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
FIGURE 8. 54. t 0.5 1 800 900 1,000 1,100 1,200 COKING TEMPERATURE "F - Coking Temperature vs. Sulfur Content of Coke. 1.20 1.10 1.00 0.90 800 900 1,000 1,100 1,200 COKING TEMPERATURE, "F FIGURE 9. - Effect of Temperature on Specific Gravity of Product Oil. , ri 11
h I I ' I 'I b I 55. In 4 u 150 I 0 + 4 ! I I , I I , E 100- z 4 5 2 > c I O , I I I I I I 800 900 1,000 1,100 1,200 COKING TEMPERATURE. 'F FIGURE 10. - Effect of Temperature on Ethylene-to-Ethane Ratio. 2 1 1 , , , , I 0 800 900 1,000 1,100 1.; COKING TEMPERATURE, "F ,FIGURE 11. - Effect of. Temperature on Methane-to-Hydrogen Ratio. 0 I I ,
- Page 3 and 4: I time curves at constant current d
- Page 5 and 6: I 1. 2. 3. 4. 5. 6. 7. 8. 9. 10. 11
- Page 7 and 8: 7. IV IV- Equivalent Weight, gr/ Eq
- Page 9 and 10: 1 3 9 SOYO FILLER,HQT PRESS Fig. 4.
- Page 11 and 12: 11. COAL PYROLYSIS USING LASER IRRA
- Page 13 and 14: 13. Macerals. Macerals from a singl
- Page 15 and 16: i 1 I Photochemistry. A fundamental
- Page 17 and 18: t P li. al ’ i ._ m LL
- Page 19 and 20: ' 19. PYROLYSIS OF COAL IN A MICROW
- Page 21 and 22: I 21. In the third stage, the gas e
- Page 23 and 24: .4 4 0 W 0 m .d m x .-( 0 x w M m s
- Page 25 and 26: ' 25. CONCLUSIONS The principal rea
- Page 28 and 29: ' .4 b s tract 28.
- Page 30 and 31: 30. the course of the experiment Ex
- Page 32 and 33: d (Sulfur] dt m i trogenj dt 32. E
- 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 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 84 and 85: Chlorine Fentafluaride T q D OC 252
- 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
FIGURE 8.<br />
54.<br />
t 0.5 1<br />
800 900 1,000 1,100 1,200<br />
COKING TEMPERATURE "F<br />
- Coking Temperature vs. Sulfur Content of Coke.<br />
1.20<br />
1.10<br />
1.00<br />
0.90<br />
800 900 1,000 1,100 1,200<br />
COKING TEMPERATURE, "F<br />
FIGURE 9. - Effect of Temperature on Specific Gravity of Product Oil.<br />
,<br />
ri<br />
11
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