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MHSMP-80-63 Dist. Category UC-
SELECTED PHYSICAL AND THERMAL PROPERTIES OF \VARIOUS FORMULATIONS OF SILICONE POTTING COMPOUNDS
Gasiy L. Tlowzsa Bill V. faablon
Jackit L. Montague. Su6an T. SmXzzn.
ofic EUCT£ 0l®usims
November 1980 ;"■■-. i
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19951214 081 iriü->*:s'-''-|fi?iii.SSi
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Process Development Endeavor No. 102
K ^31«
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OPERATED FOR THE
P. O. BOX 30020 AMARiLLQ, TEXAS 79177
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DE-ÄC04-76ÖP-ÖC487
NOTICE
This report was prepared as an account of work sponsored by the United States Government. Neither the United States nor the United States Department of Energy, nor their employees, nor any of their contractors, subcontractors, or their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness or usefulness of any information, apparatus, product or process disclosed, or represents that its use would not infringe pri- vately-owned rights.
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-- 1 - AD NUMBER: 0433398 -- 5 - CORPORATE AUTHOR: MASON AND HANGER-SILAS MASON CO INC AMARILLO TEX
PANTEX PLANT - 6 - UNCLASSIFIED TITLE: SELECTED PHYSICAL AND THERMAL PROPERTIES OF
— "VARIOUS f^RtWLATIONS-OF SI1IC0NE POTTING COMPOUNDS, -10 - PERSONAL AUTHORS: FL0WERS.6. L. ;FAUBION,B. D. ;MONTAGUE,J. L. ;
SWITZER.S. T. ; -II - REPORT DATE: • NOV , 1980 -12 - PAGINATION: 18P -14 - REPORT NUMBER: MHSMP-80-63 -15- CONTRACT NUMBER: AC04-76DP-00487 -20- REPORT CLASSIFICATION: UNCLASSIFIED -22 - LIMITATIONS (ALPHA): APPROVED FOR PUBLIC RELEASE; DISTRIBUTION
.UHLIMITED.-HUIiTllinTITTY- HUTHIInb TiilDIICAL DirOWIATHII »(WlCEi ■cpniHoriCLD, 'I'I'I. cami IIIIOIIP OI a.
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SELECTED PHYSICAL AND THERMAL PROPERTIES OF VARIOUS FORMULATIONS OF SILICONE POTTING COMPOUNDS
Gcuty L. flowoAA Billy V. Taubion.
Jackie. L. Montague. Sub an T. SwiXzeA
NOVEMBER 1980
Process Development Endeavor No. 102
INTRODUCTION
When Dow Corning discontinued production of several of their addition cured silicone potting compounds used by the DOE complex, it became necessary to develop alternate or substitute materials. This task was undertaken jointly by the Lawrence Livermore National Laboratory (LLNL) and Pantex. Several substitutes were developed and tested at both facilities. Much of this work has been reported previously^, 2., 3,4,5,5,7) This report deals with some of the physical and thermal properties of many of these substitutes as well as some of the starting materials.
These substitutes were originally developed as replacements for 93-119, 93-120, 93-122 and mixtures of 93-119/93-120 and 93-119/93-122a. These substitutes are based on combining various quantities of any or all of six raw materials. These materials include:
Sylgard 186a - Silicone dioxide filled, high viscosity, slow curing, high strength, two part RTV.
Sylgard 184a - Medium viscosity, slow curing, high strength, two part RTV.
Q3-6527 Dielectric Gela- Low viscosity, very slow curing, very low strength,
two part RTV.
aProduat of Bow Corning3 Midland, Michigan
-1-
Q3-6559 Accelerator
a
DC-1107
Cabosil MS-75^
.a
Low viscosity, vinyl terminated polydimethylsiloxane fluid containing a large concentration of a platinum catalyst.
Low viscosity, silane hydrogen terminated poly- dimethylsiloxane fluid used as an accelerator.
- Silicon dioxide filler.
For this particular study, 19 formulations were selected. They include raw material only formulations as well as formulations of products currently in use by the DOE and products considered for future use by the DOE. The test data reported here are comprised of the following categories:
PHYSICAL PROPERTIES
Disk or punch shear strength Lap shear strength Butt tensile strength Compressive strength Bulk tensile strength Durometer hardness Dynamic shear modulus Density Crosslink density
THERMAL PROPERTIES
Coefficient of thermal expansion Thermal conductivity Specific heat Thermal diffusivity
All samples were prepared and cured at 25 C. unless otherwise stated, all samples were tested at 25 C after a minimum cure time of 30 days.
aProduat of Dow Corning, Midland, Miahigan
^Product of Cabot Coloration
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*
Physical Properties
DISC OR PUNCH SHEAR STRENGTH
The punch shear test (similar to ASTM 0732) employed a 1.59 mm thick test sample located between a punch and die. The punch sheared the sample into the die at a rate of 1.27 mra/min during testing.
Standard Standard Material Average Deviation Material Average Deviation Number (KPa) (KPa) Number (KPa) (KPa)
1 1100 85 11 2314 135 2 1178 34 12 3057 157 3 1514 53 13 938 43 4 1381 36 14 1782 57 5 1553 37 15 1789 136 6 1774 91 16 1462 22 7 1831 46 17 2292 54 8 2174 62 18 1941 49 9 1602 35 19 - -
10 1760 44
NOTE: Sample Size n = 5
LAP SHEAR STRENGTH
The lap shear test (ASM D-1002) employed two aluminum panels (25.4 mm x 101.6 ram) which overlapped 12.7 mm with an adhesive thickness of 0.127 mm. These assemblies were tested in shear at a rate of 1.27 mm/min.
Standard Material Average Deviation Number (KPa) (KPa)
NOTE: Sample Size n = 5
Standard Material Average Deviation Number (KPa) (KPa)
1 167 16 11 _ _
2 - - 12 - -
3 322 72 13 - -
4 157 26 14 329 51 5 209 8 15 151 18 6 192 20 16 - -
7 - - 17 374 65 8 363 66 18 - -
9 357 93 19 - -
10 475 92
-5-
BUTT TENSILE STRENGTH
The butt tensile test (ASTM D-2094) employed two aluminum cylinders (28.66 mm diameter x 38.1 mm high) butt bonded with an 0.127 mm thick adhesive bond. These samples were then tested to failure in tension at a rate of 1.27 mm/min.
Standard Standard Material Average Deviation Material Average Deviation Number (KPa) CKPa) Number CKPa) CKPa)
1 1293 163 11 _ .
2 - - 12 - - 3 1666 424 13 - - 4 1708 189 14 2508 270 5 946 80 15 1329 140 6 971 90 16 3575 - 7 - - 17 3575 345 8 1923 174 18 - - 9 3178 451 19 - -
10 3026 486
NOTE: Sample Size n = 5
COHPRESSIVE STRENGTH
The compressive strength test was performed on cylindrical test speci- mens 20.27 mm diameter x 25.4 mm high. These were tested to failure in compression at a compression rate of 2.5 mm/min.
Standard Standard Material Average Deviation Material Average Deviation Number CKPa) (KPa) Number (KPa) (KPa)
1 23.1 10.3. 11 _ _
2 33.3 13.4 12 - - 3 42.9 5.3 13 - - 4 73.2 20.4 14 45.7 5.6 5 76.8 7.9 15 58.3 7.5 6 76.5 13.0 16 59.4 6.7 7 200.0 32.9 17 276.0 - 8 7.9 1.5 18 276.0 - 9 104.1 13.7 19 1.0 0.49
10 182.2 27.8
NOTE: Sample Size n - 5
-6-
DUROHETER HARDNESS
Durometer hardness was determined via a Shore A2 durometer according to ASTM D-1706. The samples were 25.4 mm x 25.4 mm x 6.35 mm patties.
Material Average Material Average Number 24 Hours 30 Days Number 24 Hours 30 Days
1 37.6 49.5 11 31.0 37.0 2 31.2 44.5 12 44.7 54.5 3 31.3 44.0 13 35.5 45.0 4 29.7 38.5 14 33.6 49.0 5 26.9 36.5 15 34.3 46.0 6 29.1 41.0 16 29.7 41.5 7 28.2 39.0 17 24.4 40.0 8 40.6 52.0 18 11.0 35.0 9 26.6 35.0 19 20.9 33.5
10 13.1 36.5
DYNAHIC SHEAR MODULUS
A Rheometrics 7200 Mechanical Spectrometer was employed for all measure- ments. The test specimens were 25.4 mm diameter X 5.7 mm high disks clamped under load between two parallel plates with serrated faces. The top plate oscillated clockwise/counterclockwise at a selected frequency while the lower plate (to which the load and torque transducers were attached) remained stationary. For a given sample, the following test parameters could be varied; clamping load, test temperature, oscillation frequency and maximum strain amplitude. Since the shear modulus is essentially independent of strain amplitude as long as strain amplitude is small and the material is in the linear portion of the viscoelastic curve, a small strain amplitude of 0.5% was selected. Since oscillation frequency can be changed quite readily, an automatic scan from 100 mhz to 10 hz was selected. Temperature is very time consuming to vary so three temperatures were selected; -40, 25 and 100 C. Load plays a very important part in determining modulus, i.e., as load increases, so does the modulus. Therefore, load was varied from 100 to 2000 g or 0.204 to 4.074 g/mm2. Fig. 1 shows a typical modulus versus clamping load for material No. 15 tested at 1 hz.
-7-
2.0 4.0 6.0
Storage Modulus G'(X 10"s dynes/cm2)
Fig. 1. Storage Modulus (G*) Versus Clamping Load for Material No. 15
3.0
Modulus normally decreases rapidly above the glass transition point as the temperature increases. Therefore, several questions arose when the 100 C curve consistently had a higher modulus than either 25 or -40 C. This occurred for several materials. A special run was made on material No. 15 where a constant load of 2000 g, strain amplitude of 0.5%, and a
test frequency of 1 hz was used and the temperature was varied from -140 to 100 C. These data, shown in Fig. 2, explain why the storage modulus at 100 C was greater than the storage modulus at either 25 or -40 C.
-60 20
Temperature CC)
Fig. 2. Modulii Versus Temperature for Material No. IS
It was decided that for a comparison test between samples that the following parameters should be chosen; maximum strain amplitude of 0.5 percent, clamping load of 1000 g or 2.037 g/mm2, test frequency of 1 hz
and a test temperature of 25 C. Under these conditions, the following data were generated. Some data were also available at these conditions except at -40 and 100 C.
Storage Shear Modulus Loss Shear Modulus Material G'(X 10
-40 C "6 dynes/cm2) 25 C 100 C
G"(X 10-tf dynes/cm2) -40 C 25 C 100 C
Tan 6CX io2) Number -40 C 25 C 100 C
1 - 5.07 - _ 14.00 _ _ 2.60 _
1A 5.56 5.05 6.10 87.70 16.60 7.17 15.40 3.30 1.18 IB 5.09 5.02 6.20 66.00 13.40 5.46 13.00 2.60 0.88 2 - 3.75 - - 3.90 - - 1.00 - 2A 3.12 3.59 4.49 23.40 4.90 2.63 7.49 1.36 0.59 2B 3.34 3.78 4.84 21.30 4.10 2.83 6.39 1.07 0.59 3 - 4.07 - - 6.30 - - 1.60 -
4 - 3.35 - - 3.58 - - 1.12 - 5 - 3.17 - - 7.29 - - 2.31 - 6 3.67 3.80 4.57 31.60 10.50 6.79 8.61 2.88 1.49 7 3.72 3.91 4.02 25.00 9.62 10.90 6.70 2.47 2.70 8 9
10
- 5.88 - - 14.60 - - 2.48 -
- 3.89 _ - 7.25 _ _ 1.86 _
11 - 3.57 - - 17.20 - - 4.82 - 12 10.20 - - 59.40 - - 5.83 - 13 - 4.91 - - 5.10 - - 1.04 - 14 - 5.09 - - 2.16 - - 4.25 -
15 6.50 4.35 4.85 144.50 2.26 6.77 22.20 5.21 1.40 16 - 3.22 - - 6.80 - - 2.11 - 17 4.40 4.40 4.23 47.70 18.60 12.10 10.80 4.41 2.89 18 - 2.92 - - 15.10 - - 5.17 - 19 2.25 2.90 3.55 1.79 0.71 0.68 0.80 0.24 0.19
DENSITY
Density was measured on small samples of materials using a standard pycnometer.
Material Density Material Density Number Cg/cm2) Number Cg/cm2)
1 1.031 11 _
2 1.020 12 -
3 1.026 13 -
4 1.044 14 1.036 5 1.051 15 1.038 6 1.068 16 1.024 7 1.075 17 1.109 8 1.054 18 1.105 9 1.067 19 0.980
10 1.074
•10-
CROSSLINK DENSITY
The molecular weight between crosslinks (M^.) and the effective number of moles of networks crosslink per cubic centimeter (Yc) can be determined by a solvent swell technique employing hexane (3*9).
Material Number Mc (M^/crosslink) Ve (crosslink moles/cm3 x 10" "*)
1 1256 7.96 2 1855 5.37 3 1825 5.48 4 4115 2.43 5 3268 3.06 6 2717 3.68 7 4184 2.39 8 1387 7.21 9 3731 2.68
10 4329 2.31 11 - -
12 - -
13 - -
14 1346 7.43 15 1822 5.49 16 2141 4.67 17 4695 2.13 18 5747 1.74 19 4505 2.22
-11-
Thermal Properties
COEFFICIENT OF THERMAL EXPANSION -CLINEAR1
Linear CTE measurements were made using the 940 Thermalmechanical Analyzer plug-in module for the DuPont 900 Thermal Analyzer. A 4mm diameter quartz expansion probe was used with a 5 g loading. Samples were nominally 6.35 mm diameter right circular cylinders cast from Lexan molds. The exact height of each sample was measured at ambient temperature with a micrometer. Temperature was increased from -80 to 90 C at 5 degrees/minute and the vertical sample expan- sion recorded. The CTE was calculated by comparing the slope of the sample curve to that of an aluminum standard. The slope was measured over a 10° temperature ranged centered at the reported temperatures. The values for the CTE of aluminum at these temperatures were taken from the American Institute of Physics Handbook, Second Edition. The CTE values reported are the average of at least four determinations with the variation given at ± la.
-23 C Coefficient of Thermal Expansion (ym/m - Peg C)
Material Standard Number Average Deviation
1 314 13 2 - -
3 - -
4 - -
5 379 14 6 379 16 7 - -
8 308 19 9 - -
10 383 10 11 a a 12 111 16 13 380 20 14 302 7 15 291 18 16 - -
17 302 1 18 - -
19 347 5
NÖTE: Sample Size n = 4
aPhase transition
27 C Standard
Average Deviation
77 C
344
325 324
316
337 377 300 318 301 322
289
316
13
6 10
13
15 4
18 1 7
18
10
Average
346
329 325
315
330 390 318 331 319 353
332
370
Standard Deviation
15
15
15 16 9 2 2
12
15
16
•12-
THERHAL CONDUCTIVITY
Thermal conductivity (K) was determined using a comparative method adapted for the Perkin-Elmer ~DSC(10}11). The same samples were used for both ther- mal conductivity and the CTE Measurements. In this method the difference in the heat flow required to maintain a 10° temperature gradient across the sample and a Teflon reference of similar dimensions is measured. Thermal conductivity is calculated using these values, the sample and reference dimensions and the thermal conductivity of the reference. Measurements were made with the DSC set at 45 C and the cold surface temperature maintained at 35 C using a button heater and temperature controller. A thin film of thermal conductive paste (Thermacote Thermal Joint Compounds, Thermallog Co., Dallas, Texas) was used to insure good thermal contact between the ends of the sample and the hot and cold plates.
Material Number
1 2 3 4 5 6 7 8 9
10
(K) (X IP1* cal/cm-sec-°C) Standard
Average Deviation
(K)(X 10lfcal/cm-sec-oC)
5.33
5.54 5.57
5.52
5.48
0.01
0.07 0.10
0.06
0.05
Material Standard Number Average Deviation
11 5.32 0.01 12 5.27 -
13 5.74 0.05 14 5.48 0.15 15 5.55 0.07 16 - -
17 5.68 0.09 18 - -
19 5.69 0.07
NOTE: Sample Size n = 4
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SPECIFIC HEAT *Cp>
Specific heat or heat capacity (Cp) was determined using a Perkin-Elmer DSC-1 following the standard Perkin-Elmer procedure. Specific heat was determined at both 40 and 50 C.
Specific Heat (Cp)(cal/g - deg C) 40 C 50C~
Material Standard Number Average Deviation
1 0.366 _
2 - -
3 - -
4 - -
5 0.324 0.006 6 0.330 0.010 7 - - 8 0.354 0.007 9 - -
10 0.332 0.004 11 0.358 0.004 12 0.340 0.0005 13 0.370 0.006 14 0.327 0.002 15 0.388 0.002 16 - -
17 0.340 0.010 18 - -
19 0.480 0.020
NOTE: Sample Size n = 4
Standard Average Deviation
0.389
0.313 0.002 a. 330 0.010
0.363 0.003
0.344 0.002 0.379 0.002 0.345 0.003 0.383 0.007 0.324 0.003 0.386
0.350 0.020
0.491 0.004
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THERMAL DIFFUSIVITY
Thermal diffusivity (a) is calculated based on the following relationship:
a = K/6 Cp
where
K = Thermal Conductivity 6 = Density Cp = Heat Capacity or Specific Heat
Material Number
Thermal Diffusivity (a) (X 103 an2/sec)
45 C Material Number
Thermal Diffusivity (a)(X 103 cm2/sec)
45 C
1 1.369 11 -
2 - 12 -
3 - 13 -
4 - 14 1.625
5 1.655 15 1.382
6 1.580 16 -
7 - 17 1.414
8 1.461 18 -
9 - 19 1.196
10 1.510
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REFERENCES
1. Flowers, G. L. and Switzer, S. T., Background Material Properties of Selected Silicone Potting Compounds and Raw Materials for Their Substitutes, MHSMP-78-18, Amarillo, Texas, 1978.
2. Flowers, G. L. and Switzer, S. T., A Substitute Potting Compound for Sylgard 93-119 Based on Sylgard 184 and Q3-6527 Dielectric Gel, MHSMP-78-23, Amarillo, Texas, 1978.
3. Flowers, G. L. and Switzer, S. T., Substitute Potting Compounds for Sylgard 93-120, MHSMP-79-37, Amarillo, Texas, 1979.
4. Clink, G. L., FT-NMR Determination of the Silane Hydrogen Content of Siloxane Pre-Polymers, MHSMP-78-45, Amarillo, Texas, 1978.
5. Clink, G. L., FT-NMR Analysis of Silane Hydrogen, Phenyl, and Vinyl Content of Several Siloxane Pre-Polymer Materials, MHSMP-79-15, Amarillo, Texas, 1979.
6. Kohn, E. and Ashcraft, R. W., High Performance Size Exclusion Chromatography (V) Molecular Characterization of Silicone Fluids and Sums by Computer Deconvolution, MHSMP-80-27, Amarillo, Texas, 1980.
7. Cady, W. E. and Buckner, A. T., Development of Alternate Silicone Potting Compounds, Vol. 1-5, Lawrence Livermore National Laboratory, UCRL-52434, Livermore, California, 1978-1980.
8. Encyclopedia of Polymer Science and Technology, Vol. 4, 331-335, Herman, F. M., Gaylord, N. G. and Biboles, N. M., Interscience Pub. John Wiley and Sons, Inc., New York, 1966.
9. Barroll II, E. M., Flandera, M. A. and Logan, J. A., A Thermodynamic Study of the Crosslinking of Methyl Silicone Rubber, Thermochimica Acta, Elsevier Pub. Co., Amsterdam, 5(1973), 415-432.
10. Baytos, J. F., Specific Heat and Thermal Conductivity of Explosives, Mixtures and Plastic-Bonded Explosives Determined Experimentally, Los Alamos National Scientific Laboratory, LA-8034-MS, New Mexico.
11. Brennan, W. P., Miller, B. and Whitewell, J. C, Thermal Conductivity Measurements with the Differential Scanning Calorimeter, J. Applied Polymer Science 12, 1800-1802, 1968.
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1
DISTRIBUTION
Department of Energy - Washington, D.C.
Caudle, R. E.
Department of Energy - ALO
Ferranti, R. Ihne, R. J. Johnson, M. S. Laseter, W. A. Myers, L. C. Poynor, E. D. Slape, R. J. Taylor, R. E.
Fredlund, R. R., Jr. Whiteman,. A. E.
Circulation Copy (1) Plant Manager, PX (2) M&H, Lexington, KY
Technical Library
Department of Energy - AAO File (5) Technical Information Center (27)
Johnson, G. W. Mound Facility
r Bendix Corp.
Smith, C. Braun, R. J. Dichioro, J.
i
Lawrence Livermore National Laboratory Sandia National Laboratories - Albuquerque
Brockett, C. T. Cady, W. E. Golopol, H. Root, G. S. Attn: van Dyk, A. C. (18)
Arthur, B. E. Central Technical Files Crawford, J. C./
Anderson, D. H. Garner, W. L. (3)
*
Los Alamos National Scientific Laboratory
Daly, R. J. DuBois, F. Flaugh, H. L. Fuller, J. C. Report Library - ISD-4 Wechsler, J. J. Yasuda, S. K.
Mason & Hanger - Pantex
Sandia National Laboratories - Livermore
Aas, E. A. Cozine, R. D.
United Kingdom
Long, W. S., British Embassy For: Kirkham, J.
n
Bailey, R. E. Carr, B. H.
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