secondary cells with lithium anodes and immobilized fused_salt
secondary cells with lithium anodes and immobilized fused_salt secondary cells with lithium anodes and immobilized fused_salt
Chlorine Fentafluaride T q D OC 252.2 252.2 , 252.2 252.2 268.5 279.4 279.4 263.2 283.0 287.4 288.2 281.4 W-6 291.8 291.5 293.0 293: 0 293.3 293.0 293.5 293.0 *.O 3m. 5 306.8 307.0 307.5 7, -c 28.9 113.0 WA.5 449.0 196.8 36-2 115.3 23.6 36.3 28.4 40.4 42.4 55.0 11.9 28-1 11.6 1b.6 3a.4 38.4 41.7 62.8 81.3 70% 9-16 11-93 12-9 8 4. -1 kl, sec 0.00292 0.00300 0.00213 0.00246 0.00803 0.0170 0.0158 0.0250 0.0252 0.0357 0.041 j 0.0398 0**59 0.0360 0.0413 0.0391 0.0394 0.0408 0.0432 O.OJ&? 0.0476 0.W 0.0959 0.115 0.123 0.109 A -1. kl , sec 0.00260 0.00803 0.0164 0.0251 0.0385 0.0417 0.113 ,
I I : \ I I 6 85. Redox in the C120-AsF System 5 C. J. Scheck and D. Pilipovich Xocketdjme, a Division of North American Rockwell Corporation Canoga Park, Celifornia 91304 Dich1orir.e oxide (or chlorine monoxide) hes been reported to form a coiplex with ,AsF5 %t -78'
- Page 34 and 35: 34. Table 1, Properties of Feed Mat
- Page 36 and 37: 0 0 0 m 0 VI b N 0 c, VI N 0 v, N h
- Page 38 and 39: - Literature Cited 38 1. Gordon, K
- Page 40 and 41: 40 z - B 30 w 6 20 yl w U 10 40. 10
- Page 42 and 43: Z 0 In 80 CK W > 6 60- 0 I- 40- Z W
- Page 44 and 45: 44. 2.0 I 1.2 - 0 2 1.0- 0.8 i TIME
- Page 46 and 47: - 2.81 1.NITROGEN 2. SULFUR 3. GASO
- Page 48 and 49: 48. The oil from the separator is v
- Page 50 and 51: . 50 . Table I . Properties of Pitc
- Page 52 and 53: 52. Coke yield A - - - - 0 800 900
- Page 54 and 55: FIGURE 8. 54. t 0.5 1 800 900 1,000
- Page 56 and 57: Introduction 56. FLUORODINITROETUNO
- Page 58 and 59: chloride extractant without other h
- Page 60 and 61: 60. identified (Reference 7) as the
- Page 62 and 63: 62. to FEFO -e quite high (80 to 85
- Page 64 and 65: 64. RECENT CHEMISTRY OF THE OXYGEN
- Page 66 and 67: polymers for the conventional fuel
- Page 68 and 69: 68. In summary, two general methods
- Page 70 and 71: 70. Table XI1 Differential Thermal
- Page 72 and 73: vapor Pressure (psia) Figure 4. Vap
- Page 74 and 75: C H -0-C-NHF, - 2 5 II 0 74. H 9304
- Page 76 and 77: 76. The infrared spectrum is descri
- Page 78 and 79: , 78. PREPARATION AND POLYMERIZATIO
- Page 80 and 81: . .- . - ..... . . I ,caving the re
- Page 82 and 83: If it ~ 3 ~ o~t 7 s Y'2t the therm1
- Page 86 and 87: , 86. Zeections of Cl30 and AsF5. M
- Page 88 and 89: aa . - The rrost difficult rctionel
- Page 90 and 91: 90. DENSITY, VISCOSITY AND SURFACE
- Page 92 and 93: 92. If it is assumed that the syste
- Page 94 and 95: 94. After condensation of oxidizer
- Page 96 and 97: Stirring Solenoid LHe 7. Cryostat 9
- Page 98 and 99: Introduction 98. RFACTIONS OF OxYcm
- Page 100 and 101: , Acknowledgement 100. This work wa
- Page 102 and 103: 102. volume and then by pumping to
- Page 104 and 105: 104. The x-ray powder pattern (Tabl
- Page 106 and 107: Irredie tion Time, mi&) 106. Table
- Page 108 and 109: I. Introduction 108. RE7IIEw OF ADV
- Page 110 and 111: 1.40 w F O/) 103-4O 'F 110. /H 0 21
- Page 112 and 113: !P, "c -- -2118.5 -195 -172 -16.1 .
- Page 114 and 115: 114. weaker than those in NF02. The
- Page 116 and 117: Compound C102F ~ 1 , 0 ~ -146 ~ 116
- Page 118 and 119: 118. fom such salts as cS+m8- have
- Page 120 and 121: 120. DETONABILITY TESTING AT NONAMB
- Page 122 and 123: I 122. top) is closed with caps whi
- Page 124 and 125: 124. five pieces of MDF, each 20.00
- Page 126 and 127: 126. auxiliary equipment. For conve
- Page 128 and 129: 128. reliability. Details of most o
- Page 130 and 131: 130. The time required for the deto
- Page 132 and 133: 132. Fig. 2 Typical Witness Plate
I<br />
I<br />
:<br />
\<br />
I<br />
I 6<br />
85.<br />
Redox in the C120-AsF System<br />
5<br />
C. J. Scheck <strong>and</strong> D. Pilipovich<br />
Xocketdjme, a Division of North American Rockwell Corporation<br />
Canoga Park, Celifornia 91304<br />
Dich1orir.e oxide (or chlorine monoxide) hes been reported to form a<br />
coiplex <strong>with</strong> ,AsF5 %t -78'
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