0.49 -0.47 -0.61 -0.67 -0.77

11 0. -0.88 -0.77 -0.73 -0.73 -0.73 -0.79 -0.95

10 0. -1.12 -1. 10 -1.08 -1.10 -1.14 -1.13 -1.06

9 0. 0. 0. 0. 0. 0. 0. 0.

8 0. 0. 0. 0. 0. 0. 0. 0.

7 0. 0. 0. 0. 0. 0. 0. 0.

6 0. 0. 0. 0. 0. 0. 0. 0.

5 0. 0. 0. 0. 0. 0. 0. 0.

4 0. 0. 0. 0. 0. 0. 0. 0.

3 0. 0. 0. 0. 0. 0. 0. 0.

2 0. 0. 0. 0. 0. 0. 0. 0.

1 0. 0. 0. 0. 0. 0. 0. 0. *

*

AX = 0.016m

AZ = 0.114m

Zm = 1.371m

Outflow rate = 0.261 kg/s

Inflow rate = 0.228 kg/s

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

63
Table B-32

Test 324; 2/3 window, 62.9 kW, location B

1 TEMPERATURE (°c)

21

20 206.03

19 217.23

18 217.20

17 24.42 216.25 212.29 209.47 206.02 207.29 207.02 210.53 209.20

16 214.64 188.35 207.09 199.08 197.76 188.81 196.39 208.23

15 210.28 117.42 183.37 175.91 175.55 157.12 171 .63 183.63

14 22.93 192.53 43.04 73.95 86.73 96.74 91.67 88.64 67.96

13 106.59 29.33 28.08 28.54 30.30 29.49 27.65 28.54

12 83.74 27.61 27.16 27.45 27.89 27.51 27.08 26.32

11 75.95 27.43 26.64 26.70 26.88 26.62 26.41 25.78

10 22.69 70.51 27.40 27.14 27.00 26.99 26.42 26.24 25.66

9 65.84 24.07 24.04 23.77 23.89 23.55 23.42 23.24

B 61.41 24.58 23.73 23.52 23.66 23.04 23.02 22.86

7 57.99 25.49 23.85 23.38 23.46 23.02 22.82 22.83

6 22.51 58.05 26.36 25.23 23.82 23.74 23.81 23.37 22.72

5 54.54 26.97 27.85 24.08 23.60 23.74 23.55 22.68

4 53.99 23.29 23.44 23.28 23.33 23.23 23.08 22.92

3 53.18 23.89 23.58 23.45 23.52 23.15 23.19 23.33

2 22.64 54.25 23.71 23.58 23.55 23.62 23.37 23.28 23.52

« VELOCITY (m/ s )

18 0.00 0.00 0.00 0.00 ' 0.00 0.00 0.00 0.00 0.00

17 0.00 2.27 2.09 2.10 2.11 2.20 2.28 2.40 0.00

16 0.00 1.67 1.61 1.47 1.40 1.39 1.50 1.74 0.00

15 0.00 1.08 0.95 1.01 1.01 0.96 1.00 1.22 0.00

14 0.00 0.15 0.33 0.37 0.40 0.41 0.39 0.25 0.00

13 0.00 -0.47 -0.41 -0.43 -0.44 -0.45 -0.46 -0.54 0.00

12 0.00 -0.70 -0.61 -0.59 -0.60 -0.60 -0.65 -0.80 0.00

11 0.00 -0.92 -0.80 -0.76 -0.76 -0.77 -0.81 - 1.00 0.00

10 0.00 - 1.18 - 1.16 - 1.12 - 1.13 - 1.13 - 1.15 - 1.15 0.00

9 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

8 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

7 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

6 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

5 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

4 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

3 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

2 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

««

AX = 0.106 m

AZ = 0.114 m

Zn = 1.382 m

Outflow rate = 0.268 kg/s

Inflow rate = 0.247 kg/s

64
Table B-33

Test 220; 6/6 door, 31.6 kW, location B

TEMPERATURE (°c)

21

20

19

18

1 ? 27.10

114.01

119.28

119.22

118.92 116 . 16 118.01 117.82 115.88 117. 10 116.95 118.50

16 118.08 112.90 119.54 113.82 112 . 13 110.31 113.74 116.62

15 116.08 50.60 114.76 100 . 12 98.80 91.79 99.30 104. 13

14 25.80 94.28 45.11 68.08 59.65 55.74 54.83 59.79 54.84

13 48.84 42.64 44.81 44.68 44.26 42.88 40.52 38.98

12 42.71 38.09 40.86 41.74 41.74 39 . 18 38.36 36.52

11 39.70 33.04 34.30 35 . 18 33.03 30.48 27.97 31.94

10 25.38 37.75 30.59 29.86 29.28 27.83 26.45 26.52 27.40

9 36.38 28.65 28 . 10 27.72 26.79 26.65 25.75 27.03

8 35.49 29.06 27.64 27.25 26.77 26.24 26.04 26.24

7 34.79 29.22 28.32 28.31 27.35 27. 14 26.31 27.50

6 25.38 34.36 29.77 28.20 27.87 27.49 26.80 26.72 26.72

5 33.76 28.93 27.94 27.72 26.97 26.56 25,61 26.76

4 33 . 43 29.41 27.83 27.54 26.98 26.36 26.07 25.78

3 33 . 03 29 . 15 28.77 28.93 28.24 27.61 26.62 26.23

2 25.68 33.40 28.97 28.97 29.07 28.57 27.56 27.27 26.26

•K* VELOCITY (to/s)

18 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0

17 0 . 1.55 1.54 1.60 1.60 1.64 1.68 1.72 0

16 0 . 1.30 1.23 1 . 18 1.11 1.13 1.19 1.30 0

15 0 . 0.89 0.87 0.83 0.84 0.82 0.86 0.99 0

14 0 . 0.65 0.62 0.57 0.52 0.55 0.59 0.62 0

13 0 . 0.49 0.43 0.39 0.36 0.35 0.34 0.34 0

12 0 . 0.25 0.31 0.29 0.27 0.22 0.20 0.22 0

11 0 . 0.05 0 . 15 0 . 15 0.12 0.04 -0 . 13 0.03 0

10 0 . - 0.22 - 0.13 -0 . 14 -0 . 19 -0.25 -0.26 -0.17 0

9 0 . - 0.27 - 0.25 -0.27 - 0.28 -0.29 -0.33 -0.27 0

8 0 . -0.38 - 0.32 -0.33 - 0.34 -0.35 -0.39 - 0.36 0

7 0 . - 0.46 - 0.40 - 0.40 -0.40 -0.43 -0.48 -0.47 0

6 • 0 . - 0.53 - 0.45 - 0.43 -0.43 - 0.46 - 0.52 -0.56 0

5 0 . - 0.56 - 0.47 - 0.44 - 0.45 - 0.49 - 0.56 -0.60 0

4 0 . - 0.60 - 0.50 - 0.46 - 0.46 -0.49 -0.57 - 0.67 0

3 0 . - 0.62 - 0.50 - 0.45 - 0.45 -0.54 - 0.60 -0.71 0

2 0 . - 0.66 - 0.52 - 0.47 - 0.48 - 0.55 - 0.62 -0.69 0

1 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0

>k*

AX = 0.106 m

AZ = 0.114 m

Z = 1.061 m

nOutflow rate = 0.346 kg/s

Inflow rate = 0.343 kg/s

65
Table B-34

Test 221; 6/6 door, 105.3 kW, location B

TEMPERATURE (°c)

21

20

19

18

17 29.33

222.69

234.83

235.51

235 . 48 203.75 258.05 246.38 245.61 248.06 251.15 242.75

16 233 . 82 143.22 249.59 233.61 231.22 231.46 238.17 246.64

15 228.38 115.93 250.65 223.21 209.80 193.94 210.58 214.63

14 26.47 199.71 85.89 183.82 155.99 137.21 130.32 148.70 152.62

13 101.93 78.21 90.24 92.47 90.82 88.08 82.08 66.82

12 75.54 68.54 74.63 80.57 82.33 80.07 70.83 65.01

1

1

66 . 06 52 . 16 51.86 59.82 62.66 60.62 56.24 51.24

10 25.76 60.70 42 . 16 40.88 47.79 47.77 40.62 35.55 42.37

9 57.22 36.63 36.02 36.54 35.11 32.67 32.24 32.57

8 54.76 35.03 33.77 33.41 33.31 31.67 30.87 32.28

7 52.45 36.57 36.21 34.51 34.64 33.57 33.65 30.91

6 25.94 50.62 36.43 34.65 34.98 34.87 33.83 32.67 30.96

5 48.24 43.69 40.28 35.97 36.09 34.26 33.35 31.50

4 46.91 41.97 38.81 36 . 19 36.21 34.49 32.56 31.89

3 45.34 37.78 37.31 36.78 36.73 35.48 33.90 30.39

2 26.95 46 . 12 36.73 37.55 38.19 38.48 36.86 34.42 32.22

>K

>K

18

VELOCITY (m/ s )

0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . 17 0 . 2.58 2.61 2.70 2.75 2.80 2.88 2.86

16 0 . 2.04 2 . 14 2.06 1.97 1.99 2 . 10 2.24

15 0 . 1.50 1.60 1.54 1.54 1.50 1.61 1.75

14 0 . 1.29 1.18 1.12 1.07 1.07 1.16 1.37

13 0 . 0.64 0.58 0.56 0.52 0.52 0.52 0.75

12 0 . 0.48 0.42 0.42 0.41 0.42 0.38 0.53

11 0 . 0.26 0.30 0.41 0.38 0.34 0.31 0.26

10 0 . - 0.28 -0.22 0.10 0.02 -0 . 13 -0.29 -0.12

9 0 . - 0.41 -0.35 -0.32 -0.35 -0.41 -0.47 -0.42

8 0 . - 0.56 -0.49 -0.47 -0.49 -0.53 -0.58 -0.57

7 0 . - 0.73 -0.65 -0.61 -0.61 -0.65 - 0.72 -0.74

6 0 . - 0.32 -0.73 - 0.68 -0.67 -0.71 - 0.80 -0.89

5 0 . - 0.86 -0.78 -0.72 -0.70 -0.74 -0.83 -0.94

4 0 . - 0.90 -0.83 - 0.76 -0.74 -0.78 -0.87 - 1.08

3 0 . -0.98 - 0.87 -0.79 -0.77 -0.80 -0.91 - 1.12

2 0 . - 1.08 - 0.90 -0.81 -0.80 -0.85 -0.95 - 1.20

1 0 . 0 . 0 . 0 . 0 . 0 . 0 . 0 . X<

AX = 0.106 m

AZ = 0.114 m

Z =1. 000 m

nOutflow rate = 0.498 kg/s

Inflow rate = 0.505 kg/s

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

66
Table B-35

Test 514; 2/6 door, 62.9 kW, location C

TEMPERATURE (°C)

21

20 201.69

19 210.11

18 211.00

17 10.57 210.85 206.56 200.84 202.91

16 210.35 198.39 199.82 199.58

15 208.63 169.73 191.37 195.19

14 8.93 208.16 185.63 191.71 192.64

13 205.65 191.57 191 . 15 194.28

12 200.40 168.82 185.27 187.44

11 188.07 118.76 146.98 151.64

10 8.75 127.89 32.72 51.77 38.02

9 78.72 11.37 10.36 11.08

8 65.45 9.88 9.58 9.36

7 56.06 12.49 11.46 10.87

6 7.79 49.57 11.72 11.64 10.31

5 46.20 10.21 8.77 8.50

4 45.00 10. 16 9.46 8.60

3 43.03 11.76 11.44 11.55

2 8.87 41.42 11.79 11.56 11.70

*

•» VELOCITY (m/ s)

%

TC 18 0.00 0.00 0.00 0.00 0 . 17 0.00 3.36 3.22 3.43 0 . 16 0.00 2.98 2.86 3.04 0 . 15 0.00 2.60 2.57 2.71 0 . 14 0.00 2.51 2.35 2.49 0 . 13 0.00 2.19 1.99 2.13 0 . 12 0.00 1.72 1 . 5 ?! 1.67 0 . 11 0.00 1.09 1.06 1.12 0 . 10 0.00 -0.06 0.25 -0.05 0 . 9 0.00 - 0.62 - 0.64 -0.68 0 . 8 0.00 - 0.82 -0.81 -0.89 0 . 7 0.00 - 1.06 - 1.04 - 1.13 0 . 6 0.00 - 1 .21 - 1.16 - 1.25 0 . 5 0.00 - 1 .33 - 1.26 - 1.36 0 . 4 0.00 - 1.43 - 1.34 - 1.45 0 . 3 0.00 - 1.44 - 1 .44 - 1.53 0 . 2 0.00 - 1.54 - 1.47 - 1.57 0 . 1 0.00 0.00 0.00 0.00 0 . »

*

A X = 0 . 067 jn

A Z = 0.114 VD Zn = 0,966 in Outflow rate = 0,248 kg/

s

Inflow rate = 0,238 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

,00

00

,00

,00

67
Table B-36

Test 544; 3/6 door, 62.9 kW, location C

TEMPERATURE

« 21

20 166.88

19 173.52

18 174.25

17 8.84 174.18 168.56 168.70 167.52 167.74 167.47

16 173.56 161 .13 168.41 164.25 163.67 165.14

15 172.24 128.91 161.84 159.66 160.62 162.02

14 7.30 171.16 139.22 158.27 154.93 157.06 160.34

13 167.20 136.01 154.60 150.71 151.32 154.20

12 155.60 97.29 114.48 121.33 117.85 132.01

11 103.97 37.72 52.27 55.08 56.03 48.27

10 7.21 56.67 13.32 16.43 14.60 12.32 11.68

9 44.29 9.67 9.32 8.57 8.77 8.87

B 38.77 9.33 9.11 8.23 8.07 8.94

7 36.04 10.88 10.64 9.93 9.12 7.86

6 6.31 34.07 10.89 10.59 9.77 8.22 6.99

5 32.07 10.08 9.37 7.70 7.05 6.20

4 30.83 10.66 9.88 8.22 6.71 6.06

3 29.20 10.31 10.20 9.48 9.36 8.89

2

* 7.43 27.30 10.54 10.46 9.53 9.39 9.03

VELOCITY

18 0.00 0.00 0.00 0.00 ' 0.00 0.00 0 . 17 0.00 2.94 2.85 2.82 2.81 2.98 0 . 16 0.00 2.55 2.39 2.34 2.37 2.54 0 . 15 0.00 2. 19 2.07 2.00 2.07 2.33 0 . 14 0.00 2.12 1.84 1.74 1.79 2.03 0 . 13 0.00 1.75 1.50 1.41 1.43 1.68 0 . 12 0.00 1.14 1.03 1.01 1.00 1.17 0 . 11 0.00 0.40 0.45 0.45 0.43 0.38 0 . 10 0.00 -0.37 -0.29 -0.35 -0.40 -0.41 0 . 9 0.00 -0.61 -0.57 -0.58 -0.62 -0.64 0 . 8 0.00 -0.78 -0.69 -0.71 -0.78 -0.74 0 . 7 0.00 -0.92 -0.84 -0.84 -0.87 -0.90 0 . 8 0.00 - 1.03 -0.94 -0.92 - 1.00 - 1.03 0 . 5 0.00 -1 . 10 - 1 .01 -0.98 - 1.03 - 1.12 0 . 4 0.00 - 1.15 - 1.05 - 1.03 - 1.10 - 1.24 0 . 3 0.00 - 1.13 - 1.12 - 1 .08 - 1.12 - 1.28 0 . 2 0.00 - 1.22 - 1.16 - 1 . 13 -0.67 - 1.32 0 . 1 0.00 0.00 0.00 0.00 0.00 0.00 0 . ««

Ax = 0.065 m

AZ = 0.114 m

Zn = 1.025 m

Outflow rate ^ 0v343 kg/s

Inflow rate = 0.337 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

68
Table B-37

Test 512; 4/6 door, 62.9 kW, location C

I TEMPERATURE ( 0 (-)

21

20 168.33

19 174.07

18 174.84

17 22.38 174.44 163.32 168.27 167.04 168.14 169.57

16 173.95 151.40 166.79 164.68 165.29 167.94

15 172.55 118.36 162.18 160.04 161.80 164.94

14 20.91 170.63 122.23 155.13 153.01 155.96 160.62

13 163.41 113.47 134.30 144.36 140.37 144.22

12 128.79 67.41 78.32 83.16 86.51 82.36

11 76.18 53.34 57.70 50.05 41.46 35.21

10 20.99 58.03 37.70 30.46 28.64 25.70 25.02

9 51.49 24.29 22.23 22.52 22.39 23.11

B 48.44 24.10 21.94 21.70 21.74 22.46

7 46.35 23.85 22.78 23.37 23.41 22.27

6 19.66 44.40 23.39 23.06 23.48 23.19 22.22

5 42.56 23.79 22.77 21.67 21 . 19 20.64

4 41.56 25.91 23.41 21.82 21.16 20.78

3 40.11 22.57 22.96 23.45 23.66 23.74

2 20.85 38.21 23.30 23.54 23.60 23.86 23.96

VELOCITY

h 18 0.00 0.00 0.00 0.00 0.00 0.00 0.00

17 0.00 2.59 2.51 2.46 2.44 2.60 0.00

16 0.00 2.14 2.05 1 .99 1.98 2.21 0.00

15 0.00 1.78 1.73 1 .64 1.72 2.02 0.00

14 0.00 1.69 1.46 1 . 3P 1.46 1.77 0.00

13 0.00 1.34 1.12 1 . C? 1.09 1.36 0.00

12 0.00 0.73 0.65 0.58 0.61 0.66 0.00

11 0.00 0.36 0.34 0.27 0.17 0.11 0.00

10 0.00 -0.23 -0.24 -0.29 -0.35 -0.35 0.00

9 0.00 -0.50 -0.49 -0.46 -0.46 - 0.52 0.00

8 0.00 -0.65 -0.60 -0.56 -0.58 -0.67 0.00

7 0.00 -0.82 - 0.74 -0.68 -0.71 - 0.85 0.00

6 0.00 -0.92 -0.81 -0.77 -0.80 -0.96 0.00

5 0.00 - 0.97 -0.87 -0.82 -0.86 - 1.05 0.00

4 0.00 - 1.02 -0.91 -0.87 -0.91 - 1.13 0.00

3 0.00 - 1.03 -0.94 -0.92 -0.95 -0.68 0.00

2 0.00 - 1.07 -0.97 -0.93 -0.97 -0.67 0.00

1 0.00 0.00 0.00 OoOO 0.00 0.00 0.00

*

«

AX = 0.098 m

AZ = 0.114 m

Zn = 1.034 m

Outflow rate = 0.393 kg/s

Inflow rate = 0.383 kg/s

69
Table B-38

Test 342, 5/6 door, 62.9 kW, location C

1 TEMPERATURE (‘^O

21

20 156.60

19 161.67

18 162.02

17 22.15 161.96 147.72 157.15 156.33 155.80 154.03 154.88 155.25

16 161.15 128.26 155.68 153.96 152.85 150. 14 155.50 153.54

15 158.97 98.11 151 . 19 148.51 146.27 145.60 147.41 141 .30

14 20.55 155.19 87.59 135.89 132.14 134.78 137.19 143.22 131.08

13 140.68 72.82 89.32 94.06 99.23 107.45 117.25 112.64

12 92.89 54.60 57.68 62.90 62.36 61.23 57.82 45.91

11 59.34 47.04 48.09 45.46 40.51 31.12 28.39 34.33

10 20.66 48.36 34.73 28.26 29.11 26.47 23.81 23.05 24.76

9 44.23 25.02 22.55 22.75 22.49 21.69 21.68 24.05

B 42.61 25.31 22.51 21.81 21.58 21.19 21.40 22.20

7 41.59 25.26 23.06 23.06 23.04 22.47 22.25 20.93

B 19.57 40.74 24.74 23.10 22.97 23.05 22.45 22.59 21.54

5 39.49 26.99 23.75 22.63 21.87 20.87 20.33 19.90

4 38.32 29.11 24.01 22.76 21.98 21.12 20.69 20.43

3 36.38 24.76 23.63 23.58 23.30 22.57 22.33 22.89

2 20.57 35.56 23.93 23.95 23.13 23.12 22.95 23.54 23.39

VELOCITY

18 0.00 0.00 0.00 0.00 » 0.00 0.00 0.00 0.00 0 . 17 0.00 2.37 2.37 2.35 2.28 2.31 2.33 2.45 0 . 16 0.00 1.84 1.88 1.87 1.78 1.79 1.87 2.11 0 . 15 0.00 1.47 1.57 1.47 . 1.44 1.49 1.60 1.75 0 . 14 0.00 1.18 1.27 1.20 1.20 1.23 1.31 1.50 0 . 13 0.00 0.98 0.87 0.73 0.72 0.75 0.92 1.11 0 . 12 0.00 0.47 0.45 0.47 0.43 0.41 0.41 0.41 0 . 11 0.00 0.26 0.23 0.24 0.15 -0.09 -0.17 0.18 0 . 10 0.00 -0.24 -0.23 -0.25 -0.30 -0.32 -0.35 -0.25 0 . 9 0.00 -0.48 -0.46 -0.41 -0.43 -0.42 -0.45 -0.42 0 . 8 0.00 -0.56 -0.55 -0.52 -0.49 -0.49 -0.54 -0.57 0 . 7 0.00 -0.74 -0.68 -0.62 -0.60 -0.60 -0.66 -0.71 0 . 6 0.00 -0.80 -0.75 -0.69 -0.66 -0.67 -0.74 -0.83 0 . 5 0.00 -0.86 -0.78 -0.72 -0.70 -0.72 -0.79 -0.93 0 . 4 0.00 -0.89 -0.83 -0.76 -0.74 -0.76 -0.83 -0.99 0 . 3 0.00 -0.90 -0.86 -0.77 -0.76 -0.81 -0.88 - 1.09 0 . 2 0.00 -0.97 - 0.88 -0.82 -0.80 -0.82 -0.90 - 1.09 0 . 1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . *

AX = 0.086 m

AZ = 0.114 m

Zn = 1.056 m

Outflow rate = 0.440 kg/s

Inflow rate = 0.442 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

70
Table B-39

Test 610; 6/6 door, 62.9 kW, location C

1 TEMPERATURE (° C )

21

20 146.92

19 151.81

18 152.25

17 19.66 152.34 146.49 147.50 146 . 84, 144.69 145.48 145.32 145.25

16 151.63 116.08 146.99 145.84 142.82 141.52 141.24 140.10

15 149.63 80.95 140.29 137.65 134.90 136.00 137.26 121.87

14 18.39 144.85 75.22 120.57 117.05 123.38 127.40 127.06 115.50

13 119.41 56.39 65.66 63.95 69.64 76.34 79.88 65.80

12 66.16 43.21 47.71 47.16 46.54 43.06 37.67 35.58

11 46.07 34.19 37.17 38.84 33.51 27.55 24.50 27.86

10 18.28 39.52 26.20 23.75 25.96 23.14 21.43 20.22 21.80

9 37.16 23.36 20.31 20.64 19.74 19.80 19.14 20.24

B 36.15 22.01 20.36 19.76 19.37 19. 10 18.83 18.85

7 35.31 24.29 20.67 20 . 96 20.39 20.61 19.67 18.10

6 17.35 34.56 23.76 20.98 20.49 20.71 20.31 19.92 17.38

5 33.42 25.45 21.06 20.38 19.29 19.14 17.95 17.35

4 32.46 25.59 21.76 20.69 19.74 19.04 18.34 16.66

3 31.03 24.23 21.08 21.23 20.62 20.89 20.04 19.99

2 18.33 30.79 21 .71 21.87 21.36 21.25 21.33 20.74 19.25

VELOCITY (m/s)

18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

17 0.00 2.24 2.25 2.22 2.19 2.15 2.25 2.31 0.00

16 0.00 1.74 1 .-78 1.71 1.65 1.64 1.70 2.03 0.00

15 0.00 1.28 1.38 1.30 1.31 1.34 1.47 1.53 0.00

14 0.00 1 . 16 1.11 1.09 1,08 1.09 1 . 15 1.43 0.00

13 0.00 0.84 0.67 0.61 0.62 0.65 0.72 0.84 0.00

12 0.00 0.40 0.38 0.39 0 . o 0.33 0.29 0.36 0.00

11 0.00 0.12 0.21 0.22 0.18 -0.09 - 0.13 0.12 0.00

10 0.00 -0.28 -0.24 -0.17 -0.24 -0.26 -0.31 -0.17 0.00

9 0.00 -0.45 -0.41 - 0.37 -0.37 - 0.37 -0.41 -0.40 0.00

B 0.00 -0.54 -0.48 - 0.44 -0,44 - 0.45 -0.47 -0.51 0.00

7 0.00 -0.70 - 0.60 - 0.56 -0.53 - 0.53 -0.60 - 0.65 0.00

6 0.00 - 0.73 -0.64 -0.60 -0.59 -0.61 -0.65 -0.73 0.00

5 0.00 - 0.78 - 0.69 -0.62 - 0.61 —0 . 63 -0.70 -0.86 0.00

4 0.00 - 0.76 -0,72 -0.64 - 0.65 - 0.67 -0.73 -0.95 0.00

3 0.00 - 0.78 -0.74 -0.68 -0.67 -0.70 -0.78 - 0.99 0.00

2 0.00 - 0.88 -0.78 -0.71 - 0.70 -0.70 -0.78 - 1.04 0.00

1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

AX = 0.106 ni AZ = 0.114 m

Zn = 1.059 m

Outflow rate = 0.498 kg/s

Inflow rate = 0.479 kg/s

71
Table B-40

Test 510; 6/6 door, 62.9 kW, location C

I TEMPERATURE (°c)

21

20 151 .02

10 156.45

18 156.98

17 24.70 157.20 152.99 152.15 151.40 150.44 150.36 152.28 154.41

IG 156.66 136.31 149.59 147.99 145.55 146.93 149.77 147.32

15 154.78 80.86 146.26 141.77 140.11 141.29 145.82 144.58

22.94 150.98 73.52 127.81 124.69 131.04 132.09 131.32 126.39

13 125.13 66.02 73.17 72.07 79.12 79.80 82.95 71.59

12 69.95 50.00 56.92 55.97 58.27 52.87 53.49 44.61

1

1

51.82 39.80 40.89 41.91 42.53 37.49 34.04 34.97

10 22.59 45.77 31.90 27.03 28.39 28.60 26.52 25.68 28.02

9 43.13 27.57 24.52 24.60 25.07 24.58 24.49 26.00

B 41.64 26.21 23.82 24.12 24.15 23.94 24.21 25.37

7 40.44 26.21 24.42 24.37 25.12 25.36 24.49 24.50

B 22.00 39.43 25.12 24.16 24.86 24.88 25.34 25.24 23.40

5 37.95 28.23 23.92 23.70 24.30 24.27 23.48 23.77

4 37.08 29.26 24.15 24.35 24.25 24.23 23.90 23.04

3 36.08 27.61 25.21 25.79 26.80 26.87 26.32 27.02

2 23.01 36.01 25.55 26.21 26.96 26.95 27.19 27.57 26.06

«•

A VELOCITY . (a/s)

If 18 0.00 0.00 0.00 0.00 ' 0.00 0.00 0.00 0.00 0 . 17 0.00 2.24 2.15 2.20 2.09 2.11 2.16 2.26 0 . 16 0.00 1.77 1.73 1.65 1.52 1.57 1 .68 1.87 0 . 15 0.00 1.27 1.36 1.28 1.27 1.29 1.42 1.71 0 . 14 0.00 1.05 1.09 1.05 1.01 1.05 1 . 12 1.44 0 . 13 0.00 0.85 0.68 0.58 0.57 0.60 0.64 0.79 0 . 12 0.00 0.39 0.38 0.35 0.33 0.33 0.33 0.32 0 . 11 0.00 0.12 0.15 0.15 0.18 0. 18 0.06 0.13 0 . 10 0.00 -0.32 -0.27 -0.25 -0.22 -0.26 -0.29 -0.19 0 . 9 0.00 -0.42 -0.38 - 0.36 -0.36 -0.40 -0.44 -0.42 0 . 8 0.00 -0.54 -0.49 -0.44 -0.43 -0.46 -0.51 -0.53 0 . 7 0.00 -0.71 -0.59 -0.54 -0.51 -0.56 -0.63 -0.68 0 . 8 0.00 -0.78 -0.65 -0.59 -0.58 -0.61 -0.67 -0.76 0 . 5 0.00 -0.83 -0.70 -0.65 -0.63 -0.64 -0.73 -0.84 0 . 4 0.00 -0.87 -0.75 -0.67 -0.65 -0.66 -0.74 -0.91 0 . 3 0.00 -0.85 -0.77 -0.70 -0.67 - 0.69 -0.77 -0.99 0 . 2 0.00 -0.90 -0.73 -0.64 -0.63 -0.69 -0.79 - 1.01 0 . 1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . «

AX = 0.J06 m

AZ = 0.114 m

Zm = 1.046 m

Outflow rate = 0.476 kg/s

Inflow rate = 0.474 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

72
Table B-Al

Test 540; 7/6 door, 62.9 kW, location C

TEMPERATURE (°c )

21

20 136.45

13 141.04

18 141.40

17 15.63 141.43 121.38 134.39 136.75 133.87 135.30 136.71 134.71 137.17 137.14

16 140.33 89.70 133.90 133.03 131.33 130.72 130.46 131.13 132.42 134.80

15 137.24 49.72 125.05 122.05 119.62 120.27 125.19 123.46 126.56 125.75

14 14.45 126.89 53.92 86.22 76.64 86.44 84.51 91.83 97.92 94.93 102.90

13 63.69 36.76 45.64 47.05 47.06 44.85 47.39 43.60 41.68 37.58

12 46.14 25.39 31.67 34.96 36.66 36.29 34.71 30.61 27.53 32.42

11 35.99 20.96 24.26 26.46 27.82 24.92 23.04 20.61 19.87 24.99

10 14.40 32.38 17.84 19.29 19.80 20.19 19.98 17.92 17.01 16.98 20.59

9 31.07 16.37 16.49 16.50 16.43 15.74 16.45 16.06 16.44 19.60

3 30.27 15.17 15.66 15.40 15.45 15.37 15.58 15.60 15.91 17.62

7 29.52 18.32 16.51 16.41 16.27 16.36 17.13 16.16 15.90 15.91

6 13.72 28.79 17.86 16.21 16.06 16.36 16.24 16.44 16.31 15.47 15.20

5 27.72 21.26 16.92 16.48 15.78 15.35 15.98 14.89 14.70 14.46

4 26.83 18.78 16.46 16.40 16.19 15.96 15.40 15.15 14.69 14.36

3 25.53 21.09 16.76 16.61 16.41 16.45 17.46 16.90 17.18 17.27

2 14.61 25.45 17.55 16.91 16.87 17.03 17.18 17.34 17.47 17.89 17.05

L VELOCITY (m/s)

F 18 0.00 0.00 0.00 0.00

% 0.00 0.00 0.00 0.00 0.00 0.00

17 0.00 2.13 2.19 2.20 2.20 2.23 2.14 2.21 2.30 2.41

16 0.00 1.68 1.70 1.64 1.58 1.58 1.60 1 .62 1.70 1.89

15 0.00 1.04 1.26 1 . 16 1.21 lc 24 1.25 1.27 1.38 1.79

14 0.00 1 . 13 0.98 0.91 0.93 0.90 0.92 0.95 0.98 1.25

13 0.00 0.66 0.61 0.57 0.55 0 . 5? 0.53 0.50 0.50 0.53

12 0.00 0.34 0.37 0.37 0.38 0.34 0.33 0.25 0.18 0.36

11 0.00 - 0.17 0.08 0.12 0.15 0.08 -0.06 -0. 18 -0.19 0.13

10 0.00 -0.28 -0.26 -0.22 -0.20 -0.27 -0.31 -0.34 -0.37 -0.15

9 0.00 - 0.40 -0.37 -0.35 -0.35 -0.37 -0.37 -0.42 -0.44 -0.28

8 0.00 - 0.47 -0.44 -0.44 -0.42 - 0.44 -0.46 -0.48 -0.54 -0.41

7 0.00 - 0.55 -0.53 -0.52 - 0.52 -0.52 -0.51 -0.57 -0.63 - 0.54

6 0.00 -0.62 -0.56 -0.56 -0.54 -0.55 -0.59 -0.62 -0.71 -0.73

5 0.00 -0.57 -0.60 - 0.58 -0.57 -0.57 -0.58 -0.64 -0.71 - 0.80

4 0.00 - 0.69 -0.64 - 0.59 -0.56 - 0.58 -0.64 - 0.67 -0.76 -0.92

3 0.00 - 0.56 -0.67 -0.60 - 0.58 -0.60 -0.63 -0.69 -0.78 -0.99

2 0.00 -0.80 -0.74 -0.67 - 0.60 - 0.62 -0.65 - 0.70 - 0.82 - 1 .03

1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

««

AX = 0.095 m

AZ = 0.114 la Zn = 1.082 m

Outflow rate = 0.560 kg/s

Inflow rate = 0.539 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

.00

00

.00

,00

,00

73
Table B-42

Test 517; 8/6 door, 62.9 kW, location C

1 TEMPERATURE (°C)

*21

20 129.43

19 133.96

18 134.44

17 16.00 134.68 105.51 131.11 129.91 131.66 128.97 128.89 128.88 130.25 129.31

16 134.07 71 .65 130.64 124.77 127.75 126.17 124.00 126.42 125.69 121.05

15 131.88 51.42 117.65 113.82 116.17 116.82 117.21 113.13 118.18 105.86

14 15.01 119.56 41.36 77.37 71.95 74.20 76.72 77.73 73.14 66.07 61.43

13 68.02 33.22 39.72 40.94 41.10 40.24 40.02 37.73 34.01 32.05

12 41.23 25.09 29.08 31.95 33.91 32.85 31 .38 27.89 25.52 26.46

11 34.09 22.47 23.59 26.04 28.03 24.20 23.64 20.64 19.39 22.45

10 14.93 30.67 19.86 18.29 19.93 19.97 19.59 18.30 17.57 17.68 19.43

3 29.06 17.34 16.76 17.26 17.75 16.74 16.61 16.76 16.66 19.07

8 28.09 17.23 16.40 15.77 16.26 16.26 16.17 16.10 16.51 17.92

7 27.32 18.07 16.25 16.69 17.19 16.98 16.90 16.61 16.49 16.72

6 14.33 26.64 18.66 16.72 16.09 16.96 16.97 16.71 16.68 15.71 15.79

5 25.65 19.08 15.99 16.20 16.47 16.13 15.82 15.46 15.37 15.39

4 24.38 19.86 17.32 15.84 16.75 16.47 15.70 15.82 15.06 14.73

3 24.05 18.26 16.92 17.10 17.52 17.48 17.43 17.04 17.61 17.31

2

K- 14.98 24.41 18.79 18.11 17.71 18.30 18.04 17.96 18.18 17.56 17.14

« VELOCITY (m/s)

% 18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 17 0.00 2.07 2.18 2.08 2.05 2.07 2.06 2.16 2.24 2.33 0 . 16 0.00 1 .42 1.58 1.55 1.48 1.47 1.46 1.49 1.63 1.64

15 0.00 1.21 1.20 1.15 1.14 1.15 1.16 1.17 1.25 1.43 0 . 14 0.00 0.89 0.83 0.86 0.81 0.82 0.81 0.80 0.81 0.94 0 . 13 0.00 0.63 0.50 0.45 0.43 0.40 0.37 0.36 0.36 0.35 0 . 12 0.00 0.19 0.22 0.31 0.28 0.25 0.22 0.19 0.14 0.19 0 . 11 0.00 -0.14 0.12 0.15 0.19 0.09 -0.03 -0.16 -0.19 0.05 0 . 10 0.00 -0.27 -0.28 -0.20 -0.22 -0.23 -0.28 -0.30 -0.33 -0.22 0 . 9 0.00 -0.35 -0.34 -0.33 -0.29 -0.34 -0.38 -0.39 -0.42 -0.32 0 . 8 0.00 -0.42 -0.43 -0.42 -0.40 -0.41 -0.43 -0.44 -0.49 -0.40 0 . 7 0.00 -0.52 -0.48 -0.48 -0.45 - 0.49 -0.51 - 0.53 -0.58 -0.51 0 . 6 0.00 -0.57 -0.55 -0.53 -0.50 -0.52 -0.54 -0.55 -0.64 -0.63 0 . 5 0.00 -0.59 -0.53 -0.53 -0.49 -0.50 -0.54 -0.60 - 0.65 -0.72 0 . 4 0.00 - 0.64 -0.57 -0.55 -0.51 -0.53 -0.57 -0.60 -0.70 - 0.82 0 . 3 0.00 - 0.67 - 0.60 -0.55 -0.53 -0.53 -0.58 - 0.64 -0.72 -0.88 0 . 2 0.00 -0.73 -0.66 -0.63 -0.56 -0.53 -0.60 -0.63 -0.74 -0.91 0 . 1 *

»

0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 .

AX = 0.111 m

AZ = 0.114 in Zn = 1.085 m

Outflow rate = 0.593 kg/s

Inflow rate = 0.576 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

74
Table B-43

Test 622; full window, 62.9 kW, location C

1 TEMPERATURE (^C ) #

21

20 148.07

19 153.37

18 153.94

17 11.10 154.09 138.77 148.01 14fe .44 148.04 148.64 152.83 150.72

16 153.65 119.42 146.35 146.97 143.57 142.43 145.65 146.11

15 152.10 83.40 138.55 135.82 137.97 138.19 145.72 119.22

14 9.47 148.12 75.17 115.58 118.77 125.31 122.42 113.97 114.05

13 123.74 53.73 71 .72 70.45 68.80 65.89 66.01 67.29

12 70.34 18.77 17.99 25.39 30.33 25.53 20.33 20.24

11 49.66 13.86 12. 12 12.16 13.02 12.26 11.32 12.42

10 9.45 40.23 13.16 11.31 11.83 11.84 11.54 10.92 10.95

9 34.34 11.83 11.27 10.45 10.82 10.55 9.98 10.03

8 31.11 11.52 10.64 10.89 10.86 10.42 9.96 10.05

7 29.76 12.33 12.93 12.09 11.85 11.35 10.15 9.05

6 8.65 29.09 11.42 11.67 11.55 11.49 10.80 10.15 9.77

5 28.28 11.29 11.10 9.92 10.07 10.08 9.22 8.53

4 27.78 10.94 10.63 10.33 10.48 9.84 9.15 9.01

3 26.62 10.80 10.47 9.72 10.10 10.29 9.33 8.75

2 9.59 26.90 11.05 10.18 10.48 10.81 10.70 10.01 9.92

»

JL VELOCITY . 1r 18 0.00 0.00 0.00 0.00 ' 0.00 0.00 0.00 0.00 0.

17 0.00 2.27 2.27 2.23 2.20 2.27 2.38 2.53 0.

16 0.00 1.84 1.77 1.68 1.61 1.67 1.83 2.04 0.

15 0.00 1.46 1.35 1.29 1.28 1.32 1.47 1.54 0.

14 0.00 1.14 1.03 1.02 1.02 1.03 1.07 1.31 0.

13 0.00 0.56 0.57 0.55 0.52 0.51 0.46 0.58 0.

12 0.00 -0.23 -0.18 -0.11 -0. 10 -0.14 -0.21 -0.26 0.

11 0.00 -0.55 -0.49 -0.48 -0.49 -0.50 -0.54 -0.56 0.

10 0.00 -0.70 -0.60 -0.58 -0.57 -0.59 -0.64 -0.79 0.

9 0.00 -0.79 -0.67 -0.62 -0.62 -0.63 -0.72 -0.87 0.

8 0.00 -0.87 -0.73 -0.69 -0.68 -0.71 -0.78 -0.98 0.

7 0.00 -1.02 -0.88 -0.83 -0.84 -0.85 -0.95 -1.12 0.

6 0.00 -1.17 -1.10 -1 . 09 -1.11 -1.15 -1 . 16 -1.22 0.

5 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.

4 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.

3 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.

2 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.

1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.

«»

AX = 0.106 m

AZ = 0.114 m

Zn = 1.228 m

Outflow rate = 0.441 kg/s

Inflor rate ss 0.435 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

75
Table B-AA

Test 522; full window, 62.9 kW, location C

1 TEMPERATURE (‘^ C ) « 21

20 153.30

IS 158.98

18 159.40

17 15.24 159.57 155.82 154.86 154.32 152.47 152. 10 151.75 151.98

16 158.97 145.61 153.53 149.44 150. 10 149.08 149.70 150.07

15 156.95 91.05 146.07 144.37 143.46 143.20 144.95 141.96

14 13.25 152.53 87.68 122.95 127.60 133.22 130.62 123.40 127.01

13 127.79 65.30 74.79 72.68 73.98 70.80 69.32 68.71

12 72.93 28.54 26.24 35.35 35.30 30.54 22.82 22.37

11 52.93 19.32 14.94 15.03 17.08 15.73 15.12 15.29

10 13.28 44.28 18.30 15.55 14.95 15.06 14.58 14.68 14.04

9 37.99 15.16 13.80 13.73 13.99 13.71 13.41 13.95

B 34.13 14.44 13.74 13.58 13.62 13.34 13.46 13.38

7 32.42 15.88 15.82 15.57 15.21 15.26 14.06 13.20

6 12.77 31.74 14.42 14.92 14.09 14.09 13.96 13.79 13.28

5 30.71 13.76 13.22 13.27 13.48 13.51 13.34 12.97

4 30.27 14.09 14.03 13.68 13.76 13.49 13.47 13.10

3 29.19 14.95 13.51 13.81 14.02 14.16 13.88 13.52

13.95 29.34 14.70 13.89 14.14 14.29 14.18 14.29 14.06

VELOCITY (m/ s ) % 18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

17 0.00 2.28 2.14 2.17 2.15 2.16 2.22 2.30 0.00

16 0.00 1.84 1.69 1.62 1.58 1.61 1.72 1.94 0.00

15 0.00 1.45 1.29 1 .26 1.25 1.30 1.40 1.69 0.00

14 0.00 1.13 1.02 1 .01 1.01 1.04 1.05 1.30 0.00

13 0.00 0.64 0.55 0.51 0.52 0.51 0.55 0.61 0.00

12 0.00 -0. 16 -0.08 0.08 -0.03 -0.11 -0.19 -0.18 0.00

11 0.00 -0.56 -0.49 -0.47 -0.40 -0.45 -0.45 -0.51 0.00

10 0.00 -0.73 -0.61 -0.58 -0.54 -0.55 -0.59 -0.73 0.00

9 0.00 -0.83 -0.68 -0.63 -0.60 -0.61 -0.64 -0.83 0.00

8 0.00 -0.94 -0.76 -0.70 -0.68 -0.70 -0.75 -0.93 0.00

7 0.00 - 1.05 -0.88 -0.84 -0.82 -0.86 -0.89 - 1.05 0.00

8 0.00 - 1.18 - 1.12 - 1.11 - 1.11 - 1.11 - 1.13 - 1.13 0.00

5 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

4 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

3 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

2 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

*

«

AX = 0.106 m

AZ = O.llA m

Zn = 1.215'm

Outflow rate = 0.A26 kg/s

Inflow rate = 0.A16 kg/s

76
Table B-45

Test 524; 2/3 window, 62.9 kW, location C

1 TEMPERATURE (°C)

21

20 171.34

19 178.25

19 178.85 . 17 10.36 178.84 163.53 173.01 172.01 170.57 169.13 168.83 169.88

16 178.32 144.47 170.11 167.50 165.67 164.39 166.06 167.47

15 176.69 89.61 165.58 163.23 160.04 158.68 165.11 141 .92

14 8.76 174.73 49.87 115.87 135.40 142.31 135.65 121.07 94.21

13 166.74 16.49 13.25 20.63 18.83 18.98 14.20 12.51

12 132.39 12.23 11.52 12.14 12.42 12.36 12.01 11.43

11 85.82 11.76 11.43 11.34 12.02 11.80 11.03 10.64

10 8.92 66.31 11.06 11.43 11.67 11.60 11.68 11.32 10.70

9 56.01 9.01 9.66 9.45 9.56 9.51 8.92 8.98

B 49.57 9.36 9.46 9.37 9.14 9.06 8.87 8.88

7 45.85 9.24 10.05 9.61 9.40 9.49 8.72 8.93

6 6.34 43.69 9.60 10.24 10.30 9.84 9.81 9.29 8.98

5 42.27 10.69 13.84 11.41 10.70 10.69 10.10 9.22

4 41.66 9.97 10.30 9.47 9.24 9.29 9.18 8.97

3 40.76 9.03 9.60 9.41 9.24 9.53 9.06 9.21

2 6.93 41.67 9.17 8.89 9.14 9.21 9.74 9.64 9.36

VELOCITY

18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 17 0.00 2.22 2.14 2.07 2.10 2.11 2.23 2.44 0 . 16 0.00 1.78 1.66 1 .55 1.50 1.55 1.66 1.90 0 . 15 0.00 1.24 1.22 1.14 1,16 1.14 1 .28 1.34 0 . 14 0.00 0.47 0.70 0.77 0 . 8 ^ 0.76 0.72 0.55 0 . 13 0.00 - 0.54 -0.48 -0.40 -0.43 -0.43 -0.44 - 0.49 0 . 12 0.00 - 0.90 -0.65 -0.63 -0.62 -0.61 -0.64 -0.86 0 . 11 0.00 - 1.11 -0.95 -0.91 -0.89 -0.90 -0.93 - 1.10 0 . 10 0.00 - 1.36 - 1.31 - 1.32 - 1.31 - 1 .33 - 1.32 - 1.35 0 . 9 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . B 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 7 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 6 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 5 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 4 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 3 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 2 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . **

AX = 0.106 m

AZ = 0.114 m

Z = 1.361 m

11 Outflow rate = 0.325 kg/s

Inflow rate = 0.287 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

77
Table B-46

Test 541; 1/3 window, 62,9 kW, Icoation C

TEMPERATURE (“^C) *21

20 275.05

19 290.26

18 291.45

17 8.59 291.27 272.54 269.42 268.27 267.43 266.32 260.31 258.98

16 290.39 211.82 254.61 253.98 254.90 249.88 249.49 238.51

15 287.27 26.12 25.34 26.17 25.61 22.53 22.16 24.14

14 7.81 286.93 18.75 19.52 20.00 20.33 19.64 18.86 15.86

13 281.96 13.06 13.49 14.31 12.61 12.58 11.28 11.82

12 271.11 11.97 11.20 11.26 10.80 9.96 9.29 9.36

11 241.40 10.26 10.52 10.44 9.30 9.29 8.85 7.92

10 7.69 192.51 9.90 10.97 11.10 11.00 10.33 9.85 8.22

9 173.53 13.03 16.10 15.96 13.84 13.80 13.66 9.91

9 164.66 9.59 9.52 9.34 9.26 8.77 8.26 7.59

7 159.13 9.90 9.63 9.51 8.51 8.31 8.04 7.28

6 6.81 155.31 9.46 10.63 9.52 9.60 9.40 8.49 7.58

5 150.65 11.58 15.62 12.24 11.53 11.02 10.73 8.30

4 145.54 8.76 8.62 7.99 7;93 7.89 7.65 7.35

3 140.81 8.06 7.96 8.05 7.63 7.54 7.43 7.28

Z * 7.78 134.64 7.98 7.54 7.80 7.69 7.85 7.74 7.52

« VELOCITY

•ft 18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 17 0.00 2.08 1.89 1.85 ' 1.84 1.84 1.88 2.07 0 . 16 0.00 1.23 1.15 1.13 1.11 1.10 1.13 1.28 0 . 15 0.00 -0.55 -0.54 -0.49 -0.46 -0.48 -0.47 -0.50 0 . 14 0.00 - 1.17 - 1.12 - 1.09 - 1.09 - 1.06 - 1.07 - 1.12 0 . 13 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 12 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 11 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 10 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 9 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 8 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 7 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 6 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 5 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 4 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 3 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 2 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 1 ««

0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 .

AX = 0 . 106 m

AZ = 0.114 m

Zn = 1.577 m

Outflow rate = 0.126 kg/s

Inflow rate = 0.108 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00
Table B-47

Test 520; 6/6 door, 31.6 kW, location C

1 TEMPERATURE ( Oc ) »21

20 90.29

19 93.91

19 94.15

17 18.49 94.40 93.07 91.68 91 . 15 90.84 90.99 91.42 91.27

16 94.11 85.49 90.88 88.74 88.94 89.70 90.07 86.79

15 93.31 53.77 87.64 86.04 84.98 84.20 88.98 79.38

14 17.45 91 . 19 51.71 77.45 77.84 80.18 77.38 80.40 69.16

13 76.45 37.21 46.34 45.27 47.60 44.01 47.20 37.12

12 43.88 27.65 33.64 33.23 33.98 29.42 29.39 24.78

11 33.20 21.84 23.61 23.77 21.74 19.99 20.03 21.85

10 17.33 29.69 19.56 19.67 19.51 18.78 18.72 18.37 19.24

9 27.83 18.66 17.96 18.07 17.97 17.89 18.24 19.31

8 26.70 18.41 17.97 17.86 17.76 17.95 18.01 18.92

7 25.99 19.07 18.13 18.33 18.51 18.36 18.20 18.13

6 17.01 25.41 18.72 18.30 18.44 18.40 18.42 18.07 17.99

5 24.70 20.37 18.08 17.97 17.84 17.78 17.84 17.84

4 24.29 20.32 18.68 18.40 18.15 18.10 17.92 18.21

3 23.87 20.43 18.67 18.73 18.82 19.09 19.21 19.23

2 17.53 24.06 19.22 19.04 19.02 19.36 19.71 19.70 19.20

*

Ji VELOCITY ( m/ s )

*lr 18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 17 0.00 1.77 1.68 1.67 1.66 1.69 1.71 1.77 0 . 16 0.00 1.37 1.34 1 .28 1.23 1.25 1 .34 1.41 0 . 15 0.00 1.03 1.06 0.99 0.99 0.99 1.07 1.13 0 . 14 0.00 0.88 0.83 0.81 0.80 0.80 0.84 0.91 0 . 13 0.00 0.52 0.47 0.41 0.41 0.38 0.42 0.41 0 . 12 0.00 0.18 0.26 0.22 0.20 0.16 0.13 0.07 0 . 11 0.00 -0.13 0.09 -0.06 -0. 13 - 0. 16 -0.16 - 0.05 0 . 10 0.00 - 0.28 -0.20 - 0.24 -0.26 - 0.29 -0.33 -0.21 0 . 9 0.00 -0.34 -0.31 -0.30 -0.30 - 0.32 -0.36 -0.32 0 . 9 0.00 -0.43 -0.37 - 0.36 -0.35 -0.38 -0.42 -0.38 0 . 7 0.00 -0.52 -0.43 -0.43 -0.43 - 0.45 -0.51 -0.49 0 . 6 0.00 -0.59 -0.48 -0.46 -0.46 -0.49 -0.56 -0.52 0 . 5 0.00 - 0.57 -0.50 -0.48 -0.48 -0.51 -0.57 - 0.63 0 . 4 0.00 - 0.60 - 0.51 -0.48 -0.50 - 0.53 -0.60 -0.68 0 . 3 0.00 -0.56 -0.54 -0.51 -0.50 - 0.52 -0.61 -0.76 0 . 2 0.00 -0.64 -0.55 -0.52 -0.49 -0.55 -0.63 -0.77 0 . 1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 .

«

AX = 0.106 m

AZ = 0.114 m

Zn = 1.121 m

Outflow rate = 0.396 kg/s

Inflow rate = 0.387 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

79
Table B-48

Test 521; 6/6 door, 105.3 kW, location C

1 TEMPERATURE (°C)

21

20 200.46

19 207.62

18 208.18

17 16.09 208.33 201.35 199.33 200.69 197.96 199.30 196.71 194.34

16 207.29 175.24 195.21 197.48 193.60 189.27 192.17 193.12

15 203.84 99.42 190.34 187.35 184.82 186.13 186.10 182.44

14 13.39 196.56 90.68 158.15 156.16 167.57 168.99 169.26 169.66

13 161.74 80.41 94.82 88.70 99.67 104.71 115.24 88.65

12 88.40 56.00 65.69 65.32 68.42 58.75 57.52 47.12

11 56.87 41.86 46.63 48.48 48.30 36.25 32.33 40.80

10 13.14 46.33 28.93 20.42 26.61 26.77 22.10 17.69 22.33

9 42.58 19.48 15.50 16.72 16.83 15.32 15.57 20.27

8 40.92 18.45 15.25 14.64 14.70 14.44 14.06 15.96

7 39.70 18.86 14.88 15.70 15.93 15.60 15.57 14.00

6 12.29 38.70 17.48 15.64 15.47 15.89 16.06 15.81 13.45

5 36.84 21.46 15.94 15.09 14.80 14.18 13.81 13.22

4 35.49 24.85 16.15 16.03 15 i,64 14.53 14.00 12.80

3 33 . 12 20.93 17.13 17.81 18.27 18.41 18.52 18.03

2 13.99 32.61 19.58 18.92 18.34 19.47 19.15 18.90 17.77

* VELOCITY (a/fi)

18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 17 0.00 2.81 2.78 2.89 ' 2.77 2.78 2.71 2.83 0 . 16 0.00 2.25 2.17 2.13 2.03 2.00 2.12 2.52 0 . 15 0.00 1.63 1.73 1.66 1.65 1.72 1.82 2.28 0 . 14 0.00 1.47 1.41 1.39 1.37 1.38 1.46 1.89 0 . 13 0.00 1.18 1.00 0.92 0.91 0.94 1 .01 1 .08 0 . 12 0.00 0.70 0.63 0.61 0.59 0.56 0.55 0.59 0 . 11 0.00 0.27 0.33 0.37 0.35 0.26 0.22 0.42 0 . 10 0.00 -0.27 -0.28 -0.17 -0.19 -0.26 -0.34 -0.18 0 . 9 0.00 - 0.50 -0.48 -0.42 -0.41 -0.43 -0.48 -0.39 0 . 8 0.00 -0.66 -0.57 -0.55 -0.54 -0.54 -0.57 -0.63 0 . 7 0.00 -0.85 -0.73 -0.67 -0.63 -0.64 -0.74 -0.76 0 . 6 0.00 -0.93 -0.79 -0.74 - 0.72 -0.72 -0.79 -0.93 0 . 5 0.00 - 1.00 -0.88 -0.79 -0.75 -0.78 -0.86 -0.99 0 . 4 0.00 - 0.99 -0.88 -0.81 -0.79 -0.81 -0.90 - 1.12 0 . 3 0.00 - 1 .01 -0.93 -0.83 -0.81 -0.84 -0.94 - 1.21 0 . 2 0.00 - 1.02 -0.88 - 0.84 -0.78 -0.82 -0.92 - 1.21 0 . 1 « 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 .

Ax = 0.,106 m

AZ = 0..114 m

Zn = 1,.021 ra Outflow rate = 0.602 kg/s

Inflow rate = 0.577 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

.00

,00

,00

80
Table B-49

Test 513; 6/6 door, 158 kW, location C

1 TEMPERATURE (°C)

« 21

20 280.09

19 292.41

le 293.67

17 20.04 293.74 273.88 275.77 276.62 264.33 268.85 285.37 286.70

16 292.22 239.13 275.92 270.24 263.47 260.24 276.63 283.43

15 285.94 129.42 259.72 256.54 243.64 249.42 265.92 273.50

14 16.06 275.73 111.53 221.89 212.66 218.63 231.30 243.94 249.27

13 228.14 113.55 144.66 135.27 138.00 140.80 170.04 157.84

12 132.55 83.88 103.36 97.02 96.92 83.66 94.24 75.77

11 84.76 63.79 75.57 78.01 68.15 63.84 64.98 61.55

10 15.66 68.20 41.82 38.94 44.33 47.89 37.87 34.54 32.48

9 62.56 24.47 20.98 22.39 21.01 20.86 21.42 25.19

8 59.80 25.88 19.30 18 i 73 18.49 17.68 18.21 20.70

7 57.90 24.97 19.92 19.53 18.65 19.15 19.43 19. 14

6 14.64 56.45 25.45 19.38 19.36 20.11 19.69 19.78 18.16

5 53.34 30.56 20.26 19.02 17.16 17.62 17.91 17.02

4 51.42 35.39 21 .02 19.84 18.94 18.03 17.88 16.48

3 47.01 27.58 23.79 23.81 21.37 23.00 24.70 26.37

2 16.95 45.20 24.97 25.80 26.04 25.22 24.24 25.68 24.42

VELOCITY

18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 O.OC 0.00

17 0.00 3.42 3.33 3.46 3.35 3.35 3.46 3.63 0.00

16 0.00 2.73 2.64 2.58 2.48 2.48 2.71 3.25 0.00

15 0.00 1.90 2.15 2.03 1.99 2.08 2.33 2.97 0.00

14 0.00 1.62 1.75 1.67 1.66 1.70 1.90 2.38 0.00

13 0.00 1.55 1.34 1.19 1.15 1.17 1.35 1.56 0.00

12 0.00 0.98 0.89 0.83 0.80 0.64 0.84 0.94 0.00

11 0.00 0.50 0.55 0.55 0.50 0.51 0.54 0.57 0.00

10 0.00 - 0.25 -0.08 0.05 0.13 -0.16 -0.20 -0.20 0.00

9 0.00 - 0.57 -0.51 -0.46 -0.45 -0.45 -0.48 -0.51 0.00

8 0.00 - 0.73 -0.65 -0.63 - 0.60 -0.56 -0.62 -0.73 0.00

7 0.00 -0.96 -0.80 -0.77 - 0.71 -0.71 -0.78 -0.96 0.00

6 0.00 - 1 .07 - 0.91 -0.85 - 0.81 -0.79 -0.90 - 1.12 0.00

5 0.00 - 1 . 15 -0.98 -0.92 -0.85 -0.87 -0.97 - 1.22 0.00

4 0.00 -1 . 17 - 1.02 -0.96 -0.91 -0.92 - 1.04 - 1.31 0.00

3 0.00 - 1 . 18 - 1 .06 -0.97 -0.93 -0.96 - 1.09 - 1.39 0.00

2 0.00 - 1.29 - 1 .09 -0.97 -0.94 -0.92 - 1.08 - 1.38 0.00

1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

**

AX = 0.106 m

AZ = 0.114 m

Zn = 0.986 m

Outflow rate = 0.677 kg/s

Inflow rate = 0.636 kg/s

81
Table B-50

Test 160; 6/6 door, 62.9 kW, location AR

TEMPERATURE (°C)

* 21

20 131.88

19 138.40

18 136.38

17 7.11 136.17 132.85 132.01 131.26 130.49 130.48 128.85 131.68

16 135.73 133.89 125.87 120.31 122.37 120.45 121.24 127.33

15 135.25 120.08 124.42 117.75 117.75 116.27 117.77 104.50

14 5.68 134.51 79.93 109.10 98.87 100.83 98.81 102.26 94.10

13 123.10 34.50 57.16 53.97 51.22 55.68 49.07 32.79

12 59. 19 20.96 25.98 30.38 31.04 27.05 21.96 22.20

11 31.89 15.78 19.96 20.47 16.55 12.36 10.41 18.28

10 5.53 25.88 10.77 10.64 11.23 8.69 7.99 8.97 11.57

9 22.86 8.05 8.39 8.16 7.97 7.96 8.14 12.71

8 21.02 7.85 7.27 7.14 7.31 6.87 7.66 9.18

7 19.87 9.37 9.21 9.12 8.89 8.72 6.98 8.60

6 5.17 19.12 9.52 8.64 8.64 8.49 7.67 7.54 7.72

5 18.09 10.17 8.79 8.36 7.43 7.17 6.02 6.98

4 17.43 9.60 8.73 8.65 8.00 6.99 6.55 6.13

3 16.48 7.25 9.56 9.60 9.70 9.61 9.23 8.84

2 6.26 17.64 9.40 9.55 9.91 10.29 9.86 10.23 8.96

VELOCITY ( a/ s )

18 0.00 0.00 0.00 0.00 ' 0.00 0.00 0.00 0.00 0.00

17 0.00 2.61 2.48 2.50 2.53 2.51 2.53 2.67 0.00

16 0.00 1.98 1.87 1.78 1.73 1.75 1.83 1.96 0.00

15 0.00 1.45 1 .44 1.42 1.39 1.40 1.45 1.34 0.00

14 0.00 ' 1.07 1.07 1.09 1.10 1.10 1.07 1.14 0.00

13 0.00 0.71 0.74 0.67 0.61 0.65 0.61 0.57 0.00

12 0.00 0.33 0.40 0.39 0.36 0.31 0.23 0.28 0.00

11 0.00 -0.13 0.17 0.16 0.04 -0.18 -0.24 0.13 0.00

10 0.00 -0.31 -0.30 -0.24 -0.35 -0.35 -0.37 -0.26 0.00

9 0.00 -0.42 -0.40 -0.40 -0.43 - 0.46 -0.52 - 0.20 0.00

8 0.00 -0.52 -0.47 -0.46 -0.52 -0.53 -0.58 -0.52 0.00

7 0.00 -0.61 -0.57 -0.56 -0.58 -0.61 -0.69 -0.44 0.00

6 0.00 - 0.70 -0.61 -0.61 -0.63 -0.66 -0.72 -0.67 0.00

5 0.00 - 0.72 -0.64 -0.62 -0.64 -0.67 -0.76 -0.65 0.00

4 0.00 -0.78 -0.68 -0.64 -0.65 - 0.69 -0.77 -0.93 0.00

3 0.00 -0.81 - 0.71 - 0.67 -0.66 -0.70 -0.80 -0.93 0.00

2 0.00 -0.89 -0.76 -0.71 -0.70 -0.72 -0.82 - 1.03 0.00

1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

«

AX = 0.106 m

AZ = 0.114 m

Z = 1.085 m

Outflow rate = 0.528 kg/s

Inflow rate = 0.516 kg/s

82
Table B-51

Test 163; 6/6 door, 62.9 kW, location BR

I TEMPERATURE (“ q ) 21

20 183.56

19 191.42

18 191.35

17 8.03 189.99 184.34 180.19 181.16 181.80 181.60 181.87 181.07

16 186.69 163.37 174.47 167.60 168.68 162.33 170.12 150.60

15 165.07 83.94 128.06 111.61 91.91 81.14 106.63 103.06

14 6.34 70.35 35.94 53.40 46.34 45.54 45.43 48.95 36.75

13 42.79 33.72 34.35 35.96 36.69 36.54 32.69 29.00

12 34.79 27.45 25.24 27.90 30.27 31.13 29.04 26.78

11 29.66 22.98 19.92 21.64 22.73 23.86 26.09 26.91

10 6.31 26.58 20.44 10.61 11.48 14.17 15.06 13.00 20.47

9 24.93 11.15 9.04 10.04 8.98 8.71 9.58 13.93

B 23.61 12.28 8.14 8.58 8.29 7.79 7.59 10.61

7 22.40 11.40 10.16 9.81 9.17 8.72 8.45 8.92

6 5.77 21.23 11.90 9.46 9.70 9.57 10.08 8.86 8.12

5 19.86 10.29 7.86 7.89 7.40 7.47 7.53 8.23

4 18.97 11.05 8.36 8.01 7.81 7.45 7.14 7.28

3 17.80 10.88 10.53 10.71 10.36 10.21 10.10 10.47

2

* 7.15 18.44 10.91 11.61 11.70 li .53 11.43 11.12 10.33

* VELOCITY ( ra / s )

18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 17 0.00 2^33 2.18 2.18 2.24 2.32 2.36 2.47 0 . 16 0.00 1.86 1 .66 1.58 ^ 1.59 1.59 1.70 1.61 0 . 15 0.00 1.18 1.17 1.11 1.07 1.07 1.16 1.34 0 . 14 0.00 0.81 0.82 0.75 0.73 0.75 0.83 0.96 0 . 13 0.00 0.65 0.61 0.56 0,56 0.59 0.58 0.60 0 . 12 0.00 0.42 0.40 0.41 0.42 0.44 0.43 0.41 0 . 11 0.00 0.15 0.16 0.17 0.17 0.21 0.27 0.31 0 . 10 0.00 -0.19 -0.26 -0.20 -0.19 -0.12 -0.20 0.13 0 . 9 0.00 -0.42 -0.35 -0.30 -0.29 -0.38 -0.40 -0.21 0 . 8 0.00 - 0.46 -0.45 -0.38 -0.38 -0.42 -0.48 -0.40 0 . 7 0.00 - 0.68 - 0.55 -0.50 -0.48 -0.55 -0.62 -0.60 0 . 6 0.00 - 0.69 -0.61 -0.56 -0.55 -0.57 - 0.65 -0.68 0 . 5 0.00 - 0.81 -0.65 -0.60 - 0.58 -0.62 -0.68 -0.78 0 . 4 0.00 - 0.78 -0.69 -0.62 -0.61 -0.63 -0.72 -0.89 0 . 3 0.00 - 0.89 -0.72 -0.66 - 0.64 -0.67 -0.75 - 1.00 0 . 2 0.00 -0.94 -0.74 -0.65 - 0.65 -0.65 - 0.76 - 1.00 0 . 1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 .

*

AX = 0.106 m

AZ = 0.114 m

Z = 1.015 m

nOutflow rate = 0.471 kg/s

Inflow rate = 0.463 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

83
Table B-52

Test 16A; 6/6 door, 62.9 kW, location CR

1 TEMPERATURE ( 0

^)

21

20 155.93

19 161.17

18 161.51

17 8.45 161.49 151.12 153.66 153.40 151.68 152.86 151.76 148.87

16 160.06 132.84 148.84 147.77 149.15 146.21 149.63 146.12

15 154.78 112.92 138.00 133.92 138.96 136.76 138.54 91.21

14 6.70 132.85 52.77 77.35 73.30 85.26 85.43 93.98 84.93

13 57.51 35.79 39.26 38.11 37.90 34.97 36.68 30.39

12 36.67 26.75 29.05 31.28 32.08 28.27 26.52 25.06

1

1

30.17 22.93 21.69 23.21 23.74 19.86 17.64 19.33

10 6.61 26.98 16.73 10.89 12.46 14.53 9.58 10.81 14.65

9 25.32 11.96 8.76 9.05 8.34 8.02 8.37 9.27

B 24.10 9.83 8.17 8.28 8.14 7.52 7.51 8.73

7 22.90 11.04 9.85 9.39 9.45 8.84 8.17 7.52

6 5.97 21.77 10.45 9.50 9.61 9.69 8.51 8.27 7.34

5 20.38 10.55 7.81 7.76 7.61 7.44 7.02 6.78

4 19.40 10.71 8.16 8.11 7.54 7.35 6.84 6.48

3 18.02 9.54 9.87 10.28 10. 12 10.13 9.52 9.45

•» 7.57 17.92 10.08 10.37 11.48 11.13 11.24 10.75 9.63

VELOCITY. (TM/ s )

18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 17 0.00 2.28 2.26 2. 19 2. 18 2.19 2.22 2.34 0 . 16 0.00 1.82 1.72 1.63 1.63 1.61 1.73 2.03 0 . 15 0.00 1.42 1.26 1.27 1.27 1.28 1.38 1.19 0 . 14 0.00 1 .08 0.95 0.88 0.92 0.90 1.02 1.19 0 . 13 0.00 0.65 0.57 0.53 0.53 0.52 0.55 0.65 0 . 12 0.00 0.37 0.37 0.38 0.39 0.36 0.38 0.40 0 . 11 0.00 0.12 0.15 0.15 0.20 0.18 0.13 0.20 0 . 10 0.00 -0.25 -0.25 -0.19 -0.16 -0.28 -0.22 -0.12 0 . 9 0.00 - 0.38 -0.37 -0.32 -0.35 -0.38 -0.41 -0.37 0 . 8 0.00 -0.51 -0.45 -0.43 -0.43 - 0.46 -0.47 -0.49 0 . 7 0.00 -0.65 -0.56 -0.50 -0.50 -0.54 -0.60 -0.67 0 . 6 0.00 -0.73 -0.62 -0.58 -0.57 -0.60 -0.63 - 0.77 0 . 5 0.00 -0.76 - 0.68 -0.61 -0.59 -0.62 -0.70 -0.84 0 . 4 0.00 -0.79 -0.70 -0.63 -0.62 -0.66 -0.72 -0.93 0 . 3 0.00 - 0.82 -0.73 -0.66 -0.65 -0.69 -0.77 -0.98 0 . 2 0.00 -0.90 -0.75 -0.67 -0.65 -0.69 -0.78 - 1.01 0 . 1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . **

AX = 0.106 m

AZ = 0.114 m

Z = 1.035 m

nOutflow rate = 0.485 kg/s

Inflow rate = 0.480 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

84
Table B-53

Test 165; 6/6 door, 62 kW, location DR

TEMPERATURE (^' C ) * 21

20 148.88

19 154.36

18 154.61

17 8.48 154.14 152.40 153.26 151.32 150.06 153.73 153.66 155.04

16 152.88 144.97 144.57 140.70 139.94 138.65 147.27 147.77

15 150.38 127.19 147.79 141.07 125.62 121.98 128.49 120.12

14 6.38 142.60 40.28 90.20 86.63 83.10 73.53 91.57 104.23

13 64.17 27.51 30.11 40.29 40.41 39.13 40.68 33.39

12 38.51 21.99 21 . 14 24.64 33.67 32.41 29.45 28.37

11 31.22 18.52 15.54 20.36 24.05 23. 14 22.45 27.08

10 6.12 27.45 13.48 10.78 12.95 15.93 13.49 12.89 22.57

9 25.17 10.29 9.56 9.34 9.14 7.88 10.07 16.41

8 23.16 9.41 8.52 8.34 7.50 7.70 8.38 13.11

7 21.46 10.89 10.04 9.37 9.31 8.70 7.64 10.93

6 5.66 20.24 10.58 10.34 9.91 9.51 9.08 7.58 9.28

5 19.17 9.48 8.09 7.66 7.60 7.12 7.24 9.24

4 18.37 9.70 8.41 8.11 7.42 7.38 6.92 7.15

3 17.30 9.09 10.22 10.33 10.39 9.98 10.05 10.80

2 7.19 18.32 9.80 10.96 11.51 ' 11.18 11.33 11.35 10.56

VELOCITY

18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 17 0.00 2.40 2.26 2.17 2.21 2.28 2.40 2.47 0 . 16 0.00 1.91 1.83 1.75 1.65 1.62 1.75 1.85 0 . 15 0.00 1.42 1.41 1.30 1.26 1.30 1.32 1.42 0 . 14 0.00 0.75 0.75 0.82 0.92 0.88 0.96 1.25 0 . 13 0.00 0.49 0.56 0.61 0.58 0.54 0.56 0.61 0 . 12 0.00 0.21 0.24 0.35 0.42 0.40 0.37 0.37 0 . 11 0.00 - 0.15 -0.08 0.24 0.23 0.20 0.20 0.25 0 . 10 0.00 - 0.31 -0.28 -0.18 -0.10 -0.16 -0.23 0.16 0 . 9 0.00 -0.39 -0.34 -0.33 -0.32 - 0.40 -0.45 -0.13 0 . 8 0.00 -0.48 -0.43 -0.41 -0.46 - 0.48 - 0.55 -0.26 0 . 7 0.00 -0.61 -0.52 -0.52 -0.51 -0.55 -0.67 -0.38 0 . 6 0.00 - 0.68 -0.58 -0 . 55 -0.57 - 0.61 -0.71 -0.54 0 . 5 0.00 - 0.75 -0.63 - 0.61 -0.60 - 0.63 -0.75 -0.67 0 . 4 0.00 - 0.79 -0.67 -0.60 -0.63 -0.65 - 0.77 - 0.91 0 . 3 0.00 - 0.86 -0.71 - 0.66 - 0.63 -0.69 -0.80 - 1.01 0 . 2 0.00 -0.90 - 0.74 -0.65 -0.67 - 0.70 -0.80 - 1.04 0 . 1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 .

•»

Ax = 0.106 m

AZ = 0.114 m

Zn = 1.034 m

Outflow rate = 0.485 kg/s

Inflow rate = C.470 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

85
Table B-5A

Test 162; 6/6 door, 62.9 kW, location ER

I TEMPERATURE (°C)

*21

20 160.94

19 155.92

18 150.13

17 7.42 146.15 150.42 146.77 144.93 145.04 146.49 147.56 143.56

16 141.42 141.76 143.29 135.96 133.63 136.42 139.82 137.86

15 137.99 129.49 126.97 117.55 123.20 140.02 143.83 97.81

14 5.71 129.92 66.46 94.27 83.19 83.72 85.01 100.87 65.42

13 81.64 33.84 40.39 39.64 41.54 33.39 27.34 26.37

12 38.56 27.44 29.83 30.56 27.30 20.16 18.46 22.01

11 27.56 22.67 23.95 19.12 16.21 10.90 11.78 19.14

10 5.58 22.91 14.27 13.99 12.30 8.66 8.42 8.64 13.98

9 21.60 10.19 8.80 7.51 7.90 7.19 7.77 11.80

8 21.04 8.80 7.52 7.33 6.91 6.71 7.14 9.55

7 20.68 12.89 10.17 9.58 10.41 8.83 8.46 7.73

6 5.25 20.39 12.36 10.05 9.86 9.36 9.00 8.01 8.00

5 19.49 11.36 7.57 6.71 7.12 6.58 6.67 7.31

4 19.25 10.85 7.63 7.57 7.02 6.76 6.59 6.83

3 18.60 9.16 9.87 9.58 9.77 9.55 9.05 8.48

2 « 6.33 20.30 9.86 9.89 10.36 10.10 9.91 10.44 8.73

VELOCITY (m/s)

18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . 17 0.00 2.48 2.44 2.35 2.27 2.37 2.48 2.82 0 . 16 0.00 1.93 1.77 1.68 1.72 1.83 1.85 2.01 0 . 15 0.00 1.48 1.31 1.31 1.30 1.44 1.50 1.32 0 . 14 0.00 1.15 1.02 0.98 0.96 0.93 1.02 1.02 0 . 13 0.00 0.68 0.62 0.59 0.61 0.55 0.51 0.50 0 . 12 0.00 0.44 0.44 0.43 0.38 0.25 0.21 0.27 0 . 11 0.00 0.21 0.25 0.17 0.06 -0.20 -0.20 0.21 0 . 10 0.00 -0.20 -0.16 -0.20 -0.32 -0.34 -0.35 -0.15 0 . 9 0.00 -0.36 -0.33 -0.37 -0.36 -0.42 -0.43 - 0.29 0 . 8 0.00 -0.50 -0.43 -0.43 -0.47 -0.48 -0.52 -0.45 0 . 7 0.00 -0.59 -0.55 -0.54 -0.54 -0.59 -0.63 -0.54 0 . 6 0.00 -0.69 -0.59 -0.59 -0.62 -0.65 -0.70 -0.63 0 . 5 0.00 - 0.68 -0.61 -0.62 -0.60 -0.66 -0.71 -0.77 0 . 4 0.00 -0.73 -0.65 -0.61 -0.62 -0.68 -0.75 - 0.88 0 . 3 0.00 -0.76 -0.69 -0.65 -0.63 -0.70 -0.76 -0.96 0 . 2 0.00 -0.86 -0.72 -0.66 -0.67 -0.69 -0.77 - 0.96 0 . 1 »

M.

0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 .

AX = 0.106 m

AZ = 0.114 m

Z = 1.063 m

nOutflow rate = 0.507 kg/s

Inflow rate = 0.486 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

86
Table B-55

Test 167; door, 62.9 kW, location FR

TEMPERATURE (° c ) *

21

20 127.44

19 128.65

18 129.12

17 8.88 128.94 130.13 l

'26.91 127.35 128.53 126.41 126.59 127.83

16 123.00 127.09 121.73 118.18 119.16 117.28 120.00 123.89

15 129.27 120.77 117.29 113.46 115.08 108.53 111.99 119.24

14 6.78 128.79 74.97 111.88 104.94 105.51 99.54 104.67 108.53

13 129.41 54.25 85.47 83.20 80.96 72. 18 71.78 69.32

12 115.14 28.19 38.03 47.55 47.39 43.63 38.61 33.60

11 51.55 20.05 18.91 24.77 25.92 19.53 13.66 21.99

10 6.53 35.39 15.33 11.72 13.83 11.89 10. 15 9.07 14.79

9 29.96 11.34 9.99 3.62 9.38 8.82 9.15 12.48

8 26.63 10.80 9.21 8.68 8.48 8.04 8.58 10.48

7 24.08 12.04 10.48 10.06 9.69 9.40 8.35 8.56

6 6.05 22.28 11.83 10.47 10.02 9.85 8.97 7.73 8.63

5 20.51 13.59 9.21 8.58 8.13 8.21 7.61 7.97

4 13.20 12.56 9.85 8.95 8.46 7.79 7. 18 6.98

3 18.36 9.53 11.32 10.82 10.81 10.71 10.55 10.41

2 7.59 19.90 10.67 11.86 11.47 11.54 11.44 11.43 10.53

* VELOCITY

18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

17 0.00 2.58 2.43 2.43 2.42 2.41 2.48 2.63 0.00

16 0.00 1.98 1 .77 1.69 1.66 1.67 1.74 1.93 0.00

15 0.00 1.58 1.44 1.41 1.40 1.37 1.44 1.55 0.00

14 0.00 1.05 1.11 1.17 1 . 15 1.11 1.14 1.37 0.00

13 0.00 0.83 0.90 0.88 0 = 82 0.77 0.78 0.93 0.00

12 0.00 0.32 0.44 0.51 0.46 0.44 0.43 0.45 0.00

11 0.00 -0.16 -0.04 0.18 0.21 -0.01 -0.17 0.18 0.00

10 0.00 -0.35 -0.34 -0.26 -0.31 -0.34 -0.44 -0.16 0.00

9 0.00 - 0.47 -0.40 -0.38 -0.41 -0.46 -0.50 -0.43 0.00

a 0.00 - 0.55 -0.50 -0.49 -0.50 -0.52 - 0.60 -0.54 0.00

7 0.00 -0.68 -0.59 -0.57 -0.59 -0.62 -0.68 -0.66 0.00

6 0.00 -0.74 -0.65 -0.63 -0.64 -0.66 -0.76 -0.69 0.00

5 0.00 -0.74 -0.69 -0.65 -0.65 - 0.68 -0.76 -0.83 0.00

4 0.00 -0.78 -0.71 -0.65 -0.66 -0.70 -0.81 -0.97 0.00

3 0.00 - 0.80 -0.75 -0.68 -0.69 - 0.73 -0.82 - 1.05 0.00

2 0.00 -0.94 -0.77 -0.71 -0.71 -0.75 -0.86 - 1.07 0.00

1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

«

AX = 0.106 m

AZ = 0.114 m

Z = 1.076 m

nOutflow rate = 0.549 kg/s

Inflow rate = 0.532 kg/s

87
Table B-56

Test 161; 6/6 door, 62.9 kW, location GR

TEMPERATURE (° C ) *

21

20 116.41

19 117.33

18 116.96

17 7.97 116.98 117.55 114.19 113.54 116.86 116.56 115.54 114.07

16 117.10 114.14 111.40 109.83 108.16 109.53 111.39 108.17

15 117.29 111.20 109.28 102.97 105.60 105.64 111.34 88.66

14 6.47 117.07 70.41 106.11 99.72 95.79 97.96 107. 18 73.27

13 115.33 72.76 86.32 82.24 83.73 79.85 85.80 67.83

12 104.35 35.27 46.25 64.56 63.46 51.97 42.19 34.32

11 70.01 25.71 34.39 39.20 37.39 23.94 14.74 24.77

10 6.31 44.73 17.36 16.36 18.77 19.59 14.45 11.38 16.52

9 35.81 10.78 10.97 10.91 11.77 11.55 11.12 14.68

9 31.20 11.17 10.13 10.69 11.48 11.56 10.82 13.02

7 26.23 17.36 18.12 17.22 18.84 16.98 10.70 9.63

6 5.90 26.72 17.92 17.10 18.57 19.25 17.46 10.11 8.98

5 25.42 10.51 9.06 9.68 11.88 12.38 9.92 9.91

4 24.83 9.24 8.13 8.86 9.77 9.57 7.61 7.37

3 23.96 8.15 8.71 7.88 8.61 9.11 8.68 9.95

2

« 7.07 25.27 9.64 8.92 8.48 8.83 9.06 9.50 8.73

VELOCITY % 18 0.00 0.00 0.00 6.00 0.00 0.00 0.00 0.00 0 . 17 0.00 2.61 2.50 2.48 2.47 2.52 2.56 2.68 0 . 16 0.00 2.03 1.90 1 .80 1.75 1.78 1.87 2.00 0 . 15 0.00 1.72 1.53 1.46 1.46 1.46 1.56 1.40 0 . 14 0.00 1.12 1.22 1.20 1.16 1.18 1.25 0.91 0 . 13 0.00 1.18 1.02 0.96 0.93 0.89 0.95 0.98 0 . 12 0.00 0.49 0.63 0.69 0.63 0.51 0.44 0.43 0 . 11 0.00 0.15 0.32 0.33 0.24 -0.14 -0.28 0.13 0 . 10 0.00 -0.36 -0.34 -0.30 -0.32 -0.38 -0.48 -0.24 0 . 9 0.00 -0.50 -0.48 -0.48 - 0.48 -0.50 -0.58 -0.44 0 . 8 0.00 -0.60 -0.56 -0.54 -0.53 -0.55 -0.67 -0.60 0 . 7 0.00 -0.75 -0.67 -0.63 -0.63 -0.65 -0.78 -0.78 0 . 6 0.00 - 0.85 -0.69 -0.66 -0.62 -0.65 -0.84 -0.85 0 . 5 0.00 -0.89 -0.73 -0 . G4 -0.62 -0.67 -0.84 - 1.02 0 . 4 0.00 -0.95 -0.66 -0.46 -0.42 -0.48 -0.81 - 1.08 0 . 3 0.00 - 1.02 -0.75 -0.57 -0.54 -0.52 -0.83 - 1.19 0 . 2 0.00 - 1.09 -0.80 -0.75 -0.71 -0.67 -0.87 - 1.21 0 . 1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0 . **

AX = 0.106 m

AZ = 1.062 in Z = 1.062 m

nOutflow rate = 0.601 kg/s

Inflow rate = 0.550 kg/s

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

00

88
Table B-57

Test 166, 6/6 door, 62.9 kW, location HR

TEMPERATURE ( Oq

) 21

20 144.96

19 151.19

18 151.65

17 9.07 151.52 136.82 142.13 146.15 147.23 145.11 144.41 146.95

16 150.87 133.85 137.89 137.99 137.02 137.80 140.47 127.30

15 149.42 125.32 129.50 128.42 122.60 115.36 117.73 109.94

14 7.19 148.08 86.21 113.43 99.36 91.36 85.70 86.85 92.85

13 115.72 43.31 61.03 55.14 47.49 48.62 46.78 45.24

12 46.36 27. 15 30.91 29.30 28.30 26.45 23.23 23.70

11 29.03 19.77 20.78 17.53 17.31 13.00 13.09 18.79

10 7.01 23.69 13.89 13.58 13.20 11.29 10.60 10.57 14.52

9 20.62 10.50 10.32 9.70 9.53 9.39 9.70 12.66

8 19.14 10.25 9.39 9.55 8.86 9.08 9.29 10.90

7 18.19 10.70 11.08 10.29 10.84 9.92 8.91 9.54

6 6.51 17.52 11.31 11.32 11.31 10.61 10.15 9.10 9.41

5 16.82 10.27 9.25 8.74 8.79 8.20 8.17 8.47

4 16.41 11.32 9.38 9.22 8.79 8.65 8.05 7.59

3 15.79 9.65 11.23 11.42 11.92 11.18 11.24 10.60

2 7.92 16.66 10.44 11.59 12.89 12.94 12.65 12.69 11.27

* VELOCITY

18 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

17 0.00 2.39 2.25 2.26 ' 2.15 2.19 2.25 2.34 0.00

16 0.00 2.00 1.80 1.69 1.64 1.67 1.73 1.68 0.00

15 0.00 1.62 1.47 1.47 1.40 1.35 1.33 1.44 0.00

14 0.00 1.15 1.11 0.98 0.96 0.99 1.04 1.22 0.00

13 0.00 0.66 0.64 0.58 0.54 0.57 0.55 0.59 0.00

12 0.00 0.34 0.34 0.29 0.25 0.25 0.16 0.25 0.00

11 0.00 0.06 0.16 -0.09 -0.06 -0.21 -0.21 0.09 0.00

10 0.00 -0.28 - 0.21 -0.22 -0.27 -0.33 -0.36 -0.10 0.00

9 0.00 - 0.43 -0.34 - 0.38 -0.36 -0.42 -0.46 -0.27 0.00

8 0.00 - 0.53 -0.44 -0.41 -0.43 -0.47 -0.50 -0.43 0.00

7 0.00 -0.67 -0.54 -0.54 -0.51 -0.56 - 0.62 -0.47 0.00

6 0.00 - 0.72 -0.59 - 0.56 -0.55 -0.61 -0.67 -0.55 0.00

5 0.00 - 0.76 -0.62 -0.61 -0.58 -0.64 -0.70 -0.71 0.00

4 0.00 - 0.78 -0.65 -0.61 -0.60 -0.64 -0.72 -0.85 0.00

3 0.00 - 0.82 -0.69 -0.65 -0.64 -0.69 -0.75 -0.93 0.00

2 0.00 - 0.30 -0.74 -0.67 -0.65 -0.67 -0.76 -0.96 0.00

1 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

«*

AX = 0.106 m

AZ = 0.114 tn

• Zn = lvG92' m Outflow rate = 0.485 kg/s

Inflow rate = 0.482 Kg/s

89
APPENDIX C. RADIATION ERROR ASSOCIATED WITH OPENING

GAS TEMPERATURE MEASUREMENTS

Since raost of the air flowing into the room must be at ambient temperature (T^), differences between the temperatures of thermocouples in the inflow

(Tti) and T^ establish the radiation error for these thermocouples and also

provide a means for estimating the error associated with the hot-gas temperatures measured by the thermocouples in the outflow region of the opening.

Although each opening thermocouple was partially shielded from the fire and

hot room by the velocity probe to which it was attached, the shielding

probably varied slightly from probe to probe. In the following analysis,

error bounds on the outflow thermocouple measurements will be estimated from

the known error associated with the inflow thermocouples by assuming that the

outflow thermocouples (a) were shielded from the fire and heated room to the

same extent as the inflow thermocouples, and (b) were completely shielded from

the fire and heated room.

The radiation incident upon the inflow-region thermocouples (q") is given

by the expression

q" = (h^/a)(T^^ - TJ + (eo/a)T^^ (C-1)

where e is the emissivity of the thermocouple bead, a is the absorbtlvity , and

h^ is the forced convection heat transfer coefficient for a sphere given by

1 . Cl* the expression

Superscripts in text refer to references at the end of this appendix.

90
h = (k/d)(2 + 0.37 Re®*^ Pr®*^^) (C-2)

where Re = pvd/u

Pr = uc/k

V is the gas velocity

p is the gas density

k is the gas thermal conductivity

c is the gas specific heat

u is the gas viscosity, and

d is the diameter of the thermocouple bead.

If it is assumed that the radiation incident upon the outflow thermocouples from the flame, gas, and surfaces within the heated room is equal to

q" , then the energy balance for any of these thermocouples is

where the second term on the left accounts for radiation from the hot gas

plume outside the opening.

q" + 0.5 aae + h (T - T ) = eoT^ ^ o u o to to

(C-3)

T is the actual outflow gas temperature.

is the temperature of the thermocouple in the outflow to

e e CO+ e o

2

the emmissivity of the opening plume.
e_ = 0,7 (Xp A)^*^/(T /lOO)^*^, the emmlssivity of the

LO2 ^^2

C2 carbon dioxide component ,

e„ - = 7.0 (Xj, -A)^*^/(Tu/100) , the emissivity of the

C2 water component ,

X is the mole fraction of the species

>

I is the mean beam length of the opening plume,

is the average temperature of the upper gas layer, and

h^ is given by Eq, C-2 evaluated at T^.^,

On the other hand, the outflow thermocouples might have been better shielded

from the hot environment than their inflow counterparts. In the limit of

complete shielding, radiant heat transfer from the junction is maximized and

the energy balance becomes

h (T - ) + aoT^ = eoT^

o to <» to

(C-4)

Solving Eqs, C-3 and C-4 for the difference between the actual and measured

gas temperatures (T - Tj.^) produces error bounds for the upper-region

thermocouple results.

(eoT^ - aq" - 0.5 aae^/)/h^ < (T - T. ) < (a/h^)(eT^^ - alS (C-5)

to o u o to o to *

92
The corrections listed in Table B-2 (Appendix B) are the maximum values

calculated with Eq. C-5 using a wide range of experimental results for T^,

'^oo» "^u* ^ values based on the complete combustion of pure methane,

A=lm, a=e=0,5, and a=e=1.0.

References

Cl. Eckert, E.R.G. and Drake, R.M. , Heat and Mass Transfer, New York, McGraw

Hill, 1959.

C2. Schack, A., Arch. Eisen Huttenwesen, 241 (1939).

93
NBS»114A (REV. 2*80

U.S. DEPT. OF COMM.

BIBLIOGRAPHIC DATA

SHEET (See instructions)

PUBLICATION OR

REPORT NO.

NBSIR 82-2520

2. Performing Organ. Report No. 3. Publication Date July 1982

4. TITLE AND SUBTITLE

Flow Induced by Fire in a Compartment

5. AUTHOR(S)

K.D. Steckler, J.G. Quintiere and W.J. Rinkinen

6. PERFORMING ORGANIZATION (If joint or other than NBS, see instructions)

national bureau of standards

DEPARTMENT OF COMMERCE

WASHINGTON, D.C. 20234

7. Contract/Grant No.

S. Type of Report & Period Covered

9. SPONSORING ORGANIZATION NAME AND COMPLETE ADDRESS (Street, City, State, ZIP)

10.

SUPPLEMENTARY NOTES

Document describes a computer program; SF-185, FIPS Software Summary, is attached.

11.

ABSTRACT (A 200-word or less factual summary of most significant information. If document includes a significant

bi bliography or literature survey, mention it here)

Fifty-five full-scale steady-state experiments were conducted to study the flow

induced by a simulated pool fire in a compartment under conditions characteristic

of the developing fire. The mass flow rate through the door or window opening

and bounds on the fire plume entrainment rate are presented as a function of

opening geometry, fire strength, and fire location.

The characteristics of the measured opening flow rates are explained by a simple hydrostatic model based on temperature distribution. A good correlation

between the measured results and the idealized flows, taking into account the

complete temperature distribution, is demonstrated.

Entrainment results for fires near walls are in reasonable agreement with results

from free-standing plume models. Except for the smallest openings, fires in

other locations entrain at a rate two to three times the rate predicted by these

models. This phenomenon is attributed to room disturbances caused by the opening

flow and is similar to the behavior of a fire plume in a cross wind.

12.

KEY WORDS (Six to twelve entries; alphabetical order; capitalize only proper names; and separate key words by semicolons)

air flows; compartment fires; entrainment; flow rates; fire plumes; opening flows

13. AVAILABILITY 14. NO. OF

PRINTED PAGES

Unlimited

1 1 For Official Distribution. Do Not Release to NTIS 101

1 1 Order From Superintendent of Documents, U.S. Government Printing Office, Washington, D.C.

20402. 15. Price

Order From National Technical Information Service (NTIS), Springfield, VA. 22161 $12.00

USCOMM-DC 9043-PBO