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
34. Table 1, Properties of Feed Material sp. gr. (250C! Tar acids, vol % of feed Tar bases, wt. % of feed Sulfur, wt. % of feed hitrogen, wt. % of feed Distillation data 1.B P , OC. 50% d istillate Pitch point Residue, vole % of feed Hydrocarbon ty es in neutral fraction 200' to 360°C, vola % Saturates Olefins Aromatics 0 " 9942 30 .o 3.5 0.6984 0.4018 200 298Oc 360°C 30.0 32.0 19.0 49.0 I' I
n I 35. Table 11. Influence of Temperature on Product Distribution (Pressure, 1500 psi) Temp. (OC.) 400 ’ Reaction Time, hrs. 13 Yield, vol. % of feed Gasoline Diesel oil Tar acids Tar bases Residue Gas (including losses) Sulfur, wt. Z of feed Nitrogen, wt % of feed Composition of gasoline, vol. % 45.0 35.0 2.0 1.0 12.0 4.5 0.0489 0.0924 Aroma tics 33.5 Ka ph the nes 10.0 Olefins 2.0 Isoparaffins 25.5 K-paraffins 29.0 Diesel index of diesel oil 40.0 425 12 51.0 29.0 1.0 0- 5 12.0 6.5 0 IO210 0.0442 35.0 9.0 3.0 26.0 27.0 37.5 450 10 56.0 24.0 13.0 7.0 0.014 0.0321 34.0 10.5 2.0 26.0 27.5 34.0 475 8 61.0 20.0 I - 11.5 7.5 0.0135 0.0201 32 - 0 10.0 2.0 27.0 29.0 31.0 500 5 64.0 16.0 - 12.0 8.0 0.0136 0.0163 33.0 10.0 4.0 25.0 28.0, 28.0 - Isobutane Pi-butane 1.0 1,25 1-45 1.51 1.75
- 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 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
n<br />
I<br />
35.<br />
Table 11. Influence of Temperature on Product Distribution<br />
(Pressure, 1500 psi)<br />
Temp. (OC.) 400<br />
’ Reaction Time, hrs. 13<br />
Yield, vol. % of<br />
feed<br />
Gasoline<br />
Diesel oil<br />
Tar acids<br />
Tar bases<br />
Residue<br />
Gas (including<br />
losses)<br />
Sulfur, wt. Z<br />
of feed<br />
Nitrogen, wt<br />
% of feed<br />
Composition of<br />
gasoline, vol. %<br />
45.0<br />
35.0<br />
2.0<br />
1.0<br />
12.0<br />
4.5<br />
0.0489<br />
0.0924<br />
Aroma tics 33.5<br />
Ka ph the nes 10.0<br />
Olefins 2.0<br />
Isoparaffins 25.5<br />
K-paraffins 29.0<br />
Diesel index of<br />
diesel oil 40.0<br />
425<br />
12<br />
51.0<br />
29.0<br />
1.0<br />
0- 5<br />
12.0<br />
6.5<br />
0 IO210<br />
0.0442<br />
35.0<br />
9.0<br />
3.0<br />
26.0<br />
27.0<br />
37.5<br />
450<br />
10<br />
56.0<br />
24.0<br />
13.0<br />
7.0<br />
0.014<br />
0.0321<br />
34.0<br />
10.5<br />
2.0<br />
26.0<br />
27.5<br />
34.0<br />
475<br />
8<br />
61.0<br />
20.0<br />
I<br />
-<br />
11.5<br />
7.5<br />
0.0135<br />
0.0201<br />
32 - 0<br />
10.0<br />
2.0<br />
27.0<br />
29.0<br />
31.0<br />
500<br />
5<br />
64.0<br />
16.0<br />
-<br />
12.0<br />
8.0<br />
0.0136<br />
0.0163<br />
33.0<br />
10.0<br />
4.0<br />
25.0<br />
28.0,<br />
28.0<br />
-<br />
Isobutane<br />
Pi-butane 1.0 1,25 1-45 1.51 1.75
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