+ All Categories
Home > Documents > Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib...

Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib...

Date post: 30-Mar-2020
Category:
Upload: others
View: 2 times
Download: 0 times
Share this document with a friend
33
NATIONAL AERONAUTICS AND SPACE ADMINISTRATION Technical Memorandum 33-655 Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING SQUIB IGNITION TIMES (Jet Propulsion Lab.) CSCL 20M Unclas G3/33 30000 REPRODUCED BY U.S. DEPARTMENT OF COMMERCE NATIONAL TECHNICAL INFORMATION SERVICE SPRINGFIELD, VA 22161 JET PROPULSION LABORATORY CALIFORNIA INSTITUTE OF TECHNOLOGY PASADENA, CALIFORNIA January 15, 1974 https://ntrs.nasa.gov/search.jsp?R=19740009527 2020-04-07T22:55:03+00:00Z
Transcript
Page 1: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

NATIONAL AERONAUTICS AND SPACE ADMINISTRATION

Technical Memorandum 33-655

Heat Transfer Model for Predicting

Squib Ignition Times

V. Sernas

(ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760

PREDICTING SQUIB IGNITION TIMES (Jet

Propulsion Lab.) CSCL 20M UnclasG3/33 30000

REPRODUCED BYU.S. DEPARTMENT OF COMMERCE

NATIONAL TECHNICALINFORMATION SERVICESPRINGFIELD, VA 22161

JET PROPULSION LABORATORY

CALIFORNIA INSTITUTE OF TECHNOLOGY

PASADENA, CALIFORNIA

January 15, 1974

https://ntrs.nasa.gov/search.jsp?R=19740009527 2020-04-07T22:55:03+00:00Z

Page 2: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

N74-17640

NATIONAL AERONAUTICS AND SPACE ADMINISTRATION

Technical Memorandum 33-655

Heat Transfer Model for Predicting

Squib Ignition Times

V. Sernas

JET PROPULSION LABORATORY

CALIFORNIA INSTITUTE OF TECHNOLOGY

PASADENA, CALIFORNIA

January 15, 1974

REPRODUCED BYNATIONAL TECHNICALINFORMATION SERVICE

U.S. DEPARTMENT OF COMMERCESPRINGFIELD., VA. 22161

J4

Page 3: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

Prepared Under Contract No. NAS 7-100National Aeronautics and Space Administration

/

Page 4: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

PREFACE

The work described in this report was performed by the Propulsion

Division of the Jet Propulsion Laboratory.

JPL Technical Memorandum 33-655 Preceding page blank

Page 5: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

CONTENTS

I. Introduction ................................... 1

II. The Bridgewire - Pyrotechnic System . . . . . . . . . . . . . . . . 1

III. The Computer Model .......................... 2

IV. Thermal Property Estimates ....................... 4

V. Results ........................... ........... 5

A. Temperature Results ................... ...... 6

B. Energy Results ............................ 7

C. Axial Temperature Distribution ................. 7

D. Program Deficiencies ........................ 8

VI. Conclusions ......................... .......... 9

References ... ..... . . . . . . . . . . . . . . . . . . . . . . . ............... 9

TABLE

1. MM'71 firing data comparison ................. 11

FIGURES

1. Cutaway view of JPL squib .................... 12

2. The bridgewire - pyrotechnic - alumina system;axial heat conduction is neglected. .......... ... . 13

3. The bridgewire - pyrotechnic system; axial heatconduction is neglected ...................... .. 14

4. The bridgewire - pyrotechnic system of Fig. 3showing division into twenty nodes of variable mass . . . 15

5. Node 3 temperature at the bridgewire - pyrotechnicinterface . ......... ... . .. . . . . . . . ... . . . . . 16

6. Radial temperature distribution within thebridgewire - pyrotechnic system ................ 17

7. Instantaneous radial heat flux and instantaneoustemperature of bridgewire and node 3 . ........... . 18

8. Temperature history of node 3 for initial squibtemperatures of 144.25 K, 294.3 K, and 366.48 K ..... 19

JPL Technical Memorandum 33-655 Preceding page blankJPL Technical Memorandum 33-655 Prceigaelv

Page 6: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

9. Temperature history of node 2 for initial squibtemperatures of 144. 25 K, 294. 3 K, and366.48 K ... ......... .... ................ 20

10. Temperature history of nodes 2 and 3 during aconstant current pulse of 3. 5 A for 1 ms ...... . . . . 21

11. Energy delivered to the bridgewire and pyrotechnic:T AM B = 294. 3K K .......................... 22

12. Energy delivered to the bridgewire and pyrotechnic:T AM B = 144.25 K ..... ............ ... ..... . 23

13. Division of the two-dimensional bridgewire - pyrotechnicsystem into nodes; the bridgewire is divided axially into10 nodes, the pyrotechnic into 25 nodes, and the pin into2 nodes . ... ..... .. .... .......... . .. . . .24

14. Axial bridgewire temperature distribution; thebridgewire is embedded in the pyrotechnic . .... ...... 25

15. Axial temperature distribution within the barebridgewire (burnwire) ....................... 26

vi JPL Technical Memorandum 33-655

Page 7: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

ABSTRACT

This memorandum describes a squib ignition model based on transient

heat conduction from the hot bridgewire to the pyrotechnic. No Arrhenius-

type chemical reaction is included. Instead, a thermal contact resistance

is postulated to exist between the hot bridgewire and the pyrotechnic.

Ignition is assumed to occur when a 2. 5-tm layer of pyrotechnic next to the

bridgewire reaches a characteristic ignition temperature for that

pyrotechnic.

This model was applied to the JPL squib, which uses a 50-[pm

(0. 002-in.) diameter Tophet A bridgewire to ignite a boron, potassium

perchlorate mix. A computer program was utilized that solves the tran-

sient heat condition problem with the boundary conditions stipulated by the

model. The thermal contact conductance at the interface was determined by

trial and error so that the experimentally determined ignition time for one

firing condition would be properly predicted by the model. This matching

test was a 3. 5-A constant current firing at 21*C for which the thermal con-

tact conductance value was found to be 31, 200 W/m2 - K (5,500 BTU/

h-ft 2 -°F). With this value of the thermal contact conductance, ignition

times for other test conditions were predicted and compared with experi-

mental data. The agreement was quite good for tests run between -129 C

and +93. 3*C at current levels of 3. 5 and 5 A. The resultant radial

temperature profiles within the bridgewire - pyrotechnic system are pre-

sented for a few test conditions. Axial heat conduction along the bridgewire

is shown to be negligible.

JPL Technical Memorandum 33-655 vii

Page 8: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

I. INTRODUCTION

The phenomenon of pyrotechnic ignition has been modeled with various

degrees of success by many investigators (Refs. 1 to 6). Some of these

models were computer simulations (Refs. 4 and 6), while others were par-

tially analytical models. This study is based on a computer model that dif-

fers from the previous studies in the way the heat transfer between the

bridgewire and the pyrotechnic is handled. A finite thermal contact

conductance is assumed to exist at this interface in the same way that it has

been shown (Ref. 7) to exist at other solid-to-solid interfaces. It has been

the objective of this study to reexamine the ignition process as it applies to

JPL squibs and to formulate a heat transfer model of the bridgewire -

pyrotechnic system. This model had to predict the time to ignition for low

current level squib firings at ambient temperatures from 144. 3 K to 366. 5 K

(-200 F to +200*F).

II. THE BRIDGEWIRE - PYROTECHNIC SYSTEM

Since the pyrotechnic ignition occurs next to the bridgewire, one needs

to look at only that portion of the total squib that is in contact with the

bridgewire and that can receive heat from the bridgewire. During the very

short period of time that the firing current passes through the bridgewire,

heat is generated within the bridgewire. Some of this heat is conducted into

the Inconel pins (see Fig. 1), some into the alumina header, but most of the

heat leaving the bridgewire is conducted to the pyrotechnic. It will be shown

that only a small portion of the total heat generated within the bridgewire is

conducted out, and that the majority of the generated heat goes into heating

up the bridgewire. If axial conduction of heat to the pins is neglected within

the bridgewire, the bridgewire should be at the same temperature along its

JPL Technical Memorandum 33-655

Page 9: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

length. (It will be shown in Subsection V-C that axial conduction is indeed

negligible. ) Thus we should be concerned only with a unit length of

bridgewire surrounded with a concentric shell of pyrotechnic and alumina as

shown in Fig. 2. The outer radius of the pyrotechnic mass should be the

distance to which heat diffuses during the time that the bridgewire is heated.

For ignition times of less than 2 ms and a pyrotechnic diffusivity of

0.518 X 10-6 m2/s (0.02 ft2/h) this distance amounts to about 5 bridgewire

radii (Ref. 8, p. 337).

In the alumina header the heat penetration distance is difficult to

estimate because a round bridgewire can make, at best, only a line contact

with the alumina. Since the thermal diffusivity of the alumina is very large,

the actual amount of alumina that has to be included within the system may

be considerable.

The presence of the alumina makes the heat flow from the bridgewire

two-dimensional. In other words, the quantity of heat flowing out of the top

of the bridgewire is not the same as that flowing out of the bottom. There is

evidence that the bridgewire lifts off the alumina while being welded to the

pins. When the loose pyrotechnic powder is dropped in over the bridgewire,

it is possible that a portion of the bridgewire is totally surrounded with

pyrotechnic and that the bridgewire would make no contact with the alumina

header. When the bridgewire is lifted off the alumina by a distance I or

greater, the bridgewire - pyrotechnic system becomes the one shown in

Fig. 3. It is this system that will be considered in the remainder of this

report. The heat flow in this system is one dimensional. The heat

generated in the bridgewire flows radially out into the pyrotechnic and con-

tinues to flow radially through the pyrotechnic.

III. THE COMPUTER MODEL

The temperature distributions in the bridgewire - pyrotechnic system

shown in Fig. 3 were simulated on the Univac 1108 computer using a library

transient heat conduction program called HEAT. The system was broken up

into twenty nodes, each representing a concentric shell of mass. Figure 4

shows a typical pie-shaped section of the bridgewire - pyrotechnic system

2 JPL Technical Memorandum 33-655

Page 10: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

and how it was divided into nodes. The bridgewire was broken up into two

nodes of equal mass, and the pyrotechnic was broken up into seventeen

nodes of varying mass. Nodes 12 through 19 that are not shown in Fig. 4

were made of shells 1. 016 X 10-3-cm (4 x 10-4-in. ) thick. The twentieth

node was a heat sink kept at the ambient temperature. As shown in Fig. 4,

node 3 is the pyrotechnic node that is in contact with the bridgewire. It is

this node that becomes the hottest and reaches ignition temperature first.-4

The thickness of node 3 was chosen as 2. 5 im (10 in. ).

It is assumed that there is one characteristic ignition temperature for

a particular pyrotechnic mix. Furthermore, it is assumed that once a

2. 5-p m- (1 x 10 - 4 -in. -) thick layer of the pyrotechnic reaches this ignition

temperature, a self-sustaining exothermic reaction will commence in the

pyrotechnic (i. e., the pyrotechnic will ignite).

Each node of the computer program must be supplied with a heat

capacity. A thermal conductance between adjacent nodes must also be

specified. The thermal capacity of a node is its mass times its specific

heat. The thermal conductance between two nodes is defined as kA/Ar

where k is the thermal conductivity of the solid making up the two nodes, A

is the average cross-sectional area normal to a line joining the two nodes,

and Ar is the distance between the two nodes. Thus it is necessary to know

the following thermal properties both for the bridgewire and the

pyrotechnic:

(1) Density.

(2) Specific heat and its variation with temperature.

(3) Thermal conductivity and its variation with temperature.

In addition, the thermal contact conductance, h, at the bridgewire -

pyrotechnic interface must be known in order that the conductance between

node 2 and node 3 in Fig. 4 can be specified. The thermal conductance

between nodes 2 and 3 is defined as hA c where A is the area of contact

between the bridgewire and the pyrotechnic. If the thermal contact con-

ductance were infinite, nodes 2 and 3 would be at the same temperature, but

when h is finite (as it always is for two solids in contact with each other)

there is a discontinuity in temperature across the interface.

JPL Technical Memorandum 33-655 3

Page 11: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

IV. THERMAL PROPERTY ESTIMATES

As it has been mentioned above, a total of eight thermal properties or

parameters are required to make this simplified, one-dimensional model

work. Of these eight, only four are reasonably well known for the JPL squib

at room temperature. These are:

(1) Density of Tophet A = 8. 4 g/cm 3

(2) Specific heat of Tophet A = 0. 447 J/g-K at 293. 15 K

(0. 107 cal/gm-°C at 20 C).

(3) Thermal conductivity of Tophet A = 0. 134 W/cm-oC.

(4) Density of B-KC104-Viton pyrotechnic = 1. 95 g/cm 3

However, no specific information is available on the variation of these

properties with temperature.

The remaining four properties are (1) specific heat of pyrotechnic,

(2) thermal conductivity of pyrotechnic, (3) ignition temperature of pyro-

technic, and (4) thermal contact conductance.

The specific heat of the pyrotechnic was estimated from the specific

heat of each component as a percentage of the total weight. The value

arrived at was 0. 84J/g-K(0.2 cal/gm-oC). The accuracy of this estimate is

suspect. Furthermore, any phase changes that may be present in the Viton

binder at temperatures below the ignition temperature could change the

effective specific heat of the pyrotechnic at elevated temperatures.

The thermal conductivity of the pyrotechnic has never been measured.

It was estimated from "no-fire" Bruceton tests to be 0. 882 W/m- K

(0. 51 BTU/h-ft- F). This estimate was based on the experimental fact that

a current of 1.7 A will fire a squib 50% of the time. The other 50% of the

time the current can flow through the squib indefinitely. This means that,

on the average, the heat generated by 1.7 A in the bridgewire raises the

pyrotechnic next to the bridgewire to its ignition temperature. It is impor-

tant to note that a thermal contact conductance value is not necessary for this

steady-state heat transfer problem (Ref. 9, p. 190). This estimate can be

grossly in error because the amount of heat drawn away by the alumina

header at long times is unknown. In other words, the boundary of the system

4 JPL Technical Memorandum 33-655

Page 12: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

shown in Fig. 3 would increase with time and include the alumina header

that, in turn, would affect the temperature distribution in the pyrotechnic

and the bridgewire by an amount that cannot be calculated accurately at

this time.

The characteristic ignition temperature for the B-KCl04-Viton pyro-

technic was estimated to be about 672.03 K (750°F). This estimate was

based on the fact that small tablets of the pyrotechnic ignited within 10 s

after being dropped into a Woods-metal bath kept at 699. 81 K (800'F).

The thermal contact conductance between the bridgewire and the pyro-

technic has never been measured experimentally. Because the pyrotechnic

is placed on the bridgewire in a form of a fine powder and pressed down

against it at 1. 378 X 108 N/m 2 (20, 000 psi), it was expected that the contact

conductance would be much larger than those reported (Refs. 7 and 9) for

metal-to-metal contact of machined surfaces. The proper value for h was

determined by matching the computer predicted time for ignition with the

experimentally measured time to bridgewire burnout (1. 6 ms) for a current

level of 3. 5 A and a 294. 3 K (70 0 F) ambient temperature. This means that

an h was found by trial and error that made the computer program predict a

temperature of 672. 03 K (750*F) in node 3 after 1. 6 ms of a constant 3. 5-A

input into the bridgewire. The only value for h that satisfies these condi-

tions (when used with the above values for the thermal properties) was found

to be 31, 200 W/m 2 -K (5, 500 BTU/h-ft 2-F). As it can be seen from

Fig. 5, smaller values for h yield lower temperatures for node 3 at 1. 6 ms,

and, as a result, the computer predicted that the time to reach an ignition

temperature of 672. 03 K (750'F) would be larger than 1. 6 ms.

V. RESULTS

With the eight thermal properties and parameters fixed at the values

indicated in the previous Section, the computer program was run with

different initial temperatures and higher current levels.to test its ability

to predict ignition times at those conditions. Table 1 shows a comparison

between the computer predicted ignition time and the experimentally

measured tizmie to bridgewire burnout for MM'71 squib tests ranging from

JPL Technical Memorandum 33-655

Page 13: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

144.25 K to 366.48 K (-200"F to +2000 F) for both 3.5 and 5 A. The

agreement in the current range is quite good. The program's performance

at higher and lower currents will be discussed in Subsection V-D.

A. TEMPERATURE RESULTS

Figure 6 shows the temperature distribution within the bridgewire -

pyrotechnic system at 0. 4-ms time intervals for the 3. 5-A, 294. 3 K (70-F)

ambient temperature condition. A number of important points about the

system can be demonstrated with this figure. First, the discontinuity in

temperature at the bridgewire - pyrotechnic interface is quite apparent.

Second, there is very little temperature difference between the center of the

bridgewire and the outside surface of the bridgewire. Finally, the heat does

not diffuse past 1.016 x 10-2 cm (4 X 10-3 in. ) within the pyrotechnic during

the first 1. 6 ms.

Figure 7 again demonstrates the dramatic temperature difference

between the bridgewire and the hottest particles of the pyrotechnic. It also

shows that the radial heat flux out of the bridgewire and into the pyrotechnic

increases with time because it is directly proportional to the temperature

difference between the bridgewire and node 3. The large magnitude of the

heat flux (in the millions of W/m2 (BTU/h-ft2)) is due to the relatively large

value of the thermal contact conductance.

Figures 8 and 9 show the temperature history within nodes 3 and 2

respectively when a 3. 5-A current is added to a squib at 144. 25 K,

294. 3 K, and 366.48 K (-200'F, +70'F, and +200'F). It should be noted

that the three curves on each figure are the same except for a temperature

offset at time zero. This happens because the driving force for conduction

heat transfer is a temperature difference. In other words, the temperature

difference between the initial ambient temperature and the temperature at

some time t is always the same for a given node regardless of the initial

starting temperature.

Figure 10 shows the temperature (T) history of a bridgewire and the

hottest pyrotechnic particles when a 3. 5-A current is terminated after

1. 0 ms. The heat in the hot bridgewire diffuses out into node 3 and raises

the pyrotechnic's temperature above what it was when the pulse was

6 JPL Technical Memorandum 33-655

Page 14: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

terminated. The maximum temperature (TMAX) in node 3 was reached

0. 4 ms after the pulse was stopped. This type of behavior is consistent with

the observed delayed firings that result when terminated pulses of low

energy are used to fire squibs.

B. ENERGY RESULTS

Figures 11 and 12 show the total energy received by the bridgewire and

the pyrotechnic as a function of time. The total electrical energy delivered

to the bridgewire is IZRt, and the energy received by the pyrotechnic is the

instantaneous heat flux out of the bridgewire (as shown in Fig. 7) integrated

over time. It can be seen from Fig. 11 that at 294. 3 K (70'F) ambient

temperature (TAMB) and 3. 5-A input the total electrical input up to the

ignition time is 26. 4 mJ. About 30% of that energy, i. e. , 8 mJ, will

have been transferred into the pyrotechnic by the same time. These 8 mJ

of energy diffused through the pyrotechnic to cause the temperature profile

at 1. 6 ms shown in Fig. 6. The energy curves of Figs. 11 and 12 are

similar for the same reasons that the temperature curves of Figs. 8 and 9

are similar in Subsection V-A.

C. AXIAL TEMPERATURE DISTRIBUTION

One of the assumptions made in the one-dimensional heat conduction

model shown in Fig. 4 is that axial heat conduction along the bridgewire is

negligible. This assumption was tested by writing a more extensive pro-

gram that incorporated all the same features as the previous one except

that both radial and axial conduction was permitted in the bridgewire and

pyrotechnic. A schematic of the new bridgewire - pyrotechnic system

divided into 39 nodes is shown in Fig. 13. Since the axial temperature

profile of the bridgewire is symmetric about its center, only one half of

the bridgewire needed to be simulated. The library program HEAT per-

mitted a maximum of forty nodes. Thus the nodes in the radial direction

were made large to keep the total number of nodes below this allowable

maximum. This coarser grid did not give as accurate a radial temperature

distribution as the previous program.

The calculated axial temperature distribution in the bridgewire at

0. 5-ms intervals for 3. 5-A input is shown in Fig. 14. It can be seen that

the temperature of the bridgewire drops sharply at both ends and that the

JPL Technical Memorandum 33-655 7

Page 15: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

central 90% of the wire is at the same temperature. Since there is no axial

temperature gradient in the central 90% of the bridgewire, no axial heat

conduction exists there, and thus the one-dimensional heat conduction

assumption is valid over that portion of the bridgewire.

Axial conduction can become important in cases where the radial heat

transfer coefficient (or thermal contact conductance) becomes very small.

An example of this type is a bare Tophet A wire heated in still air.

Figure 15 shows the axial temperature distribution for such a wire at 20-ms

intervals. It is quite clear that the average bridgewire temperature is

considerably smaller than the maximum bridgewire temperature, and that

axial conduction is important over the whole wire.

D. PROGRAM DEFICIENCES

The bridgewire - pyrotechnic system of Fig. 3 has been shown to be

an adequate system to predict squib initiation at 3. 5- and 5-A current

levels. For smaller currents, this one-dimensional system is inadequate

because the heat diffusion from the bridgewire would be affected by the

alumina header. The system shown in Fig. 2, or one like it, must be simu-

lated on the computer to predict initiation in the vicinity of the "no-fire"

current levels.

;The computer program was also run at 15- and 20-A levels in an

attempt to predict experimentally measured bridgewire burnout times at

those current levels. The results were somewhat unrealistic at these high

currents in that the computer program predicted the bridgewire would melt

before the hottest pyrotechnic particles reaches 672.03 K (750'F). Two

things can be done to obtain more reasonable computer results. First, an

increase in h above the value of 31,200 W/m2-K (5,500 BTU/h-ft2 - F) used

in the program would heat up the pyrotechnic faster and keep the bridgewire

from becoming completely molten. Second, if the specific heat of Tophet A

increases with temperature as much as it does for nickel and chromium (the

two constituents of Tophet A), the bridgewire may be prevented from

becoming molten. It is clear that the computer model should be extended to

incorporate variable thermal properties for the system. The temperature

variation of the specific heat of Tophet A must also be determined experi-

mentally from room temperature up to the melting point.

8 JPL Technical Memorandum 33-655

Page 16: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

VI. CONCLUSIONS

A transient heat conduction model for the prediction of squib initiation

has been presented. The three main features of the model are:

(1) A thermal contact conductance between the bridgewire and the

pyrotechnic is incorporated in the model.

(2) A single ignition temperature is assumed.

(3) The bridgewire and the pyrotechnic are treated together in a

coupled system.

It has been shown that the model adequately predicts ignition at 3. 5-A

and 5-A levels for ambient temperatures between 144. 25 K and 366. 48 K

(-200°F and +200 0 F). More accurate thermal properties for Tophet A and

the pyrotechnic are required for accurate predictions at higher currents. At

lower currents, the alumina header must be included in the system.

REFERENCES

1. Austing, J. L., et al., "A Heat Transfer Study of Hot Wire Ignition ofa Metal-Metal Oxide Mixture, " in Proceedings of the 5th Symposiumon Electroexplosive Devices, Franklin Institute, Philadelphia, Pa.,1967.

2. Stresau, R. H., Peterson, R., and Chamberlain, D., "Electrical andThermal Considerations in the Design of Electro-Explosive Devices, "in Proceedings of the 5th Symposium on Electroexplosive Devices,Franklin Institute, Philadelphia, Pa., 1967.

3. Davenport, D. E., and Reynolds, H., "Quantitative Predictions ofEED Firing Characteristics, " in Proceedings of the 6th Symposium onElectroexplosive Devices, San Francisco, Calif., 1969.

4. Dansby, H. B., and Freeman, W. B., "Numerical Thermal Analysisof Electroexplosive Devices, " in Proceedings of the 7th Symposium onExplosives and Pyrotechnics, Franklin Institute, Philadelphia, Pa.,1971.

5. Petrick, J. T., and Montgomery, R. L., "Recent Developments inModeling the Hotwire Igniter, " in Proceedings of the 7th Symposium onExplosives and Pyrotechnics, Franklin Institute, Philadelphia, Pa.,1971.

JPL Technical Memorandum 33-655 9

Page 17: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

6. Osterkamp, A. M. , and Peckham, H. D. , "Pyrotechnic DeflagrationModel, " in Proceedings of the 7th Symposium on Explosives andPyrotechnics, Franklin Institute, Philadelphia, Pa. , 1971.

7. Fried, E., "A Joint Heat Transfer Data Critical Study and DesignGuidelines, " NASA-CR- 119933. General Electric Valley Forge SpaceCenter, Philadelphia, Pa., June 1971.

8. Carslaw, H. S. , and Jaeger, J. C. , Conduction of Heat in Solids,2nd Edition, Oxford University Press, Oxford, England, 1959.

9. Fletcher, L. S. , "A Review of Thermal Control Materials forMetallic Junctions, " AIAA Paper No. 72-284, presented at theALAA 7th Thermophysics Conference, April 10 - 12, 1972,San Antonio, Texas, 1972.

10 JPL Technical Memorandum 33-655

Page 18: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

Table 1. MM'71 firing data comparison

Ambient No. of Average time Model prediction ofNo. of Range, time to reach

Amperes temperature, to burnout, mstime to reachK (OF) s msms 672.03 K (750'F), ms

3. 5 294.3 (70) 20 1. 59 1. 45 - 1. 79 1. 6

3.5 144.25 (-200) 10 2.02 1.8 -2.2 2.27

Un

3. 5 366.48 (+200) Bridgewire burnout data not available 1. 31

5 294.3 (70) 3 0.84 0. 80 - 0. 88 0. 82

5 144. 25 (-200) 4 1.08 1. 05 - 1. 1 1. 1

5 366.48 (+200) 4 0.58 0. 51 - 0.71 0. 70

Page 19: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

OUTPUTCHARGE

END CLOSURE

BR IDG EW IRE

ALUMINAADAPTERCONNECTOR HEADERASSEMBLY

BODY

Fig. 1. Cutaway view of JPL squib

12 JPL Technical Memorandum 33-655

Page 20: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

DISTANCE TO WHICHHEAT HAS DIFFUSEDFROM TIME ZERO TO

PYROTECHNIC IGNITION TIME/ PYROTECHNIC

/ BRIDGEWIRE

\ - ALUMINA

Fig. 2. The bridgewire - pyrotechnic - alumina system;axial heat conduction is neglected

JPL Technical Memorandum 33-655 13

Page 21: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

DISTANCE TO WHICHHEAT HAS DIFFUSEDFROM TIME ZERO TO

/IGNITION TIME

/BRIDGEWIRE

\ PYROTECHNIC

ALUM INA

Fig. 3. The bridgewire - pyrotechnic system;axial heat conduction is neglected

14 JPL Technical Memorandum 33-655

Page 22: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

I-

PYROTECHNIC

BRIDGEWIRE

w -: : . 2.54 -3 10-3- () NODE LOCATION, cm x 10 (in. x 10

0.48 3.05 3.56 4.06 4.51 5.08 5.59 6.09 6.60 15.49(0.189) 5 (1.2) (1.4) (1.6) (1.8) (2.0) (2.2) (2.4) (2.6) (6.1)

2 3 6

0 ~0 2. NODE NUMBERS

o ,i. I /

Fig. 4. The bridgewire - pyrotechnic system of Fig. 3 showing

division into twenty nodes of variable mass

04, BR/,D 0. 43

Page 23: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

810.9-" (1000)

01

S755.4S(900) IGNITION TEMPERATURE =

672.0 K (7500 F)

II- 699.8

O (800)U-

Eo 644.3"o (700)I*-m h = 31,200 W/m2 - Kc 588.7a (600) (5,500 BTU/h-ft - OF)Oz

533.2LU (500)I-

477.6C1. (400)

I-

0 11,360 22,720 34,080 45,440(2,000) (4,000) (6,000) (8,000)

THERMAL CONTACT CONDUCTANCE h, W/m 2 - K (BTU/h-ft 2 - OF)

Fig. 5. Node 3 temperature at the bridgewire - pyrotechnic interface

16 JPL Technical Memorandum 33-655

Page 24: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

1366.5(2000)

1.6 ms1255.4(1800)

1144.3(1600)

1.2

1033.25 A(1400) I= 3.5 A

h = 31,200 W/m - K

922.0 (5,500 BTU/h-ft2 - OF)

0 (1200)

LUS0.8

D 810.9(1000)

u 699.8(800)

588.7 -0.4-(600)

477.6(400) 1.61.6 ms

366.5 1.2(200) 1 0.8283.2(50) 1

0 2.5 5 7.6 10 12.7 15(1) (2) (3) (4) (5) (6)

RADIAL DISTANCE FROM CENTER OF BRIDGEWIRE, cm x 10-3 (in. x 10-3)

Fig. 6. Radial temperature distribution within thebridgewire - pyrotechnic system

JPL Technical Memorandum 33-655 17

Page 25: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

25.22 I I(8.00) 1= 3.5 A

- 2h = 31,200 W/m 2 - K

(7.00)- (5,500 BTU/h - ft 2 - 0F)- /

18.91 1922.0(6.00)- BRIDGEWIRE (3000)

MELTINGTEMPERATURE

.o 15.76 1644.3(5.00) (2500)

12.60 1366.5o (4.00)- (2000)( 0

U--9.46 1088.7

(3.00) (1500) -

AVERAGEO BRIDGEWIREx TEMPERATURE ,

6.30 / 810.9u- (2.00) (1000)

3.15 533.2S(1.00) IGNITION (500)

TEMPERATURE

NODE 3TEMPERATURE

0 1.0 1.6 2.0 3.0

TIME, ms

Fig. 7. Instantaneous radial heat flux and instantaneoustemperature of bridgewire and node 3

18 JPL Technical Memorandum 33-655

Page 26: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

699.8(800) 672 K(7500F ) 1.31 ms 2.27ms 1.60 ms

644.3 _(700)

IGNITION TIME

588.7(600)

533.2(500)

477.60 (400)

" 422.0- (300)-

: 366.5- (200)

Ui

O 310.9Z (100)

294.3(70) 1= 3.5 A

255.4 h = 31,200 W/m 2 - K(0) (5, 500 BTU/h - ft2 - °F)

199.8(-100)

144.3(-200)

88.7(-300) I

0 1 2 3

TIME, ms

Fig. 8. Temperature history of node 3 for initial squibtemperatures of 144. 25 K, 294. 3 K, and 366. 48 K

JPL Technical Memorandum 33-655 19

Page 27: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

1477.6 I(2200) 2.27ms

1366.5(2000)

1.60 ms

1255.4 IGNITION(1800) 1.31 ms TIME

1144.3(1600)

1033.2(1400)

0922.0(1200)

I--

810.9(1000)

IU

C*-

wU 699.8- (800)OZ

588.7(600) 1= 3.5 A

h = 31,200 W/m - K(5,500 BTU/h - ft2 - OF)

477.6(400)

366.5(200)

294.3(70)

0

144.3(-200) I I

0 1 2 3

TIME, ms

Fig. 9. Temperature history of node 2 for initial squib temperaturesof 144. 25 K, 294. 3 K, and 366. 48 K

20 JPL Technical Memorandum 33-655

Page 28: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

I = 3.5 A

h = 31,200 W/m 2 - K(5,500 BTU/h-ft 2 - oF)

1088.7(1500)

PULSE TERMINATION

BRIDGEWIRETEMPERATUREU-

0 INODE 2810.9

, (1000)

I-

0L

T = 545.9 KLU MAX

T = 522.6 K (5230F)(4810F)

533.2(500)

PYROTECH N ICTEMPERATURENODE 3

0II0 1 2 3

TIME, ms

Fig. 10. Temperature history of nodes 2 and 3 during a constantcurrent pulse of 3. 5 A for 1 ms

JPL Technical Memorandum 33-655 21

Page 29: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

40 I I /

TAMB = 294.3 K (700F)1=3.5A 2

h =31,200W/m - K

(5,500 BTU/h-ft 2 - oF)

30 /

26.4

E

O 20

ELECTRICALENERGYDELIVERED

10 - /1 /

ENERGY8.0 RECEIVED BY

PYROTECHNIC

IGNITIONTIME

0 1.0 1.6 2.0 3.0

TIME, ms

Fig. 11. Energy delivered to the bridgewire and pyrotechnic:TAMB = 294. 3 K

22 JPL Technical Memorandum 33-655

Page 30: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

40 I I I

TAMB = 144.3 K (-2000 F) 37.5

I= 3.5 A

h = 31,200 W/m 2 - K

(5,500 BTU/h - ft2 - OF)

30

E

ELECTRICAL20 - ENERGY

, / DELIVERED

13.8IGNITIONTIME

10

ENERGYRECEIVED BYPYROTECHNIC

0 1.0 2.0 2.27 3.0

TIME, ms

Fig. 12. Energy delivered to the bridgewire and pyrotechnic:TAM B = 144. 25 K

JPL Technical Memorandum 33-655 23

Page 31: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

CENTER OFBRIDGEW0.0045 in.RE

Fig. 13. Division of the two-dimensional bridgewire -pyrotechnic system into nodes; the bridgewire is divid-ed axially into 10 nodes, the pyrotechnic into 25 nodes,and the pin into 2 nodes

24 JPL Technical Memorandum 33-655

Page 32: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

1144.3 I 1(1600)

1033.2(1400) 1.5 ms

U-. 922.0

2 (1200)

2 810.9 1.0 ms(1000)

LUI

699.8"u (800)I--LU

- 588.7 0.5 ms"' (600)

477.6m (400) 1 = 3.5 A

h = 31,200 W/mrn 2 - K366.5 2(200) (5,500 BTU/h - ft2 - °F)

0 I I I I0 0.2 0.4 0.6 0.8 1.0

AXIAL DISTANCE ALONG BRIDGEWIRE, X/L

Fig. 14. Axial bridgewire temperature distribution;the bridgewire is embedded in the pyrotechnic

JPL Technical Memorandum 33-655 25

Page 33: Heat Transfer Model for Predicting Squib Ignition · Heat Transfer Model for Predicting Squib Ignition Times V. Sernas (ASACR-fR~3834) HEAT TRANSPER MODEL FOR N74-1760 PREDICTING

1144.3 I I I(1600)

1033.2(1400) 60 ms

I- 922.00 (1200)

Lii 810.9S(1000) 40 ms

-

699.8(800)

I-_ 588.7

3: (600)0 20ms

477.6

(400) BURNWIRE (TOPHET A)

366.5 I 0.5 A(200) h 56.8 W/m2 - K (10 BTU/h - ft2 - OF)

o0 I I I0 0.2 0.4 0.6 0.8 1.0

AXIAL DISTANCE ALONG BRIDGEWIRE, X/L

Fig. 15. Axial temperature distribution within the barebridgewire (burnwire)

26 JPL Technical Memorandum 33-655NASA-JPL-Coml., L. A. Calif.


Recommended