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
44. 2.0 I 1.2 - 0 2 1.0- 0.8 i TIME, HRS Figure Y. Plot of first-order equation for gasoline formation 2.0 - 1.8 - 1.6- 1.4- 1.2 - 0 7 lo 1.0- 0 - 0 0.8 - 0.6- 0.4 - 0.2. 01 0 2 4 6 8 10 12 14 16 18 20 TIME, HRS. Figure 12. Plot of first-order equetion for desulphurization. , I I I
i \\ I 3 , ' '1 I i I , - -1 I 02- 0 - - 45. . . . \ I TIME, HRS Figure 13. Plot of first-order equation for denitrogenation 0.1 0.0 - 0.2 * 0- 0.4 0 - -0.6 -0. E 1. NITROGEN 2.SULFUR ' 3.GASOLINE \ -1 .c 1.0 1.1 1.2 1.3 3 1/T XI0 1.4 1.5 Figure 14. Arrhenius plot for gasoline formation, deeulphurization and denitrogenation . .- ._ .. . . . . . . . . . . . .. . . .., -. ~ . _ I . . .
- Page 1 and 2: Introduction 1. SECONDARY CELLS WIT
- 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 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 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
44.<br />
2.0 I<br />
1.2 -<br />
0<br />
2 1.0-<br />
0.8 i<br />
TIME, HRS<br />
Figure Y. Plot of first-order equation for gasoline formation<br />
2.0 -<br />
1.8 -<br />
1.6-<br />
1.4-<br />
1.2 -<br />
0 7<br />
lo 1.0-<br />
0<br />
- 0<br />
0.8 -<br />
0.6-<br />
0.4 -<br />
0.2.<br />
01<br />
0 2 4 6 8 10 12 14 16 18 20<br />
TIME, HRS.<br />
Figure 12. Plot of first-order equetion for desulphurization.<br />
, I<br />
I<br />
I
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