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AD-A240 185 TECHNICAL REPORT 3L-91-11
1KA-Ill, PHASE C, M-1 PROPELLANT TESTS:DEFLAGRATiON IN PARTIAL CONFINEMENT
by
Charles E. Joachim
Structures Laboratory
DEPARTMENT OF THE ARMYWaterways Experiment Station, Corps of Engineers
3909 Halls Ferry Road, Vicksburg, Mississippi 39180-6199
DTICrS ELECTSEP11 1991
;;J D
July 1991-a Final Report
Approved For Public Release; Distribution Is Unlimited
91-10272
Prepared for US DoD Explosives Saiety Board,
LT Norwegian Defence Construction Service, andLABORATORY ,afety 6evit.s Organisation, Ministry of Defence, United Kingdom
)i :- !, G7 3
form ApprovedREPORT DOCUMENTATION PAGE OMB No. 0704-0188
Pubhi repoting burden for this colet'on of information is estimated to average 1 hour per response. including the time for reviewing instructions, searching existing data sources,gathering in g the data needed, and completing and reviewing the collection of information Send comments regarding this burden estimate or any other aspect of thiscollection of information. ncu ngsuggestions for reducing this burden, to Washington Headquarters Services. Directorate for information Operations and Reports. 1215 ;effefson
Davis Highay. Suite 1204. ArlingtOn. MVA 22202-4302. and to the Office of Management and Budget. Paperwork Reduction Project (0704-0188). Washington, OC 20503
1. AGENCY USE ONLY (Leave blank) 2. REPORT DATE 3. REPORT TYPE AND DATES COVERED
I July 1991 Final report4. TITLE AND SUBTITLE 5. FUNDING NUMBERS
KA-Ill, Phase C, M-1 Propellant Tests: Defiagration in PartialConfinement6. AUTHOR(S)
Charles E. Joachim
7. PERFORMING ORGANIZATION NAME(S) AND ADDRESS(ES) 8. PERFORMING ORGANIZATIONREPORT NUMBER
USAE Waterways Experiment Station, Structures Laboratory, Technical Report3909 Halls Ferry Road, Vicksburg, MS 39180-6199 SL-91-11
9. SPONSORING / MONITORING AGENCY NAME(S) AND ADDRESS(ES) 10. SPONSORING / MONITORING
AGENCY REPORT NUMBER
US DOD Explosives Safety Board, Norwegian Defence ConstructionService, and Safety Services Organisaio,:, Ministry of Defence,United Kingdom
11. SUPPLEMENTARY NOTES
12a. DISTRIBUTION /AVAILABILITY STATEMENT 12b. DISTRIBUTION CODE
Approved for public release; distribution is unlimited
13. ABSTRACT (Maximum 200 words)
When a propellant material is stored under confined conditions, US and NATO explosives safetyregulations require that the safety hazard quantity-distance (Q-D's) used for Hazard Class 1.1 (massdetonating) explosives be applied, rather than the less restrictive Q-D's normally used for propellantsand other Class 1.3 materials. This is based on the assumption that high gas pressures produced byan accidental burning of propellant in a confined volume will cause the burning (defiagration) totransition to a detonation. To test this assumption, a series of experiments were conducted in whichincreasing amounts of propellants were ignited and burned inside a heavy concrete structure with aninternal chamber volume of 5 m3. Pressure and temperatures were measured inside the chamber, in aconnecting exhaust vent, and in the free field beyond the exhaust vent pipe. Although there was noevidence that a detonation occurred, the high gas pressures produced by burning of the largestpropellent charge (250 kg) were sufficient to fail the structure.
14. SUBJECT TERMS 15. NUMBER OF PAGES
Deflagration/detonation Munitions storage 143M-1 propellant Propellant bum 16. PRICE CODE
17. SECURITY CLASS!FICATION 18. SECURITY CLASSIFICATION 19. SECURITY CLASSIFICATION 20. LIMITATION OF ABSTRACTOF REPORT OF THIS PAGE OF ABSTRACT
UNCLASSIFIED UNCLASSIFIED I INSN 7540-01-280-5500 Standard Form 298 (Rev 2-89)
Prescrbed by ANSI St Z39-18298-102
PREFACE
The KA-III Test Program was a series of explosive tests conducted as a
follow-on to the Defense Nuclear Agency's (DNA) MISERS COLD EVENT (June 1989).
The KA-III, Phase A and B tests were jointly sponsored by DNA and the
Norwegian Defence Construction Service, and subjected several Norwegian
structures previously tested on MISERS COLD to detonation effects of fuel-air
explosives (FAE), conventional bombs, and bigh explosive charges. The KA-III,
Phase C Test Program was sponsored by the US Department of Defense Explosives
Safety Board (DDESB), the Norwegian Defence Constructicn S.r.. 'NDCOS, ,iLd
the Safety Services Organisation (SSO) of the Ministry of Defence, United
Kingdom.
The KA-III Test Program was conducted on the DNA's MISERS GOLD Test Bed
at the White Sands Missile Range. LCDR W. F. Taylor was the DNA Test Director
and Mr. R. !. Flory, Washington Research Center, was Program Coordinator. The
DDESB, NDCS, and SSO Technical Monitors for Phase C were Dr. C. E. Canada,
Mr. Arnfinn Jenssen, and Dr. N. J. M. Rees, respectively.
The KA-III, Phase C, propellant burn study was performed by the
Explosion Effects Division (EED), Structures Laboratory (SL), US Army Engineer
Waterways Experiment Station (WES). Mr. Charles E. Joachim, EED, was Project
Manager and is the author of this report. The work was performed under the
general supervision of Mr. L. K. Davis, Chief, EED, and Mr. Bryant Mather,
Chief, SL. Field support was provided by Messrs. D. P. Hale, EED, and W. W.
Tennant, WES Engineering and Construction Services Division. Messrs. J. W.
Johnson and D. P. Biggs, WES Instrumentation Services Division, provided
timing and firing and instrumentation support for the field tests. Messrs. R.
Edgar and R. Campbell, Ballistec Systems, Inc., Quebec, Canada provided
digital recording and final data plots of all transducer-time histories.
COL Larry B. Fulton, EN, was the Commander and Director of WES, and
Dr. Robert W. Whalin was the Technical Director. Accczioo ror
NTIS CV. -ID , O iL '2
J -, U. a 3 iAv*1.i
CONTENTS
Page
PREFACE....................................i
LIST OF FIGURES................................iv
LIST OF TABLES................................xi
CONVERSION FACTORS, SI (METRIC) TO NON-SI UNITS OF MEASUREMENT . . . . xii
SECTION 1 INTRODUCTION............................1
1.1 BACKGROUND AND REQUIREMENT ........................ 1
1.2 OBJECTIVES................................2
SECTION 2 TEST PROCEDURES..........................3
2.1 GENERAL APPROACH.............................3
2.2 TEST STRUCTURE..............................3
2.3 PROPELLANT DESCRIPTION ......................... 4
2.4 ARMING AND FIRING............................5
2.5 INSTRUMENTATION.............................6
2.6 VIDEO COVERAGE..............................7
SECTION 3 TEST RESULTS............................8
3.1 INSTRUMENTATION PERFORMANCE ........................ 8
3.2 RESULTS OF TEST C-i (10-kg Charge) .................... 8
3.3 RESULTS OF TEST C-2 (25-kg Charge) .................... 9
3.4 RESULTS OF TEST C-3 (100-kg Charge) .................. 10
3.5 RESULTS OF TEST C-4 (250-kg Charge) .................. 11
SECTION 4 ANALYSIS OF RESULTS.......................13
SECTION 5 CONCLUSIONS...........................15
SECTION 6 RECOMMENDATIONS.........................16
REFERENCES.................................17
ii
CONTENTS (Continued)
Page
APPENDIX Al TEST C-I, 10-kg M-1 PROPELLANT BURN,DATA-TIME HISTORIES ...... ................... . 56
APPENDIX A2 TEST C-2, 25-kg M-1 PROPELLANT BURN,DATA-TIME HISTORIES . . . . . . . . . . . . . . . . . . . 72
APPENDIX A3 TEST C-3, 100-kg M-1 PROPELLANT BURN,DATA-TIME HISTORIES . . . . . . . . . . . . . . . . . . . 91
APPENDIX A4 TEST C-4, 250-kg M-1 PROPELLANT BURN,DATA-TIME HISTORIES ...... ................... . 109
iii
LIST CF FIGURES
Page
1. MISERS GOLD test site location ...... .................. .. 18
2. Vertical cross-section of horn antenna bunker with vent pipeattached. The M-l propellant charge was placed in a cardboardbox for Tests C-l, C-2, and C-3 and poured directly on thebunker floor for Test C-4 ....... .................... 19
3. Test C-2 charge (25 kg of M-1 propellant) placed in a cardboard
box on the floor of the bunker with booster (electric matchsurrounded by 50 gm of pistol powder) laid on the top surface ofthe charge ........... ............................ 20
4. Test C-3 charge (100 kg of M-1 propellant) placed in fourcardboard boxes taped together, with booster laid on the surfaceof the charge .......... .......................... . 20
5. Chamber pressure gage mount (ABII80) directly below vent pipe.Note: accelerometer mounting bracket (lower left) was left over
from M.iSERS GOLD EVENT ........ ...................... . 21
6. Water filled cylinder with five pressure gages. Note pipe with900 elbow connecting the cylinder to the interior of horn antenna
bunker ........... ............................ 21
7. Vent pipe with one free-field, side-on overpressure gage(ABEl73). Cables are seen for two internal vent pipe
transducers: thermal flux gage (TF192, left) and side-onoverpressure gage (ABEl72) ....... .................... . 22
8. Instrumentation layout (plan view) showing internal and externaltransducer locations. Five pressure gages were attached to thewater filled cylinder which was connected to the chamber via theair-filled pipe (upper left corner of drawing) .. .......... . 23
9. Recording bunker protecting digital recording system. A shallowcable ditch can be seen running (left to center background) fromthe recording bunker to the horn antenna bunker . ......... .. 24
10. Plan view of external airblast instrumentation and photo marker
locations ........... ............................ 25
11. Test C-1: length of exhaust gas plume (from end of vent pipe) asa function of relative time. Zero-time was not recorded, so alltimes are relative to an arbitrarily chosen start time ...... . 26
12. Test C-1: measured peak pressures as a function of distance fromthe center of the 10-kg M-1 propellant charge .. .......... . 27
iv
LIST OF FIGURES (Continued)
Page
13. Test C-i: tIerral flux at mid-length in the vent pipe (Gage
Tf!91) versus the differential of measured temperature (Gage
THCI7 0) wi1i respect to time. Each data point represents a *"pair" of values; an x-value from a given dT/dt, and a y-value
from the thermal flux record corresponding to the same timeinstant .after zero time) as the dT/dt value .. ........... . 28
14. Test C-l: calculated pseudo-thermal flux (from temperaturemeasurements of Gage THCI90) in the bunker chamber compared to
measured thermal flux-time histories in the vent pipe (GagesTF191 and TF192) .......... ......................... .. 29
15. Test G-2: length of exhaust gas plume (from end of vent pipe) as
a function of relative time. Zero-time was not recorded, so alltimes are L"iaLive to an arbitrarily chosen start time ...... .. 30
16. Test C-2: measured peak pressures as a function of distance from
the center of the 25-kg M-1 propellant charge .. .......... . 31
17. Test C-2: thermal flux at mid-length in the vent pipe (Gage
TFl91) versus the differential of measured temperature (GageTHCI90) with respect to time. Each data point represents a"pair" of values; an x-value from a given dT/dt, and a y-value
from the thermal flux record corresponding to the same time
instant (after zero time) as the dT/dt value .. ........... . 32
18. Test C-2: calculated pseudo-thermal flux (from temperature
measurement of (Gage THCI90) in the bunker chamber compared to
measured themal flux-time histories in the vent pipe (Gages
(TFl91 and TF192) ......... ........................ . 33
19. Test C-3: length of exhaust gas plume (from end of vent pipe) asa function of relative time. Zero-time was not recorded so all
times are relative to an arbitrarily chosen start time ...... .. 34
20. Test C-3: measured peak pressures as a function of distance fromthe center of the 100-kg M-1 propellant charge .. .......... . 35
21. Test C-3: thermal flux at mid-length in the vent pipe (Gage
TFl91) versus the differential of measured temperature (GageTHCI90) with respect to time. Each data point represents a"pair" of values; an x-value from a given dT/dt, and a y-value
from the thermal flux record corresponding to the same time
instant (after zero time) as the dT/dt value .. ........... . 36
V
LIST OF FIGURES (Continued)
Page
22. Test C-3: calculated pseudo-thermal flux (from temperaturemeasurement of (Gage THCl90) in the bunker chamber compared to
measured themal flux-time histories in the vent pipe (Gages
(TFI91 and TF192) ......... ........................ 37
23. Test C-4: length of exhaust gas plume (from end of vent pipe) asa function of relative time. Zero-time was not recorded so alltimes are relative to an arbitrarily chosen start time ...... .. 38
24. Test C-4: measured peak pressure as a function of distance from
the center of the 250-kg M-1 propellant charge .. .......... . 39
25. Peak overpressure versus distance from the center of the M-1propellant charge, KA-III, Phase C ..... ................ . 40
26. Peak chamber pressure versus M-1 propellant loading density,KA-III, Phase C; comparison with previous data from BRL testswith one and three ignition points of propellant charge ..... 41
27. Peak overpressure at end of vent pipe versus chamber loadingdensity; KA-III, Phase C ....... ..................... . 42
28. Peak total free-field pressure versus distance from the center of
the M-1 propellant charge, KA-III, Phase C ... ............ . 43
29. Peak thermal flux versus distance from the center of the M-1
propellant charge; KA-III, Phase C. Note: chamber thermal fluxdata Are calculated from thermocouple measurements ......... .. 44
30. Peak thermal flux versus M-1 propellant loading density, KA-III,
Phase C .............. ............................ 45
31. Peak chamber temperature versus loading density, KA-III, Phase C;comparison with previous data from BRL model test with one and
three ignition points of propellant charge ...... ............ 46
Al-l. Test C-l, airblast overpressure-time history at mid-length
inside the vent pipe, Gage ABEl71 .... ............... . 57
Al-2. Test C-l, airblast overpressure-time history at the exteriorend of the vent pipe, Gage ABEl72 .... ............... .. 58
Al-3. Test C-l, free-field airblast overpressure-time history at
0.3-m from the end of vent pipe, Gage ABEl73 .. .......... . 59
AI-4. Test C-1, free-field airblast overpressure-time history at
0.9-m from the end of the vent pipe, Gage ABEl74 ......... .. 60
vi
LIST OF FIGURES (Continued)
Page
Al-5. Test C-l, free-field airblast overpressure-time history at
2.1-m from end of vent pipe, Gage ABEl75 ... ............ . 61
Al-6. Test C-I, free-field airblast overpressure-time history at4.5-m from end of vent pipe, Gage ABEl76 .. ........... . 62
Al-7. Test C-l, free-field airblast total pressure-time history at2.1-m from end of vent pipe, Gage ABEl78 .. ........... . 63
Al-8. Test C-i, chamber airblast pressure-time history, Gage ABI180 64
Al-9. Test C-i, chamber airblast pressure-time history, Gage ABI182 65
Al-lO. Test C-l, chamber (water filled cylinder) airblast
pressure-time history, Gage ABI184 .... .............. . 66
Al-ll. Test C-1, chamber (water filled cylinder) airblastpressure-time history, Gage ABI185 .... .............. . 67
Al-12. Test C-I, chamber (water filled cylinder) airblastpressure-time history, Gage ABI187 .... .............. . 68
Al-13. Test C-l, chamber temperature, Gage THC190 .. .......... . 69
Al-14. Test C-l, thermal flux-time history at mid-length inside thevent pipe, Gage ABE191 ........... .................... /0
Al-15. Test C-1, thermal flux-time history at the extprio-r end ofthe vent pipe, Gage ABEl92 ...... .................. 71
A2-1. Test C-2, airblast overpressure-time history at mid-length
inside the vent pipe, Gage ABEl71 .... ............... . 73
A2-2. Test C-2, airblast overpressure-time history at the exteriorend of the vent pipe, uage ABZI72 .... ............. 74
A2-3. Test C-2, free-field airblast overpressure-time history at0.3-m from the end of vent pipe, Gage ABEl73 .. .......... . 75
A2-4. Test C-2, free-field airblast overpressure-time history at
0.9-m from the end of the vent pipe, Gage ABEl74 ......... .. 76
A2-5. Test C-2, free-field airblast overpressure-time history at2.1-m from end of vent pipe, Gage ABEl75 ... ............ . 77
A2-6. Test C-2, free-field airblast overpressure-time history at
4.5-m from end of vent pipe, Gage ABEl76 ... ............ . 78
vii
LIST OF FIGURES (Continued)
P;ige
A2-7. Test C-2, free-field airblast total pressure time- histrorv N'
0.9-m from end of vent pipe, Cage ABF177 .. ..... . .
A2-8. Test C-2, free-field airblast total pressutep-tim hivrnv,
2.1-m from end of vent pipe, Gage ABE8 ........... . 0
A2-9. Test C-2, chamber airblast pressure-time histni\, ,npe AWO 81
A2-10. Test C-2 chamber airblast pressure-time histoiv, Gage IBTPI+Y 82
A2-11. Test C-2, chamber airblast pressure-time histor-, Coge :\.1 83
A2-12. Test C-2, chamber airblast pressure-t-imp histov, -,w 9\:. 44
A2-13. Test C-2, chamber (water filled cylinder) airhlot:
pressure-time history, Gage ABI185 .................... 85
A2-14. Test C-2, chamber (water filled cylinder) airblint
pressure-time history, Cage ABI186 .................. 86
A2-15. Test C-2, chamber (water filled cylinder) airhlot,pressure-time history, Gage ABI187 .. .......... .
A2-16. Test C-2, chamber temperature, Gage THG1CO . . 88
A2-17. Test C-2, thermal flux-time history at mid-length inqidp :u cvent pipe, Gage TF191 ........ .................. 89
A2-18. Test C-2, thermal flux-time history at the oleyioy eld ot
the vent pipe, Gage TF192 ......... ................ 90
A3-1. Test C-3, airblast overpressure-time hist ,i v :i m d lene'l
inside the vent pipe, Gage ABE7I1 . . . .
A3-2. Test C-3, airblast overpressure-time histn,'v at Ac V.:;riv,
end of the vent pipe, Gage ABE172 . .. .. 03
A3-3. Test C-3, free-field airblast overpregsure-t e h h ,ov a!0.3-m from the end of vent pipe, Gage AF17I 91:4
A3-4. Test C-3, free-field airblast overpressura-tim: , nte w
0.9-m from the end of thp vent pipe, Gag,. 17. 95
A3-5. Test C-3, free-field airblast overpressurv- 1> i hsi: .t2.1-m from end of vent pipe, Gage AE1l75 .. Q
A3-6. Test C-3, free-field airblast o''erp r s ui :< hjw v ,>
4 5-m from end of vent pipe, Cage A PF1. 97
viii
LIST OF FIGURES (Continued)
Page
A3-7. Test C-3, free-field airblast total pressure-time history at
2.1-m from end of vent pipe, Gage ABEHl78 .. ........... . 98
A3-8. Test C-3, chamber airblast pressure-time history, Gage ABII80 99
A3-9. Test C-3, chamber airblast pressure-time history, Gage ABI181B 100
A3-10. Test C-3, chamber airblast pressure-time history, Gage ABI182 101
A3-11. Test C-3, chamber (water filled cylinder) airblastpressure-time history, Gage ABI185 .... .............. . 102
A3-12. Test C-3, chamber (water filled cylinder) airblastpressure-time history, Gage ABI186 .... .............. . 103
A3-13. Test C-3, chamber (water filled cylinder) airblast
pressure-time history, Gage ABI187 .... .............. . 104
A3-14. Test C-3, chamber (water filled cylinder) airblast
pressure-time history, Gage ABI188 .... .............. . 105
A3-15. Test C-3, chamber temperature, Gage THC190 .. .......... 106
A3-16. Test C-3, thermal flux-time history at mid-length inside thevent pipe, Gage TFi91 ....... ..................... . 107
A3-17. Test C-3, thermal flux-time history at the exterior end ofthe vent pipe, Gage TF192 ...... ................... .. 108
A4-1. Test C-4, a4 blast overpressure-time history at mid-length
inside the vent pipe, Gage ABEl71 ....... ............... 110
A4-2. Test C-4, airblast overpressure-time history at the exteriorend of the vent pipe, Gage ABEl72 .... ............... . i
A4-3. Test C-4, free-field airblast overpressure-time history at0.3-m from the end of vent pipe, Gage ABEl73 .. .......... . 112
A4-4. Test C-4, free-field airblast overpressure-time history at0.9-m from the end of the vent pipe, Gage ABEl74 ......... .. 113
A4-5. Test C-4, tree-field airblast overpressure-time history at
2.1-m from end of vent pipe, Gage ABEl75 ... ............ . 114
A4-6. Test C-4, free-field airblast overpressure-time history at
4.5-m from end of vent pipe, Gage ABEl76 ... ............ . 115
ix
LIST OF FIGURES (Concluded)
Page
A4-7. Test C-4, free-field airblast total pressure-time history at
0.9-m from end of vent pipe, Gage ABPH177 .. ........... . 116
A4-8. Test C-4, chamber airblast pressure-time history, Gage ABII80 117
A4-9. Test C-4, chamber airblast pressure-time history, Gage ABI181B 118
A4-10. Test C-4, chamber airblast pressure-time history, Gage ABI182 119
A4-11. Test C-4, cbamber airblast pressure-time history, Gage ABI183T 120
A4-12. Test C-4, chamber (water filled cylinder) airblast
pressure-time history, Gage ABI185 .... .............. . 121
A4-13. Test C-4, chamber (water filled cylinder) airblast
pressure-time history, Gage ABI186 .... .............. . 122
A4-14. Test C-4, chamber (water filled cylinder) airblast
pressure-time history, Gage ABI187 .... .............. . 123
A4-15. Test C-4, chamber (water filled cylinder) airblastpressure-time history, Gage ABI188 .... .............. . 124
A4-16. Test C-4, chamber temperature, Gage THC190 .. .......... . 125
A4-17. Test C-4, thermal flux-time history at mid-length inside the
vent pipe, Gage TF191 ....... ..................... . 126
A4-18. Test C-4, thermal flux-time history at the exterior end of
the vent pipe, Gage TF192 ...... ................... .. 127
x
LIST OF TABLES
Page
1. KA-III, Phase C: Configuration larameters for M-1 PropellantCharges ........... ............................ 47
2. Test C-I (Loading Density 2 kg/m3): Pre-Test Gage Location andDigital System Set-up Data ....... .................... .. 48
3. Test C-2 (Loading Density 5 kg/m3): Pre-Test Gage Location andDigital System Set-up Data ....... .................... .. 49
4. Test C-3 (Loading Density 20 kg/m3): Pre-Test Gage Location andDigital System Set-up Data ....... .................... .. 50
5. Test C-4 (Loading Density 50 kg/m3): Pre-Test Gage Location andDigital System Set-up Data ....... .................... .. 51
6. Test C-I (Loading Density 2 kg/m3): Gage Location and Peak
Measured Data .......... .......................... . 52
7. Test C-2 (Loading Density 5 kg/m3): Gage Location and Peak
Measured Data .......... .......................... . 53
8. Test C-3 (Loading Density 20 kg/'m3): Gage Location and PeakMeasured Data .......... .......................... . 54
9. Test C-4 (Loading Density 50 kg/m3 ): Gage Location and PeakMeasured Date ... . ...... .......................... 55
xi
CONVERSION FACTORS, SI (METRIC) TO NON-SIUNITS OF MEASUREMENT
SI (Metric) units of measurement used in this report can be converted toNon-SI units as follows:
Divide By To Obtain
calories per square centimeter-second 0.2712459 BTU per square foot-seconds
cubic metres 0.02831685 cubic feet
degrees Celsius* 1.8 C + 32 degrees Fahrenheit
kilograms 0.45359237 pound (mass)
kilograms per cubic metre 16.01846 pounds (mass) per cubic foot
kilopascals 6.894757 pounds (force) per square inch
metres 0.3048 feet
square metres 0.9290304 square feet
* To obtain Fahrenheit (F) temperature readings from Celsius (C) readings,
use the following formula: F - 1.8 C + 32. To obtain kelvin (K)readings, use: K - C + 273.14.
xii
KA-III, PHASE CM-1 PROPELLANT TESTS: DEFLAGRATION IN PARTIAL CONFINEMENT
SECTION 1
INTRODUCTION
1.1 BACKGROUND AND REQUIREMENT
In order to maintain a satisfactory level of combat readiness, the armed
forces of NATO nations must store large amounts of ammunition and propellant
for artillery and naval guns. Ammunition usually contains high explosives
that are classified as Class 1.1 explosion hazards by US and NATO guidelines,
due to the fact that they will "mass detonate"; i.e., an accidental explosion
of a single round will sympathetically detonate the entire mass of ammo rounds
in close proximity. Consequently, large separation distances, or "Quantity
Distances (Q-D's)," are required between a given quantity of stored ammunition
and other magazines (or other ammo storage or explosive operations areas),
inhabited buildings, public traffic routes, etc.
Under most conditions, propellants may burn, but they will not mass
detonate. They are therefore designated as Hazard Class 1.3 materials, and
are subject to much less restriction and have much smaller Q-D's than 1.1
materials. The theory exists, however, that if propellant is stored in a
chamber or other confined area, an accidental fire could quickly ignite the
propellant mass and rapidly produce a large volume of combustion gases.
Because this rapid buildup of gases can only vent through the relatively small
entrance into the chamber, the chamber becomes highly pressurized. The theory
postulates that such high pressures can cause the deflagration of the
propellant to transition to a detonation. Consequently, propellant stored
under confined conditions must be classified as a mass-detonating explosive,
or Hazard Class 1.1, instead of 1.3. This, in turn, requires much larger
"buffer zones", or Quantity-Distance (Q-D) separations between magazines,
inhabited buildings, public traffic routes, etc.
1.2 OBJECTIVES
The objective of the Phase C tests was to determine the combination of
confinement pressure and loading density required for M-1 propellant to
transition from deflagration to detonation, in the event of an accidental
1
fire. The tests also measured the temperatures, thermal flux and internal andexternal pressures generated by the deflagration of the various propellant
loading densities.
2
SECTION 2
TEST PROCEDURES
2.1 GENERAL APPROACH
Following the MISERS GOLD explosion test (1 June 1989) at White Sands
Missile Range, NM, several relatively undamaged, full-scale structures were
available for further testing at the MISERS GOLD site (Fig-ure 1). The KA-III
Test Series was developed to exploit these structures in an extensive program
of tests to evaluate the detonation effects of conventional (l.e., non-
nuclear) munitions. Phase C of the KA-III Series was planned to consist of up
to five deflagration and/or detonation tests, using M-1 propellant, inside a
small concrete bunker. The Phase C plan called for increasing the propellant
loading density with each successive test (loading densities of 2, 5, 20, 50
and 100 kg/m3)* until either (a) a transition from burning to a detonation
occured, or (b) the structure failed from the buildup of internal pressures.
The test program would be terminated at either point.
2.2 TEST STRUCTURE
The test structure, known as the Horn Antenna Bunker (MISERS GOLD
Structure #6410G), had internal dimensions of 1.4 m (side-to-side), 1.9 m
(front-to-back) and 1.9 m (height). The reinforced concrete walls, roof, and
floor of the structure were 30 cm thick. For the KA-III-C tests, the bunker
was modified by the addition of a vent tube welded into the observation port
opening, and by strengthening of the access hatch to resist internal pressures
from the propellant burn tests. The vent tube cross-sectional area was
selected to simulate the chamber and access tunnel proportions of the Shallow
Underground Tunnel/Chamber Explosion Test conducted at China Lake, CA, in
1988. The chamber and access tunnel at China Lake had the following
dimensions (volume, cross-sectional area and length):
Chamber: V. - 331.2 m 3 Tunnel: Vt - 132.5 m 3
Ac - 18.4 m2 At - 5.3 m2
LC - 18 m Lt - 25 m
• A table of factors for converting SI (metric) units of measurement to non-SI
units is presented on page xii.
3
The volume of the Horn Antenna Bunker (Vb) was 5 m3. If the vent area ratio
(vent area/chamber volume) of the China Lake facility is applied to the bunker
test design, then
At/VC - 5.3/331.2 - 0.016, A,/Vb - 0.016,
A, - 0.016 x 5.0 - 0.08 M 2.
A steel pipe was selected whose diameter gave a vent area closest to this
value. The pipe was 35.6 cm (14 in.) in diameter, with an extra heavy
(12.7 mm, or 0.50 in.) wall thickness. With an inside diameter of 33.02 cm
(13 in.), this pipe provided a vent area of:
A, - 3.1416 x (33.02/2)2 - 0.0857 m2 .
For the tunnel and vent pipe, the following ratios apply:
nIn/It - (Av/At) 112
The length of pipe required was computed from this ratio as:
L.,L t (At/At)"12 = 25 (0.0857/5.3)1/2 - 3.18 m.
The Horn Antenna Bunker with vent tube attached is shown in plan view in
Figure 2.
2.3 PROPELLANT DESCRIPTION
The M-1 propellant used in the Phase C test program was demilitarized
material obtained from the US Army Armament, Munitions and Chemical Command's
Rock Island (Illinois) Arsenal (stock number 1376-451-2881). It was shipped
to the White Sands Missile Range in metal-lined, wooden containers (type M-24)
with a stated propellant weight of 64 kg in each canister. The actual
propellant weight in each canister was found to average approximately 45 kg.
The propellant grains were examined at WES under an electron microscope, and
average dimensions were obtained. The propellant grain was cylindrical, with
a single perforation (a perforation is a hole through the entire length of the
4
grain cylinder). The grains were nominally 5 mm long, with a 1.1-mm outside
diameter, a 0.5-mm inside diameter, and, a 0.36 mm WEB (web thickness).
Shipping labels indicated the material was all from Lot No. RAD 69214.
For Tescs C-I - C-3, the M-1 propellant charge was placed in a cardboard
box at the center of the chamber floor (Figure 3). For Test C-3, four boxes
were taped together, as shown in Figure 4. The individual boxes were 4.92 cm
wide, 6.50 cx. long, and 4.92 cm deep. For Test C-4, the propellant was poured
onto the floor, forming an approximately conical shape. Charge weight,
volume, and surface area data for each test are given in Table 1.
2.4 ARMING AND FIRING
Atlas electric matches were used to initiate all M-1 propellant burns.
The match was placed in a plastic bag along with a booster charge of 50 grams
of smokeless pistol powder to assure ignition. The electric match lead wires
were connected to separate leads of a 4-conductor shielded cable which exited
the bunker through a cable grommet installed in the hatcn cover. The firing
line was approximately 200 m long, running from the bunker to a sandbagged
junction box containing a 12-volt battery and a single-pole, double-throw
relay. The shorted side of the relay was connected to the cable from the
electric match, and the other side to the test event control system.
All tests were computer controlled from North Park Bunker #1. The event
controller provided relay signals to start the Digistar digital system at
T-100 msec. A closure at T-0 msec (zero-time) switched the firing line from
short to 12 volts, which initiated the electric match. After the deflagration
and/or detonation was complete, the firing control unit was disconnected from
the firing line and the test area inspected for possible hazards by a reentry
team consisting of the WES blaster, WES Project Officer, and DNA Site Safety
Officer. When no visual signs of internal burning were evident, the bunker
was approached from the rear and a hand-held, digital, temperature meter was
attached to the thermocouple cable to monitor the temperature inside the
bunker chamber. The hatch cover was reopened when the temperature monitor
indicated that the internal temperature had fallen below 130°F. A ventilrtion
duct, connected to an exhaust fan, was then placed inside the chamber through
the open hatch to exhaust fumes from the chamber. When gas sampling indicated
5
that the carbon dioxide content of the interior was safe, personnel were then
allowed to reenter the bunker for cleanup and instrumentation work.
2.5 INSTRUMENTATION
Instrumentation for all Phase C tests included four flush-mounted
airblast pressure gages on the interior bunker walls. Two pressure gages were
mounted on the center of the side wall (right side as observed from outside
through the vent pipe); one at a height of 63 cm and the other at 1.27 cm.
The other two internal gages were mounted at the center (mid-height and
mid-width) of the front (under the vent pipe, Figure 5) and rear walls. The
pressure gages were placed in mounts that were glueti with epoxy into holes
drilled through the bunker concrete wall. These gage mounts included a metal
baffle system and nylon bushings to protect the airblast gages from direct
heating by the burning propellant.
Five additional airblast gages were mounted on a water-filled cylinder
which was connected to the bunker interior through an air-filled steel vent
pipe, 12.7 mm in diameter (inside) and 2.8 m long. The pipe penetrated the
chamber wall at the upper rear corner of the chamber (wall on right side),
with the other end connected to the water-filled cylinder through a 90° elbow
(Figure 6). The vent pipe was instrumented at two internal points for
side-on airblast and thermal flux measurements. Four additional side-on
airblast pressure gages were installed on the ground surface outside the
bunker along the extended vent pipe centerline to measure side-on
overpressure, and two total-pressure probe gage mounts were placed along the
extended centerline of the vent pipe. The vent pipe, with the first of the
four free-field, side-on overpressure gages, is shown in Figure 7. The
temperature inside the bunker during the propellant burns was monitored with a
Type K thermocouple, mounted in the hatch cover. Gage locations are shown in
Figure 8. Gage types, locations, and predicted peak values are given in
Tables 2 through 5.
Kulite Model HKS-375 series pressure gages were used in all locations
where predicted peak pressures exceeded 1.5 MPa. Kulite XT-190 Series gages
were used for lower pressures. Thermal flux measurements were made with
Medtherm Model #64-250SB-17 heat flux transducers. These gages use a
6
Schmidt-Buelter thermopile with a capacity of 250 BTU/ft2-sec, with an
over-range capability of 150%. Bunker temperatures during propellant burns
were monitored with Medtherm Model TC-K1212UP thermocouples. These gages use
a Type K Chromel/Alumel junction. Temperatures were digitally recorded during
the burns.
Transducer analog signals were digitized and recorded by Ballistech
Systems, Incorporated (BSI) using their Digistar II digital system. The
transducer signals were transmitted to the recording bunker (Figure 9) on
4-conductor, shielded cable (approximately 200 m long) with a floating ground.
Each channel was electrically calibrated at the digitizer by the equivalent
voltage method. The digital records were field processed for quick-look data
assessments. BSI provided final, filtered time-history plots at a later date.
These plots akL presented in Appendix Al through A4.
2.6 VIDEO COVERAGE
A VHS video camera was used to obtain visual data on the external effects
of the propellant burn. The camera was positioned to provide coverage of the
bunker, vent tube and a region approximately 25 m to the front of the vent
tube. The video camera was started just prior to each test and ran unat-
tended. There was no visual zero time indicator. Photo markers were emplaced
on both sides of the extended vent tube centerline to provide reference points
from which to estimate flame spread and other visual effects. The markers
were 61-cm square plywood sheets, attached to 10-cm square posts and painted
with alternating 30-cm black and white squares. Photo marker locations are
shown in Figure 10.
7
SECTION 3
TEST RESULTS
3.1 INSTRUMENTATION PERFORMANCE
Because preshot predictions of the peak overpressure levels expected in
the bunker from the propellant burns were too high, a number of gages failed
to record useful records on Tests C-1 and C-2. Of the 20 data channels on
Test C-i, eight produced good quantitative data, eight produced records useful
for a qualitative analysis, and four produced no data. On Test C-2, seven
channels provided good quantitative data, ten produced qualitative
information, and two had no data. Nineteen channels were operational on
Tests C-3 and C-4, with 15 providing gcod records on C-3 and 11 on C-4. One
channel was overdriven on Test C-3, and seven on C-4, but these still produced
useful qualitative information.
For all tests, the data was digitized at a rate of one sample per
220 micro-seconds, which gave a nominal recording time of 60 seconds on each
channel.
3.2 RESULTS OF TEST C-1 (10-kg Charge)
The initial visual indication of the internal M-1 propellant burn was
black smoke that was projected some 3 meters beyond the end of the vent pipe.
The smoke quickly changed to flame and, by 4 seconds after (assumed)
initiation, the flame extended approximately 5 meters from the end of the
pipe. Total duration of the external flame was approximately 11 seconds. The
position of the fire plume is plotted versus time in Figure 10. Since the
video does not have a zero (initiation) time indicator, an arbitrary start
time was assumed. As shown in Figure 11, the initial gas flow out the vent
pipe had a velocity of 3.47 m/sec. Although not seen in the video, an orange
vapor or smoke persisted more than an hour after burning ceased, seeping out
through the antenna port, vent pipe and around the imperfectly-sealed hatch
cover.
Measured peak pressure data are presented in Table 6. Peak side-on
overpressures (Figure 12) produced by the burning of the 10-kg M-1 propellant
charge were very low. Pressures beyond the vent pipe were higher than the
8
very low transducer signals indicated for the overpressure inside the bunker.
This fact suggests that uncombusted gas and propellant was carried outside and
secondary burning occurred in the vented gas plume. When the bunker was
reentered, the propellant charge container (cardboard box) was charred but not
destroyed, indicating a lack of sufficient oxygen during deflagration. The
video record shows the presence of a pulsing flame in the gas plume released
through the vent pipe. Herrera (1984) reports that, in an earlier study, un-
burned propellant was transported outside a similar test structure in a plume
with overpressures on the order of 1.6 kPa.
The temperature history recorded by the thermocouple inside the bunker on
Test C-1 was differentiated with respect to time by computing the slope
between digitized data points. This yielded a value, "dT/dt", for each time
interval sampled. In Figure 13, the different dT/dt values obtained from the
thermocouple record have been matched with the thermal flux levels recorded
for the same time intervals, at the mid-point of the vent pipe, by Gage TFI91.
These "pairs" of dT/dt and thermocouple readings are used as x and y values
for the data points shown in Figure 12. A linear least squares fit to the
data in Figure 12 therefore relates the temperature time differential to the
thermal flux. Although the thermocouple (Gage THCI90), located in the bunker
hatch cover directly above the burning propellant, was separated from the
thermal flux transducer by a distance of 2.55 m, this curve provides a crude
method for relating temperature to a "pseudo"-thermal flux. Applying the
relation shown in Figure 12, a pseudo-thermal flux-time history was calculated
from the temperature history (Gage (THC190). The calculated pseudo-thermal
flux for the chamber is compared with the measured flux in the vent pipe
(Gages TF191 and TF192) in Figure 14. As shown here, the calculated and
measured data are in good agreement.
3.3 RESULTS OF TEST C-2 (25-kg Charge)
The initial visual indication of the M-1 propellant burn inside the
bunker for Test C-2 was a glowing plume projected some 3 meters beyond the end
of the vent pipe, within approximately one second after initiation. The plume
of smoke and flame quickly extended, reaching a length of 10 m after
approximately 10 seconds. The position of the leading edge of the plume is
plotted versus time i Figure 15. As shown in the figure, the initial plumc
9
velocity was 3.13 m/sec. Although it continued to burn violently, the length
of the plume decreased after 10 seconds, retreating to the end of the vent
pipe. Total duration of the external gas plume was approximately 18 seconds.
The orange residual vapor observed after Test C-1 was not present after
burning of the Test C-2 propellant charge had ceased.
Measured peak pressure and thermal flux data are presented in Table 7.
Peak side-on overpressures (Figure 16) produced inside the bunker by the
burning of the 25-kg propellant charge were very low. Although the peak
external overpressures were approximately 20 percent higher for Event C-2 than
for Event C-l, the results still indicated that uncombusted gas and unburned
propellant were carried outside by the gas plume for external burning. Once
again, when the bunker was reentered, the propellant charge container
(cardboard box) was charred but not destroyed, indicating a deficiency of
oxygen during deflagration. The video recording again showed the presence of
a pulsing flame in the gas plume released through the vent pipe.
As was done for Test C-l, the temperature history recorded by the thermo-
couple on Test C-2 was differentiated with respect to time (dT/dt) by comput-
ing the slope between digitized data points. Thermal flux values recorded at
the mid-point of the vent pipe (Gage TFI91) are plotted versus dT/dt in
Figure 16. An "eyeball" fit was made to the data through the point
(dT/dt) - 0 and Q - 3.459 cal/m2-sec. Applying the relation shown in
Figure 17, a pseudo thermal flux-time history was calculated from the tempera-
ture history. The calculated pseudo-thermal flux for the chamber is compared
with the measured flux in the vent pipe (Gages TF191 ano TF192) in Figure 18.
As shown here, the calculated and measured data are in good agreement.
3.4 RESULTS OF TEST C-3 (100-kg Charge)
The initial visual indication of the propellant burn in Test C-3 was a
smoke plume projected some 1.5 meters beyond the end of the vent pipe within
approximately in 0.2 seconds. The plume of smoke and flame reached a length
of 16 m in approximately 6 seconds. The position of the leading edge of the
plume is plotted versus an arbiLtaLy Linik itk Figure 19. As shown in
Figure 18, the initial plume velocity was 5.58 m/sec, which was slightly
higher than seen on the first two experiments. Although it continued to burn
10
violently, the length of the plume began to decrease after 6 seconds,
retreating towards the end of the vent pipe. At approximately 11 seconds, a
violent gas exhaust was noted, which had an estimated velocity of 29.5 m/sec
and a duration of about one second. This sudden jet ripped up clods of earth
from the ground surface, throwing them into the air at velocities approaching
11 m/sec. The total duration of the external gas plume , including the late
jetting phenomena, was approximately 12 seconds. The orange residual vapor
observed after Test C-1 was again observed after burning of the Test C-3
propellant charge ceased, although it did not persist once ventilation of the
bunker was begun.
Measured peak pressure and thermal data are presented in Table 8. Peak
side-on overpressures (Figure 20) produced by the burning of the 100-kg
propellant charge were still low compared to predictions. The data presented
in Figure 19 show a consistent trend of decreased side-on overpressure with
distance from the center of the bunker. The attenuation rate increases beyond
the end of the vent pipe, where the jet was allowed to expand in three
dimensions. The results still indicated that uncombusted gas and unburned
propellant are carried outside by the gas plume for external burning. Once
again, when the bunker was reentered, the propellant charge container
(cardboard box) was found to be charred but not destroyed, indicating a
deficiency of surplus oxygen during deflagration. The video recording showed
the presence of a pulsing flame in the gas plume released through the vent
pipe.
Thermal flux values recorded at the mid-point of the vent pipe (Gage
TFI91) were again matched with dT/dt values from the thermocouple gage,as
shown in Figure 21. An eyeball-fitted line was forced through the point
(dT/dt) = 0 and Q = 3.459 cal/m 2-sec. The calculated pseudo-thermal flux
(Gage THCI90) for the chamber is compared with the measured flux in the vent
pipe (Gages TF191 and TF192) in Figure 22. As shown here, the calculated and
measured data are in good agreement. All three time-histories show the pres-
ence of a later peak at about 15 seconds after initiation. This peak occurs
in the vent pipe first, indicating movement back into the chamber from the
free-field outside the bunker. This is postulated to be an indication of
reignition of hot gages, progressing from the exterior back into the bunker.
11
3.5 RESULTS OF TEST C-4 (250-kg Charge)
The initial visual indication of the propellant burn for Test C-4 was a
smoke plune projected some 1.3 meters beyond the end of the vent pipe within
approximately in 0.3 seconds. The plume of smoke and flame quickly extended
from the vent, filling the video field of view (a distance greater than 25 m)
in approximately 5.3 seconds. The position of the leading edge of the plume
is plotted versus an arbitrary time in Figure 23. The initial plume velocity
was 3.88 m/sec, which is slightly higher than seen on the first two ex-
periments but less than that measured from Test C-3. Shortly afterwards (at
approximately 6 sec), the structure failed, releasing all internal pressure in
the process. The remaining unburned propellant then burned rapidly in the
oxygen-rich outside air.
In Test C-4, the Horn Antenna Bunker clearly failed from excess internal
pressure. Visual observation of the post-test structure showed that the
concrete bond to the reinforcing rods had failed, and the rods were pulled out
of the concrete. Only a small number of rods showed necked-down sections
characteristic of tensile failure of the steel. At the time of failure, the
hatch cover and roof section were hurled high into the air. The video record
shows the hatch cover, although tumbling, moving with an average velocity
upward velocity of 33.3 m/sec shortly after failure. Similarly, the roof
section moved upward at an average velocity of 11.4 m/sec.
Measured peak pressure and thermal data for Test C-4 are presented in
Table 9. Peak side-on overpressures (Figure 24) produced by the burning of
the 250-kg propellant charge were the highest measured in this test series,
but still seemed relatively low by weapons effects standards. The data
presented in Figure 24 shows a consistent trend of decreasing side-on
overpressure with distance from the center of the bunker. The attenuation
rate increases beyond the end of the vent pipe, where the jet was allowed to
expand i~n three dimensions.
12
SECTION 4
ANALYSIS OF RESULTS
The peak overpressures measured in the Phase C tests are plotted versus
distance from the center of the burn chamber in Figure 25. Least squares fit
lines are shown for Tests C-1 and C-3 (vent tube and free-field data).
Average peak pressures are plotted in Figure 25 for the overpressure
measurements in the chamber and water-filled cylinder. The measured peak
chamber pressures are plotted versus the chamber loading densities in
Figure 26.
The Ballistic Research Laboratories (BRL) conducted a series of
experiments modeling the KA-Ill/Phase C experiments prior to the actual tests.
The model chamber was 25.4 cm in diameter by 184 cm long, with a volume of
93180 cm3 (0.93 M3). The vent tube was 10 cm in diameter by 257 cm long, with
a volume of 2047 cm3. Venting was further restricted at the chamber/tube
interface by a 5.1 cm diameter opening. The BRL data (unpublished) is shown
for comparison in Figure 26. A significant difference is seen in the model
results between experiments using one-point ignition and three-point ignition.
The additional ignition points increased the energy release rate, which
apparently increased the measured peak overpressures. As seen in Figure 26,
the model and prototype results from experiments using one-point ignition are
in good agreement.
The pressures measured at the end of the vent pipe for each test are
plotted versus loading density in Figure 27. Peak exit pressure increases as
the loading density to the 1.653 power, for loading densities grelter than
5 kg/m 3. For loading densities below 5 kg/m3, the relatively large chamber
volume appears to inhibit the exit pressures.
Figure 28 is a plot of peak total pressure versus distance from the
center of the M-i propellant charge. Total-pressure gages were positioned
outside the bunker along the extended vent pipe centerline to measure jetting
effects. The side-on pressure gage located at the same range as the
successful total-pressure measurement (Gage ABEl78) on Test C-3 was
over-driven, indicating an overpressure in excess of 70 kPa. For Test C-4,
the side-on pressure gage at the same 0.9 m location as the total-pressure
13
gage recorded a peak of 34.5 kPa, which appears to be abnormally low when
compared to the data trend. Therefore, these total-pressure measurements
indicate that jetting is not a significant problem compared to the fire and
gas plume hazards outside the vent tube.
Figure 29 gives a comparison of thermal flux versus distance from the
center of M-1 propellant charge. Chamber thermal flux is calculated from the
thermocouple records. The thermocouple was located beneath the bunker hatch
cover, directly above the charge. This distance was approximately 1.5 m above
the charge surface. The thermal flux measurements from Test C-4 were
over-driven, so the actual peak data are somewhat greater. The peak thermal
flux data in Figure 29 shows the effects of loading density and distance from
the source. Thermal flux increased with increasing propellant loading density
and, at any particular loading density, the flux decreased with distance.
Thermal flux is plotted versus loading density in Figure 30. The
calculated chamber thermal flux indicates that the energy release increased in
almost linear proportion to the propellant loading density. The vent pipe
measurements show a two-slope relation, with a lower flux gradient at lower
loading densities (< 5 kg/m3). At greater loading densities, the curve
essentially parallels the thermal flux-loading density relation for the
chamber.
Chamber temperature is plotted versus propellant loading density in
Figure 31. Temperature data from the BRL model tests are included in
Figure 31 for comparison. The KA-III chamber temperature measurements were
made at the the mocouple location; i.e., beneath the bunker hatch cover
directly above the center of the propellant charge. Thermocouples for the BRL
model experiments were located at the chamber wall. As shown in Figure 31,
the number of ignition points influenced peak chamber temperature. The model
test data also indicates an increase in temperature with loading density.
This trend is not seen in the KA-III data.
14
SECTION 5
CONCLUSIONS
While the peak overpressures measured during the KA-Ill/Phase C
experiments were relatively low, these experiments demonstrate that a serious
flame and gas venting problem exists in front of a storage chamber exit. The
catastrophic failure of the bunker roof from Test C-4 indicates that
structural failure may occur, releasing the gas pressures from a propellant
burn before the internal pressures can build enough to cause a transition from
a deflagration to a detonation.
The pressures generated are a direct function of the loading density. It
is suggested that, when M-I propellant is stored in underground facilities
with sufficient overburden to prevent cover venting, an accidental burn will
produce far greater overpressures at loading densities above 50 kg/m3 than was
indicated by the KA-II/Phase C Tests. Rupture of the bunker roof
substantially reduced the pressures generated by Test C-4.
Chamber overpressures are also a function of the number of burn ignition
points. The BRL model tests demonstrated that higher pressures are generated
when more than one ignition point is used. Exit pressures are a function of
chamber volume, below a loading density of 5 kg/m3 . The test data indicates a
similar volume relation exists for thermal flux at loading densities below
5 kg/m3. The peak chamber temperatures measured in the KA-Ill/Phase C tests
were essentially constant, irrespective of loading density.
15
SECTION 6
RECOMMENDATIONS
Additional testing should be done to investigate the effect of gas
pressures from propellant burns in underground storage situations where cover
rupture will not occur. These tests should include a measurement system to
collect data on heat release rate (related to the change in mass of the
unburned propellant with respect to time) of the propellant burn. This
quantity is proportional to the product of the burn rate and propellant
surface area. These data are required to fully assess the influence of the
surface burn area on the deflagration gas pressures generated.
16
REFERENCES
Herrera, William R., Vargas, Luis M., Bowles, Patricia M., Baker, Dr. WilfredE., "A Study of Fire Hazards from Combustible Ammunition, Effects of Scale andConfinement (Phase II)," Final Report, December 1984, Southwest ResearchInstitute, San Antonio, Texas 78284
Zardos, Steve; unpublished data (personal communication), US Army LaboratoryCommand, Ballistic Research Laboratory, Aberdeen Proving Ground, Maryland21005-5066
17
PERMANENT HIGH EXPLOSIVE TEST SITE
IUP LAUNCHERE XPERIMENT
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18
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19
Figure 3. Test C-2 charge (25 kg of M-l propellant) placedin a cardboard box on the floor of bunker withbooster (electric match surrounded by 50 gm ofp~stol powder) laid on the surface of the charge.
Figue /* T~t . 3har (100 kg, ot M-1 propellant) placed
n tom- c ardbilard boxes t aped t oget her , with11OStt or Ilaid on the surface of the charge.
20
S ti ' 3. (h~mLbc, p- pre,-re j e runt (ABI 180) directlv
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Figure 7. Vent pipe with one free-field, side-onoverpressure gage (ABEl73). Cables are seen
for two internal vent pipe transducers; thermalflux gage (TF192, left) and side-on overpressure
gage (ABEl72).
22
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Figure Ii. Test C-I: length of exhaust gas plume (from end of ventpipe) as a function of relative time. Zero-time was notrecorded, so all times are relative to an arbitrarilychosen start time.
26
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Figure 12. Test C-i: measured peak pressures as a function ofdistance from the center of the 10-kg M-i propellantcharge.
27
TEST C-idT/dt - DIFFERENTIAL OF CHAMBER TEMPERATURE (THC190)
30 q - THERMAL FLUX (TF191), cal/rn-sec0
25
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Figure 13. Test C-i: thermal flux at mid-length in the vent pipe(Gage TF1l9) versus the differential of measuredtemperature (Gage THCl90) with respect to time. Each datapoint represents a "pair" of values; an x-value from agiven dT/dt, and a y-value from the thermal flux recordcorresponding to the same time instant (after zero time)as the dT/dt value.
28
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CO $
41 0%0 E-4
U~~ 1*0 _ _
E -
Cd4.)
4)0 "~4
413
V~ 0
0 41~
'-4
U - 140
00 0C0 0 0 0U') mqC Cuj
-4)
'.4
-'.4
29
12 TEST C-2
5 kg/m3
N-1 PROPELLANT
E10 -
0
Z8-HN-
0 2/3 -N 4 -
2
0 " ,4
O2 0 4 6 8 10 12 14 16 1 20
TIME, secFigure 15. Test C-2: length of exhaust gas plume (from end of vent
pipe) as a function of relative time. Zero-time was notrecorded, so all times are relative to an arbitrarilychosen start time.
30
10 I I
TEST C-2 I I5 5kg/m3 I
M-1 PROPELLANT 1 0
: .I I
0 AGE LOCATIONS I I i
oFree-Reld
I '1 10
DISTANCE, rmFigure 16. Test C-2: measured peak pressures as a function of
distance from the center of the 25-kg M-1 propellantcharge.
31
m • • l n i m mu n n l
50
q = 0.6090 (dT/dt) + 3.459
U 4 0
E30
00 00
D~ 10v-j
0-j
-10 NTEST C-2-0 dT/dt - DIFFERENTIAL OF CHAMBER TEMPERATURE (THC190)
q -THERMAL FLUX (TF1 91 ), cal/ma-sec
dT/dt
Figure 17. Test C-2: thermal flux at mid-length in the vent pipe(Gage TF19l) versus the differential of measuredtemperature (Gage THCl90) with respect to time. Each datapoint represents a "pair" of values; an x-value from agiven dT/dt, and a y-value from the thermal flux recordcorresponding to the same time instant (after zero time)as the dT/dt value.
32
_ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _4-4 4)
m U
G4.
T:I r-4I- F- 020 r
.4
4)24
f~ 0 -4
- 0 E-4
r 4 0 C%
44O 44E U
~oo
Z. 0.JJJ
>r4 . 4)
o 4 2
V-4
0
O 0. C
000O 0 0 0 0
I -4
44
D~~S-~UI/TjD I~lI IVNHHH1
33
18 r Event ;-320 kg/m
M-1 Propellant
Fireball
.14-uJZ12
W510
Sr LATE STAGE JET
6-
I2- I
0 2 0 2 4 6 8 1'2
TIME, sec
Figure 19. Test C-3: length of exhaust gas plume (from end of ventpipe) as a function of relative time. Zero-time was notrecorded, so all times are relative to an arbitrarilychosen start time.
34
I S
103-
D. ~iI
TEST C-3 Io 20 kg/=3
0. . M-1 PROPELLANT I
LU
V) I(n 0
> GAGE LOCATIONS IO I1 0 * Fre-Field
a Vent pipe I>& Chamber Wall I0
Li * Water-Filled Cylinder
II
0-1 10DISTANCE. m
Figure 20. Test C-3: measured peak pressures as a function ofdistance from the center of the 100-kg M-1 propellantcharge.
35
1500
o q = 4.145 (dT/dt) + 3.459
0
N 100E
0
50 0o
0 0
x 0
0 P
~-50Li
TEST C-3dT/dt - DIFFERENTIAL OF CHAMBER TEMPERATURE (THC190)
q - THERMAL FLUX (TF191), cal/m 2 -sec
-1 0 0 -0 0 2 400 8 0dT/dt
Figure 21. Test C-3: thermal flux at mid-length in the vent pipe(Gage TFgl9) versus the differential of measuredtemperature (Gage THCl90) with respect to time. Each datapoint represents a "pair" of values; an x-value from agiven dT/dt, and a y-value from the thermal flux recordcorresponding to the same time instant (after zero time)as the dT/dt value.
36
4-4 4)
~LLLL (AI-___ __LOa
CC
cu 0 -4l-.44
0) A.E4.4 0 '-4
T-4 E-o
(C)4 0"-4
E4 41 -4 -4 (
___ __ __ .~ 4)
EA 0
:3 ) Ia.f4).M"
I. 4)
-4
37O
16TEST C-4SO kg/ 3
1 4 M-1 PROPELLANT
14-Fireball
12 0i oCOO,
10 0
Z 8
VHatch Cover
56
Bunker Roof4
2
_02 468TIME, sec
Figure 23. Test C-4: length of exhaust gas plume (from end of ventpipe) as a function of relative time. Zero-time was notrecorded, so all times are relative to an arbitrarilychosen start time.
38
10 4
I I
TEST C-4 Io 50 kg/ 3
0.. 1-1 PROPELLANT
II
.10 3-o
"biiV)
CL
LJ GAGE LOCATIONSo
lo = o Free-Fleidloll a Vent pipe .1
a Chamber Wall IlJ 0 Water-Flled Cylinder
I I©1
II S I I m II I I , , I i ,Ii
1%441
1 10DISTANCE, m
Figure 24. Test C-4: measured peak pressures as a function ofdistance from the center of the 250-kg M-1 propellantcharge.
39
I!I10
4 -
(I)0
i'I
LiLJ
Q- 10
a..uIGi
(1. 4.-kg/rnI ILIJ-
I~l
:i , i | I i I I i -- I I i I 1- ii
0 I1I I10DISTANCE,
Figure 25. Peak overpressure versus distance from the center of the
M-l propellant charge, KA-Ill, Phase C.
40
CHAMBER
0~0
0103-
Uf) P 0.5502 (Q /V) 0bJ
a_
010 2
NUMBEROF IGNITERS
o KA-IlI. 1 Igniter0 BRL Model, 1 IgniterA BRI Model. 3 Igniters
10 1 10 10 2
LOADING DENSITY, kg/rnFigure 26. Peak chamber pressure versus M-1 propellant loading
density, KA-ITI, Phase C; comparison with previous datafrom BRL tests with one and three ignition points ofpropellant charge.
41
10 -
o ~VW PMP EXICL PRESSURE
wD10
(/)
IL
LUJ
10 = 0.6156 (Q V ,)1 -65
10 10LOADING DENSITY, kg/r 3
Figure 27. Peak overpressure at end of vent pipe versus chamberloading density; KA-Ill, Phase C.
42
103
0
I 50• 0 kg/=3
(nI I
IJ
a- Ios 20Ig
..
0I-- ['"GAGE LOCATIONS
11
DISIANCE, m
Figure 28. Peak total free-field pressure versus distance from thecenter of the M-1 propellant charge, KA-, Phase C.
43
I iBH Hiin l n a aan anIli n l I
03
5kg/n 3
Ij 2.---. 5
1E-11DITNE0
Fiue2.Pa hra lxvru itnefo h etro hM-1 ropllat carge KAM, has C. ote chmbe
thra lxdt r acuae rmtemculmesueens
-44
1 0 3
U (Overdriven Data Points)4)U)
N /
E_ .//t
4L'4t
~10 1~
"--Il, /e
45
'< /
I
11 10 10'LOADING DENSITY, kg/rn3
Figure 30. Peak thermal flux versus M-l propellant loading density,KA-III, Phase C.
45
103& Oft ME de. 3 lontif/
~/a OM Modl. 1 Igniter
(0 KA-11
LL
Ix"0
2DFCHAMBER
LIJ NUMBEROF IGNITERS
W 0 KA-III, 1 Igniter0 BRL Model. 1 IgniterA BRL Model. 3 Igniters
1 i i i i ia ii p 1 a ill1 0 103LOADING DENSITY, kg/r 3
Figure 31. Peak chamber temperature versus loading density, KA-III,Phase C; comparison with previous data from BRL model testwith one and three ignition points of propellant charge.
46
Table 1 KA III, Phase C: Configuration Parameters for M-1 PropellantCharges
Charge Surface AreaCharge Surface Charge To VolumeWeight Area Volume Ratio
Test Aky-L (M2) - (Mn3 ) (fir1)
C-1 10 0.1334 0.01771 7.796
c-2 25 0.1334 0.04277 3.118
C-3 100 0.5335 0.1771 3.118
C-4 250 1.95* 0.4277 4.547
*Estimnated
47
0 1
. 0 0 0 0 0 0 0 0 0 ,
U 0>
1(
L) 4
CCa
4) 41 4)
41 0 0 ( -A (A (A Wfa A
CU CL a. IL 9L IL ID U (
w ) 0 w 0 u uA 0 u
'0 '0IL)
4141 141 1 4141 4 41 1 >0~ j L L L L 1 1 I. L L L L
0U C CD L tv Lr L L c
"L L L L L f- L
a o 0 0 0 0 0 0 L L L La. a. a. a. a. a.' a. a.15
c c
0) > -> 4 >U >4'- '- U U ~ > . > ) . . 4
w '0 'O 0'If 0.. Ki -
(Uk (U. 0. (U. IL CL z. .
.2 u01 m1 Cl QC W! 41 41 W! 4
ig 414141 141 C41 ZLL Z 14
(U LnLn VC., 41
V (U
1 L
L 1- (U ( (U U ~ U48
-4,,
4,~0 60 0 In 00 0 u ~ .
0 -- 0 (A W (0 M (A-o a>
00W
U, 'A)
- u~ u ci c, u u* 2 x~
41 v v 4j 4.41 4
C .I. L IL CL C 41L L L L L L L L
00 )
W! 0: Lf L
4.1 4, 4*
~~~6 4, 4 , jL
0 Lu
It -* -&nL. 9) L
C) C
In L
4) 4
-~~~~I .IZOA ;
n-t - 0 - - - -n t- - ~ O
4, 40
lw a U0 a a a a . a .a .C 0 3 C a in a. a. in
A L" M ~ -
Y± a 0 0 L 0 CL a
0, 4 , , 4 4, Co Co 404 , (4, 4,0, 4, u
~ IL3 L Lt L. L. U 0 IU UL~ E IU U
LA .
o 01 4- 4- IS 5 U
to L A w w. L, L) u L) u
S0 a 0
0S 0 0 0 . L- L - L
L) C.U
EE~~ EK EE O .
0 - CD, ~ -~ , 0 0
L - L L-5
4, 4p 4, 4, 4, 4
o > > .U .U .4,
, U)
>. &. &, 4 U m UL C L CL 0
a In .1,4 U! 4 , U %. . a
It %r 0
CotLA 't 'LA LA - 00
a- 00na nC
0 0 ~ A 0 - -- ; In a
I- I- 00 000 00 7
x' x x
I.-
50
0
0 0 41 4P 0 , 4, 0
AUU
41
us s ).0.0 0 0 0 0 a. 0. 0.0 00 0 00 0.
oL IL m C C I C I a. C' a
.-
0 . . 4. 4D on 6 '1 V
-~~C C 0 0 0 0 :A.
01 Z
w3 W
4.~Z f E - 4.4L4.*~~~ 7S 4 4~ . .
I-4 ~ 4. .-' L AL A I A 6 60x
x x x x A LI m;3 3
LiA L L A
In U
A.. 51
... .... .. ... .. .. .... 66
Table 6 Test C-I (Loading Density 2 kg/m3): Gage Location and Peak Measured Data.
Transducer
Designation Location Measurement Type Measured Peak Data
ABEl71 Vent Tube, 1.6 m from Portal Side-on Pressure <0.9 kPa
ABEl72 Vent Tube, 0.3 m from Portal Side-on Pressure <0.3 kPa
ABEl73 Free-Field, 0.3 m from Portal Side-on Pressure 5.6 kPa
ABEl74 Free-Field, 0.9 m from Portal Side-on Pressure 4.3 kPa
ABEl75 Free-Field, 2.1 m from Portal Side-on Pressure 2.1 kPa
ABE176 Free-Field, 4.5 m from Portal Side-on Pressure 1.3 Kpa
ABEl77 Free-Field, 0.9 m from Portal Total Pressure <0.7 kPa
ABE178 Free-Field, 2.1 m from Portal Total Pressure <1.0 kPa
ABI180 Front Wall of Chamber Chamber Pressure <1.4 kPa
ABI181B Right Wall of Chamber Chamber Pressure(1/3 Height)
ABI182 Back Wall of Chamber Chamber Pressure <1.5 kPa
ABI183T Right Wall of Chamber Chamber Pressure(2/3 Height)
ABI184 Water Filled Cylinder Chamber Pressure <1.0 kPa
ABI185 Water Filled Cylinder Chamber Pressure <1.0 kPa
ABI186 Water Filled Cylinder Chamber Pressure ----
1BI187 Water Filled Cylinder Chamber Pressure 290. kPa
ABI188 Water Filled Cylinder Chamber Pressure ----
THVlO Chamber Hatch Cover Chamber Temperature 630. °C
TF11 Vent Thbe, 1.6 m from Portal Thermal Flux 34. cal2-sec
TF192 Vent Tube, 0.3 m from Portal Thermal Flux 27. cal2-sec
Note: The digitizer sample rate was one sample per 220 micro-sec, for a total recordlength of 60 sec.
52
Table 7 Test C-2 (Loading Density 5 kg/m3): Gage Location and Peak Measured Data.
Transducer
Designation Location Measure!,nt Type Measured Peak Data
ABEl71 Vent Tube, 1.6 m from Portal Side-on Pressure <1.3 kPa
ABEl72 Vent Tube, 0.3 m from Portal Side-on Pressure <0.5 kPa
ABEl73 Free-Field, 0.3 m from Portal Side-on Pressure 6.4 kPa
ABE174 Free-Field, 0.9 m from Portal Side-on Pressure 7.1 kPa
ABE175 Free-Field, 2.1 m from Portal Side-on Pressure 3.5 kPa
ABE176 Free-Field, 4.5 m from Portal Side-on Pressure 6.4 Kpa
ABE177 Free-Field, 0.9 m from Portal Total Pressure <2.2 kPa
ABEl78 Free-Field, 2.1 m from Portal Total Pressure <1.9 kPa
ABI180 Front Wall of Chamber Chamber Pressure <4.0 kPa
ABI181B Right Wall of Chamber Chamber Pressure <3.4 kPa(1/3 Height)
ABI182 Back Wall of Chamber Chamber Pressure <4.0 kPa
ABI183T Right Wall of Chamber Chamber Pressure <2.7 kPa(2/3 Height)
ABI184 Water Filled Cylinder Chamber Pressure ----
ABI185 Water Filled Cylinder Chamber Pressure <6.7 kPa
ABI186 Water rilled Cylinder Chamber Pressure ----
IBI187 Water Filled Cylinder Chamber Pressure <13.5 kPa
ABI188 Water Filled Cylinder Chamber Pressure ----
THV190 Chamber Hatch Cover Chamber Temperature 604.OC
TF191 Vent Tube, 1.6 m from Portal Thermal Flux 42. cal2-sec
TF192 Vent Tube, 0.3 m from Portal Thermal Flux 34. cal2 -sec
Note: The digitizer sample rate was one sample per 220 micro-sec, for a total recordlength of 60 sec.
53
Table 8 Test C-3 (Loading Density 20 kg/m3): Gage Location and Peak Measured Data.
Transducer
Designation Location Measurement Type Measured Peak Data
ABEl71 Vent Tube, 1.6 m from Portal Side-on Pressure 335.kPa
ABE172 Vent Tube, 0.3 m from Portal Side-on Pressure 56.1kPa
ABE173 Free-Field, 0.3 m from Portal Side-on Pressure ----
ABEl74 Free-Field, 0.9 m from Portal Side-on Pressure 89.0 kPa
, BE175 Free-Field, 2.1 m from Portal Side-on Pressure >70.0 kPa
ABEl76 Free-Field, 4.5 m from Portal Side-on Pressure 11.2 Kpa
ABEl77 Free-Field, 0 9 m from Portal Total Pressure ----
ABEl78 Free-Field, 2.1 m from Portal Total Pressure 104. kPa
ABI180 Front Wall of Chamber Chamber Pressure 235. kPa
ABI181B Right Wall of Chamber Chaber Pressure 196.kPa(1/3 Height)
ABI182 Back Wall of Chamber Chamber Pressure 155. kPa
ABI183T Right Wall of Chamber Chamber Pressure ----
(2/3 Height)
ABI184 Water Filled Cylinder Chamber Pressure ----
ABI185 Water Filled Cylinder Chamber Pressure 155. kPa
ABI186 Water Filled Cylinder Chamber Pressure 135. kPa
1BI187 Water Filled Cylinder Chamber Pressure 145. kPa
&B1188 Water Filled Cylinder Chamber Pressure 69.0 kPa
THC190 Chamber Hatch Cover Chamber Temperature 616. °C
TF1l Vent Tube, 1.6 m from Portal Thermal Flux 220. cal/m -sec
TF192 Vent Tube, 0.3 m from Portal Thermal Flux 166. cal/m2-sec
Note: The digitizer sample rate was one sample per 220 micro-sec, for a total recordlength of 60 sec.
54
Table 9. Test C-4 (Loading Density 50 kg/m3): Gage Location and Peak Measured Data
Transducer
Designation Location Measurement Type Measured Peak Data
ABEl71 Vent Tube, 1.6 m from Portal Side-on Pressure >1400. kPa
ABEl72 Vent Tube, 0.3 m from Portal Side-on Pressure 350. kPa
ABEl73 Free-Field, 0.3 m from Portal Side-on Pressure 382. kPa
ABEl74 Free-Field, 0.9 m from Portal Side-on Pressure 34.5 kPa
ABE175 Free-Field, 2.1 m from Portal Side-on Pressure
ABEl76 Free-Field, 4.5 m from Portal Side-on Pressure
ABE177 Free-Field, 0.9 m from Portal Total Pressure 285. kPa
ABEl78 Free-Field, 2.1 m from Portal Total Pressure -
ABI18O Front Wall of Chamber Chamber Pressure ----
ABI181B Right Wall of Chamber Chamber Pressure 889. kPa(1/3 Height)
ABI182 Back Wall of Chamber Chamber Pressure 587. kPa
ABI183T Right Wall of Chamber Chamber Pressure 1833. kPa(2/3 Height)
ABI184 Water Filled Cylinder Chamber Pressure ----
ABI185 Water Filled Cylinder Chamber Pressure 840. kPa
ABI186 Water Filled Cylinder Chamber Pressure 722. kPa
1BI187 Water Filled Cylinder Chamber Pressure 545. kPa
ABI188 Water Filled Cylinder Chamber Pressure 298. kPa
THC190 Chamber Hatch Cover Chamber Temperature ----
TF191 Vent Tube, 1.6 m from Portal Thermal Flux >372. cal/m2-sec
TF192 Vent Tube, 0.3 m from Portal Thermal Flux >372. cal/m 2-sec
Note: The digitizer sample rate was one sample per 220 micro-sec, for a total recordlength of 60 sec.
55
APPENDIX Al
KA-III, PHASE C
TEST C-1
10 kg M-1 PROPELLANT BURN
DATA-TIME HISTORIES
56
C3
,0 00
oa 0 0
00 0
co a
e r=
>C C[
-- 0I
C~
0 -L
xw
4- -
(n
L C
-
00
o0 0 0 00 0 0 0 00o 00
(led) anSSa~1duaAO
57
0 00
0 010 0
00 0
0 0
40 0 IN II
fnJ
0
cu
C~
L IonI W C
-- o0
AI-)
(n
LL
0co %
58.
IMPULSE (kPa x sec)
Co a4 a 0 0 0 0 0C. (D 03 003 0 0 0 0
p 0P
a CM v E
0 w0
m in
NL W> m
C a)
c- C.)
a Ij* c w49I - I
* ( (nm
co 3
E- L
/ 44
0 in
>4l N C
/ C-uda~
H C-59
IMPULSE (kPa sec)
o 0 00 0 00000
fn0
.0 EII" 0
ru 7
0 0 E
w r'0
X- 0 -
CU :
0 _O
-. 0)
42 0)L
-. ~ co 2.42j~ 42 /42 w
COD ( (n
L C
00
(0
0C 0L :3
C-* 7I C
60(
IMPULSE (kPa x sec)
.0-
0(n
C : Cu.u
01 5
x 01
x 7nU -9
CL cux.
X. CMuxi
z ~, -0.4-41c
a)
w a)
0 c0
L (13<- U
zxaw
to C,
cn
oo
0 U)cu 0
7L
(edx)aunssuciaa
61z
IMPULSE (kPa ~Esec)
o 0 0 0 0
0 0
it 0~
0. 0. a
inwE
c a)-4-
0. CU (n :
CC
%D
00 0 0
ul 0 tn 0
(RC13 H~n~q~dlH3A62C
(2 00(1
C, 0C,0. aC
cuu
- 0A
0) 003>
0-
U-
00
0 M
-J-(1)
441
_ _ xwC
00
1-4
ONl
40 I 'n_______
0 0 0 C-'
_____ ____ 463
m CL 0
00 0v 0n0u0 7
- 0
0 0
> CE
U'
C Dua _ _ _ _ _ _ _ _ _ _ _ _ _L
Fc
4 _ _ _ _ _ _ _ _ _ _ _ _ _ _C) _ _ _ _ _ _ _ _ _ _ _ _ _Lo~~~E
Z__ __ _ _ __ _-
00
03 4
0 Ul 0
644
0. C.
in G
(1v 0j
40 tv
- LL
> 0O
C-D
c'"a a
o 0oF 0
I-I C.CL
0 01
ru 0 0
00
(Rdx)aunss~d~I0
650
00 00.00-0t0
C, 0
00
00 x
- 04
000
a,
-4-0
a a)
C-L CL
0 fnUl 1 0 F
001ex 2 isauua_ _ _ _ _ _ _ _ 66
* ru
00
0 0n
4,1
MI 1 0
(lJn
zc
a))
1-4
CD Cinm
(VdX)- allS(-daA
67-
IMPULSE (kPa sec)
o 00 00 0 0 0o o a a a 000 0 0o a0 0 0 0o 0 0 a 0
Qnj
Eto 0
" 0L
co CP (1
x /uZ) 0
E VI' /
10
in W
C- rrj
4Ji
C
cn
m a)
C2-
0
0 0 0
0 0dlU-,
68
00
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o o
Mi
- a0
0 CD
U -1
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c i-02
o E Ea
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ci.
044
020,-
4-I
In C, U
(sn~~slao 020p)adrvada
>49
0.0-~
0 0
0 C
* -4
0 -:
cu ai
4, 4, 0
- = 41
4, 4,X-.
D.
*o LL
(J U
0 00
0 C0
00
on 0>to o Qi
G LL
4-
co >
41 04"
x
4) 0)
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4,4
CD 0
o G
XnqA IVM3H
71D
APPENDIX A2
KA-III, PHASE C
TEST C-2
25 kg M-1 PROPELLANT BURN
DATA-TIME HISTORIES
72
CL Q.
2i -
a ai
F--
D E
* CD
2:3
4J4
< wj0))
mI-I cloC
4 EnC L
0 (
0 ~
a:)
zra(
0 0
ceam amnsaucma0
730
0
0 0.0
o 0 0
0 0
0 0
0 010 0O00
go~
100
0
> CO
(In
C :DL (U
0 3J
* 4 1x
a)>1 L
0 L2
aa
nL
0 0 C<D 0 0z0 02
74L
IMPULSE (kPa *see)
o 0 C
o 0 0in00
o 0 0 0 0o 0 07
1EE3j Ixa
Ln-
240.
>0 CO-
C DL ro
x - I
xLLJ
aaIL
0 U)
>4w <
0
cu c r0m
I-I ci
(Vdm)aunssadsaI
/5
IMPULSE (kPa sec)
0 0 0 0 3 000o000 0 0 0
o 0 0 0 0 0 00oo Wu CU
0(f
0 0
r- -O
0 in
f1 u/
~> C O
CO
!-41- di
OD C4cJ
S x n
LnL
m
0L
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(Rd~) alnS~ad~aA
o70
IMPULSE (kPa sec)
o 0 0000
o00 0 0
.1
in in/I
10
LU <
C D- S p
aa
41 L
cnco
LU
00
In4
C.3)
CeJX)a~n9SHJ~aA
77 Z
IMPULSE (kPa sec)
o 0 0 0
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to Im
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>m_on LU .
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to 0
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aJ 4
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(ram)~- amsa]~~
____I 87
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903
APPENDIX A3
K%-IlI, PHASE C
TEST C-3
100 kg M-1 PROPELLANT BURN
DATA-TIME HISTORIES
91
IMPULSE (kPa x* sec)o 0 00
oCo 0 0 0 3 C 0o~C 0
0 40a
o ~ c 0 000O
0 0 0 at
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C:(D 0. L> M
C'
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z
uu
m
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______________ L92
IMPULSE (kPa sec)
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0 C3
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> CD
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(no -1 (
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95
(nV
cn wto0
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tot~
_ _ _ _ _ _96
IMPULSE (kPa *sec)
o 0 0 000 0 000
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C w 0
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IMPULSE (kPa * see)
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('RdX 2=SH~d rVJAX
98)
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IMPULSE (kPa *sec)
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100
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1024
IMPULSE (kPa sec)
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0 0o0 0 000
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InI-xnqa vW~aw
108u
APPENDIX A4
KA-Ill, PHASE C
TEST C-4
250 kg M-1 PROPELLANT BURN
DATA-TIME HISTORIES
109
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o~ o 0
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w 0
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(1)
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110-
IMPULSE (kPa sec)
0 0 00
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11
(-
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C
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(led) R~S9Z~l~aA
112
IMPULSE (kPa sec)
o 0 0 a 0a 0 000o 0 00 00 0! 000
in 0 0i 0 0W irig Mi -u - -ug
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IMPULSE (kPa ~*sec)
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117
IMPULSE (kPa ~*sec)
0 00 00 0 0o0 0 004 o 0R
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c CO
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IMPULSE (kPa ~*sec 1000)
o 00 00 0
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119u
IMPULSE (kPa sec)
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o 0o 0 ni
o 0 a i 0L
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120
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o An m0 d
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(12d%)~C MSS,(A
1224
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o
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0 0 0
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