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ABSTRACT LIQUEFACTION CO-PROCESSING
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eaction temperature, 1000-1500 psig
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6. 7. 8. 9. 10. 11. 12. 13. 14. 15
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I 0" 100- I I I WyO-3 P 3: 1500 psi
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11.3 A-6 yJ 600 OF, 1500 psig CO, 3
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Experimental UDqradinq and Cooroces
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catalytic to the thermal hydrogenat
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the reaction with oil production re
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TET did not promote the production
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MICROAUTOCLAVE DESCRIPTION AND PROC
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FEEDSTOCK PROPERTIES Some propertie
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CONCLUSIONS HRI's microautoclave ha
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176
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100. 2 8%. M = ?8. 38. .... . . . .
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CATALYTIC CO-PROCESSINS OF OHIO NO.
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CATALYST COMPARISON STUDY The premi
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fractions and a decrease of heavier
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TABLE 2 Coal Analyses I1 1 i noi s
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Temperature WHSV, G/hr/cc TABLE 6 C
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z FIGURE 3 COAL REACTIVITY SCREENIN
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COPROCESSING USING HzS AS A PROMOTE
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- 3 - that product yields depend on
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- 5 - occurs in the yields of aspha
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Table 1 Analysis of Feedstocks Fore
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THO-STAGE COPROCESSING OF SUBBITUMI
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esult in retrogressive reactions ta
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8. 6. Ignasiak, L. Lewkowicz, G. Ko
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Table 4 OVERALL MASS BALANCE FOR TH
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BACKGROUND COAL LIQUEFACTION/RESID
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system, which could be operated wit
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TABLE 1 EFFECT OF LC-FINING~"' TEMP
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Figure 1. SCHEMATIC OF LCI CO-PROCE
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SIMULATION OF A COAL/PETROLEuII RES
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20 pseudocomponents was developed t
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ottoms is less sensitive to the num
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Low Pressure Separator A temperatur
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7. Gallier, P.W., Boston, J.F., Wu,
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- Page 81 and 82: FIGURE 1 I DISTRIBUTION OF REFINERI
- Page 83 and 84: Table 1. Samples Analyzed PNLNumber
- Page 85 and 86: the coal itself. The chemical compo
- Page 87 and 88: - - ITSL PAH Fraction PAH Fraction
- Page 89 and 90: PROCESS DEVELOPMENT STUDIES OF TWO-
- Page 91 and 92: SUMMARY e The major effect of close
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- Page 99 and 100: qkCqQ r! o! 0 0 0 0 0 0 0 I-UH ')I
- Page 101 and 102: Materials The catalyst was shell 32
- Page 103 and 104: CONCLUSIONS Separation of a light h
- Page 105 and 106: Table 3. Results of activity testin
- Page 107 and 108: feed coal and plant configuration a
- Page 109 and 110: P1 #2 #3 114 115 #6 ITSL subbitumin
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- Page 113 and 114: TABLE 1 EXPERIMENTAL CONDITIONS AND
- Page 115 and 116: la Figure 1. lH-NMR spectra of samp
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- Page 121 and 122: Recycle Residuum Hydrogenati On Res
- Page 123 and 124: FIRST STAGE HRI'S CATALYTIC TWO STA
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- Page 129 and 130: TRANSPORTATION FUELS FROM TWO-STAGE
- Page 131 and 132: Process Identification LV% Of AS- R
- Page 133 and 134: Table I11 HYDROTREATING TESTS WITH
- Page 135 and 136: Table IV HYDROTREATING TO 0.2 PPM N
- Page 137 and 138: Table VI EFFECT OF BOILING RANGE ON
- Page 139 and 140: (4) In all cases studied, the jet f
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- Page 145 and 146: are over-riding features in its fav
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- Page 155 and 156: Process TABLE 1: TWO-STAGE PROCESSE
- Page 157 and 158: Abstract Temperature-Staged Catalyt
- Page 159 and 160: Results and Discussion Reactions in
- Page 161 and 162: 2. 3. 4. 5. 6. Derbyshire, F. J. an
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- Page 165 and 166: Materials Feeds to the WGS-solvent
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- Page 169 and 170: 5. R. J. Xottenstette, Sandia Natio
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- Page 173 and 174: change in weight being compared to
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T,\llI.l< I ASAI,YSIS OP \\YOl)Al\:
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00 3000 2000 le00 1600 1400 1200 IO
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THE EFFECT OF REACTION CONDITIONS O
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and may ultiontely form methyl-subs
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! 5. Narain, N.K., Utz, B.R., Appel
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4 (u I t + 9 (u I 337 - Q 0