liquefaction pathways of bituminous subbituminous coals andtheir
liquefaction pathways of bituminous subbituminous coals andtheir liquefaction pathways of bituminous subbituminous coals andtheir
3 Table 111. Aliphatic vs. Aromatic Deuterium in Products from Thermolysis of 1,2-Diphenylethane under Dz at 450' C by NMR: Compound Time Aromatic D (min) /molecule 1,a-Diphenyl- ethane 8 0.13 30 0.91 Toluene 8 0.17 30 0.65 Benzene 30 0.66 Ethylbenzene 15 0.36 30 0.50 45 1.32 Figure 1. Fiml.Ordw Pi01 for Convenion of 12-Diphenylethene Under D, a1 450. C. 1.6 1.4 - 0 - 1.2 - 1.0 - 0.1 - 0.11 - . 0.4 - 0 0.2 - E @ 0.0 0 10 20 30 40 Time (min) 50 532 Aliphatic D /molecule CH2 CH3 0.09 0.65 0.18 0.39 0.18 0.54 0.213 0.44 0.54 0.71 Figure 2. Glans Readon Vessel for Thermolysis Under D,.
Figure 3. Minimum Steps to Explin Deuterium DiotribuUon Patlorn 533
- Page 7 and 8: NEW DIRECTIONS TO PRECONVERSION PRO
- Page 9 and 10: ecause of incorporation of the coal
- Page 11 and 12: should be considered more. The step
- Page 13 and 14: 17 18 Run no. 0 cys I ToS-CyS TS-To
- Page 15 and 16: INTRODUCTION Effects of Thermal and
- Page 17 and 18: apid decline in modulus. The loss m
- Page 19 and 20: -0.01- . 04 5 -0.03- E 6 -0.0s- c)
- Page 21 and 22: Assessment of Small Particle Iron O
- Page 23 and 24: yields are calculated by subtractin
- Page 25 and 26: conversion is greater than the corr
- Page 27 and 28: Table 3. Effect of Superfine Iron O
- Page 29 and 30: EFFECT OF A CATALYST ON THE DISSOLU
- Page 31 and 32: inherent volatility of Mo(CO), perm
- Page 33 and 34: Analysis of the quantity and compos
- Page 35 and 36: $ EO .- 0 m L 0 c 0 0 > 40 300 350
- Page 37 and 38: 0 0 0 0 0.000 0.005 0.010 0.015 0.0
- Page 39 and 40: of these studies indicate that cont
- Page 41 and 42: Different levels of adsorption occu
- Page 43 and 44: Nominal 2 Table 1. Concentration of
- Page 45 and 46: - iF m 1.6 1.4 1.2 - - - 1- 0 0.8 -
- Page 47 and 48: RESULTS AND DISCUSSION Swelling of
- Page 49 and 50: . . % . . 9 'HF 0 0 0 *. . 0 . . 0
- Page 51 and 52: 1.50 KQ 1.00 0.50 I / ' 02 525 I 1
- Page 53 and 54: hydrogen atoms. The hydrogen atoms
- Page 55 and 56: D to generate more D atoms. It is r
- Page 57: 12. a. Poutsma, M. L.; Dyer, C. W.
- Page 61 and 62: Apoaratus and Procedure Microflow R
- Page 63 and 64: Model ComDound Test Figure 5 shows
- Page 65 and 66: Figure 1. High resolution gas chrom
- Page 67 and 68: Figure 5. Product distribution for
- Page 69 and 70: THQ at somewhat higher temperatures
- Page 71 and 72: areas of the particles and the SEM
- Page 73 and 74: Experimental Catalyst Precursors an
- Page 75 and 76: impregnating solvent. Table 3 shows
- Page 77 and 78: of MoCo-TC2 at the level of 0.5 wt%
- Page 79 and 80: Table 4. Effect of Temperature Prog
- Page 81 and 82: In the past, chemical treatments in
- Page 83 and 84: The effect of Corn20 preaatment on
- Page 85 and 86: Reaction Time Figure 1 - Schematic
- Page 87 and 88: DISSOLUTION OF THE ARGONNE PREMIUM
- Page 89 and 90: A much more def~tive trend is seen
- Page 91 and 92: EFFECT OF CHLOROBENZENE TREATMENT O
- Page 93 and 94: same conditions and an extraction t
- Page 95 and 96: ACKNOWLEDGEMENT The authors thank t
- Page 97 and 98: THE STRUCTURAL &=RATION OF HUMINlTE
- Page 99 and 100: to be originally derived from demet
- Page 101 and 102: 145 30 I --/---Jh I , , I I , 250 2
- Page 103 and 104: THE EFFECTS OF MOISTURE AND CATIONS
- Page 105 and 106: 1 for the Zap lignite. These result
- Page 107 and 108: content of the samples ion-exchange
3<br />
Table 111. Aliphatic vs. Aromatic Deuterium in Products from<br />
Thermolysis <strong>of</strong> 1,2-Diphenylethane under Dz at 450' C by NMR:<br />
Compound Time Aromatic D<br />
(min) /molecule<br />
1,a-Diphenyl-<br />
ethane 8 0.13<br />
30 0.91<br />
Toluene 8 0.17<br />
30 0.65<br />
Benzene 30 0.66<br />
Ethylbenzene 15 0.36<br />
30 0.50<br />
45 1.32<br />
Figure 1. Fiml.Ordw Pi01 for Convenion <strong>of</strong><br />
12-Diphenylethene Under D, a1 450. C.<br />
1.6<br />
1.4 - 0 -<br />
1.2 -<br />
1.0 -<br />
0.1 -<br />
0.11 - .<br />
0.4 -<br />
0<br />
0.2 - E<br />
@<br />
0.0<br />
0 10 20 30 40<br />
Time (min)<br />
50<br />
532<br />
Aliphatic D<br />
/molecule<br />
CH2 CH3<br />
0.09<br />
0.65<br />
0.18<br />
0.39<br />
0.18 0.54<br />
0.213 0.44<br />
0.54 0.71<br />
Figure 2. Glans Readon Vessel for<br />
Thermolysis Under D,.
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