Liquefaction co-processing of coal shale oil at - Argonne National ...
Liquefaction co-processing of coal shale oil at - Argonne National ... Liquefaction co-processing of coal shale oil at - Argonne National ...
TABLE 1 OIL REFINING PROFILE (CONTINENTIAL USA) Low High Specialty Hydroskimming Conversion Conversion Plants Number of Refineries 24 59 61 41 Capacity, K BBLlday 560 4,685 9,215 475 % Capacity 4 31 62 3 Major's Operate, % 30 25 90 Low Source - Oil and Gas Journal TABLE 2 IMPACT OF CONVERSION OF EXISTING REFINERY CAPACITY TO ADVANCE0 COP ROCESSING OF FUTURE HEAVY CRUDES Coal Consumption, MMTY Feedstock Existing Refinery Type Atmospheric Residuum Residuum Hydroskimning 9 - 11 3 - 6 Low Conversion High Conversion 74 - 94* 146 - 185* 229 - 290 * Requires Shutdown of Existing Units --Prime Application for Coprocessing 231 58 - 99* 91 - 155
FIGURE 1 I DISTRIBUTION OF REFINERIES BY SIZE j I 1980 to 1985 I THOUSAND BARRELS PER DAY FIGURE 2 FLOW DIAGRAM HIGH CONVERSION REFINERIES WITH COPROCESSING - 232
- Page 29 and 30: CATALYTIC CO-PROCESSINS OF OHIO NO.
- Page 31 and 32: CATALYST COMPARISON STUDY The premi
- Page 33 and 34: fractions and a decrease of heavier
- Page 35 and 36: TABLE 2 Coal Analyses I1 1 i noi s
- Page 37 and 38: Temperature WHSV, G/hr/cc TABLE 6 C
- Page 39 and 40: z FIGURE 3 COAL REACTIVITY SCREENIN
- Page 41 and 42: COPROCESSING USING HzS AS A PROMOTE
- Page 43 and 44: - 3 - that product yields depend on
- Page 45 and 46: - 5 - occurs in the yields of aspha
- Page 47 and 48: Table 1 Analysis of Feedstocks Fore
- Page 49 and 50: THO-STAGE COPROCESSING OF SUBBITUMI
- Page 51 and 52: esult in retrogressive reactions ta
- Page 53 and 54: 8. 6. Ignasiak, L. Lewkowicz, G. Ko
- Page 55 and 56: Table 4 OVERALL MASS BALANCE FOR TH
- Page 57 and 58: BACKGROUND COAL LIQUEFACTION/RESID
- Page 59 and 60: system, which could be operated wit
- Page 61 and 62: TABLE 1 EFFECT OF LC-FINING~"' TEMP
- Page 63 and 64: Figure 1. SCHEMATIC OF LCI CO-PROCE
- Page 65 and 66: SIMULATION OF A COAL/PETROLEuII RES
- Page 67 and 68: 20 pseudocomponents was developed t
- Page 69 and 70: ottoms is less sensitive to the num
- Page 71 and 72: Low Pressure Separator A temperatur
- Page 73 and 74: 7. Gallier, P.W., Boston, J.F., Wu,
- Page 75 and 76: I I I I I I I I I 100- --- Experime
- Page 77 and 78: Coprocessing Schemes The coprocessi
- Page 79: processing 25,000 and 150,000 bbl/d
- 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
- Page 93 and 94: omw '??h 4NO WNID ?N? 000 wmm c9'1'
- Page 95 and 96: tl f 246
- Page 97 and 98: 248
- 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
- Page 111 and 112: temperature, time and solvent power
- Page 113 and 114: TABLE 1 EXPERIMENTAL CONDITIONS AND
- Page 115 and 116: la Figure 1. lH-NMR spectra of samp
- Page 117 and 118: PERFORMANCE OF THE LOW TEMPERATURE
- Page 119 and 120: BENCH UNIT DESCRIPTION Process deve
- Page 121 and 122: Recycle Residuum Hydrogenati On Res
- Page 123 and 124: FIRST STAGE HRI'S CATALYTIC TWO STA
- Page 125 and 126: FIRST-STAQ COAL CONVERSION (W I IIA
- Page 127 and 128: REACTOR SOLIOS HTOROGEN/CARBON ATOl
- Page 129 and 130: TRANSPORTATION FUELS FROM TWO-STAGE
TABLE 1<br />
OIL REFINING PROFILE (CONTINENTIAL USA)<br />
Low High Specialty<br />
Hydroskimming Conversion Conversion Plants<br />
Number <strong>of</strong><br />
Refineries 24 59 61 41<br />
Capacity,<br />
K BBLlday 560 4,685 9,215 475<br />
% Capacity 4 31 62 3<br />
Major's<br />
Oper<strong>at</strong>e, % 30 25 90 Low<br />
Source - Oil and Gas Journal<br />
TABLE 2<br />
IMPACT OF CONVERSION OF EXISTING REFINERY<br />
CAPACITY TO ADVANCE0 COP ROCESSING OF FUTURE HEAVY CRUDES<br />
Coal Consumption, MMTY<br />
Feedstock<br />
Existing Refinery Type Atmospheric Residuum Residuum<br />
Hydroskimning 9 - 11 3 - 6<br />
Low Conversion<br />
High Conversion<br />
74 - 94*<br />
146 - 185*<br />
229 - 290<br />
* Requires Shutdown <strong>of</strong> Existing Units<br />
--Prime Applic<strong>at</strong>ion for Co<strong>processing</strong><br />
231<br />
58 - 99*<br />
91 - 155