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
. 50 . Table I . Properties of Pitch Feed Ultimate analysis: As received Carbon. % ..... 1 ... 84.72 . Hydrogen. 70 .......... 8.53 . . Nitrogen. 70 ......... 0.87 . . Oxygen. 70 ........... 4.62 Sulfur. 70 .......... 0.90 Chlorine. 70 ......... 0.01 Moisture. 70 ....... : . 0.00.' . . Flash point. F .............................. 510 Softening point (R & B) glycerin. C .............. 90 Softening point (cube in glycerin). . C .............. 105 Penetration at 77" F. 100 grams. 5 seconds ......... 0 . . Specific gravity. 25 ~/250 c ................... 1 .. 1.128 Ash. 70 ................................... 0.35 Water. % ................................. 0.00 Ductility. cm at 77 F ......................... 0 Bitumen. soluble in CS, ....................... 78.80 Free carbon ............................... 20.85 Distillation : TO 3OO.C. 70 ............................. 6.40 Softening point of residue (R & B). C ............. 90 Sulfonation index of distillate to 300" C ........... 0 Conradson carboni., TO'., .......................... 20.81 Table LT . Composition of Gas at a Coking Temperature of 950" F Component Volume -percent co. ........... 0.74 co ............ 4.91 H. ............ 7.67 CH. ........... 43.83 C2% ........... 13.97 C2H4 ........... 9.94 C.H. ........... 13.54 C.'. ........... 5.40 . I
51. Gas n t 7 A. Pitch feed tank Oil B . Pitch feed pump C . Delayed coking drum D . Gas and oil cooler E . Oil separator F . Pitch line preheater G . Wet test meter H . Gas water scrubber I . Scrubber seal pot J - Hydraulic speed control K . Pump flushing oil tank Water Water FIGURE 1. - Flowsheet of Delayed Coking Process. FIGURE 2. - The Delayed Coking Apparatus.
- 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 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 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
- 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
.<br />
50 .<br />
Table I . Properties of Pitch Feed<br />
Ultimate analysis: As received<br />
Carbon. % ..... 1 ... 84.72 .<br />
Hydrogen. 70 .......... 8.53 . .<br />
Nitrogen. 70 ......... 0.87 . .<br />
Oxygen. 70 ........... 4.62<br />
Sulfur. 70 .......... 0.90<br />
Chlorine. 70 ......... 0.01<br />
Moisture. 70 ....... : . 0.00.' . .<br />
Flash point. F .............................. 510<br />
Softening point (R & B) glycerin. C .............. 90<br />
Softening point (cube in glycerin). . C .............. 105<br />
Penetration at 77" F. 100 grams. 5 seconds ......... 0<br />
. .<br />
Specific gravity. 25 ~/250 c ................... 1 .. 1.128<br />
Ash. 70 ................................... 0.35<br />
Water. % ................................. 0.00<br />
Ductility. cm at 77 F ......................... 0<br />
Bitumen. soluble in CS, ....................... 78.80<br />
Free carbon ............................... 20.85<br />
Distillation :<br />
TO 3OO.C. 70 ............................. 6.40<br />
Softening point of residue (R & B). C ............. 90<br />
Sulfonation index of distillate to 300" C ........... 0<br />
Conradson carboni., TO'., .......................... 20.81<br />
Table LT . Composition of Gas at a Coking<br />
Temperature of 950" F<br />
Component Volume -percent<br />
co. ........... 0.74<br />
co ............ 4.91<br />
H. ............ 7.67<br />
CH. ........... 43.83<br />
C2% ........... 13.97<br />
C2H4 ........... 9.94<br />
C.H. ........... 13.54<br />
C.'. ........... 5.40<br />
.<br />
I
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