liquefaction pathways of bituminous subbituminous coals andtheir
liquefaction pathways of bituminous subbituminous coals andtheir liquefaction pathways of bituminous subbituminous coals andtheir
I ---b rc-BuNH, 0 50 100 MmH-concentration(vol-%) figure 3 Coal Swelling in Binary mixture (Illimir No.6C,ul.WIiXhncrh:il(?O'C) Table 2 q-values of various Chemicals (Illinois No. 6 Coal; MI(X)mesh; at 20°C) Chemicals OKQ nitromethane acetonitrile n-butyronitnle ethlenecarbonate acetone trimetylphsphate DMF nitrobenzene b-naphthol maleic anhydride benzoic acid 524 0.43 0.41 0.52 0.61 0.68 0.88 I .M) 1.08 1.14 1.21 I .62 1.13 1.22 I .30 0.80 0 50 100 DMF(vol%)
1.50 KQ 1.00 0.50 I / ' 02 525 I 1 5 I I I I / I I I 80 I
- Page 1 and 2: LIQUEFACTION PATHWAYS OF BITUMINOUS
- Page 3 and 4: the conversion of A+P and O+G with
- Page 5 and 6: Asphaltcncs PrCasphaltenCS Cwr%, da
- 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: . . % . . 9 'HF 0 0 0 *. . 0 . . 0
- Page 53 and 54: hydrogen atoms. The hydrogen atoms
- Page 55 and 56: D to generate more D atoms. It is r
- Page 57 and 58: 12. a. Poutsma, M. L.; Dyer, C. W.
- Page 59 and 60: Figure 3. Minimum Steps to Explin D
- 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
I ---b rc-BuNH,<br />
0 50 100<br />
MmH-concentration(vol-%)<br />
figure 3 Coal Swelling in Binary mixture<br />
(Illimir No.6C,ul.WIiXhncrh:il(?O'C)<br />
Table 2 q-values <strong>of</strong> various Chemicals<br />
(Illinois No. 6 Coal; MI(X)mesh; at 20°C)<br />
Chemicals OKQ<br />
nitromethane<br />
acetonitrile<br />
n-butyronitnle<br />
ethlenecarbonate<br />
acetone<br />
trimetylphsphate<br />
DMF<br />
nitrobenzene<br />
b-naphthol<br />
maleic anhydride<br />
benzoic acid<br />
524<br />
0.43<br />
0.41<br />
0.52<br />
0.61<br />
0.68<br />
0.88<br />
I .M)<br />
1.08<br />
1.14<br />
1.21<br />
I .62<br />
1.13<br />
1.22<br />
I .30<br />
0.80<br />
0 50 100<br />
DMF(vol%)
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