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 ...
GAS GENERATION AND SEPARATION COAL SOLUBILIZATION HYDROGENATION DISTILLATION AND AGGLOMERATION SteaE (Optional) Natural Gas co Rich Bi twn Bi tmen (andlor (andlor heavy of1 1 Coal heavy oi 1 ) Recycle Mater Figure 1: Block Diagram of the ARC Two-Stage CO/Steam-K2C03 - H2 Coal/Bitumen Process Concept 207
BACKGROUND COAL LIQUEFACTION/RESID HYDROCRACKING VI A THO - STAGE INTEGRATED CO- PROCESS I NG Marvin Greene Avinash Gupta William Moon LUMMUS CREST INC. 1515 BROAD STREET BLOOMFIELD, NEW JERSEY 07003 Lummus Crest Inc. (LCI), a subsidiary of Combustion Engineering Inc., has been developing technology for the simultaneous processing of coal and heavy petroleum liquids under a joint development contract with the U. S. Department of Energy. The LCI co-processing route is an outgrowth of its Integrated Two-Stage Liquefaction (ITSL) technology developed over the past decade by LCI for coal liquefaction. A 33-month R&D contract was initiated in October 1984 with the objective of determining the technical and economic feasibility of coal liquefaction via the LCI co-processing route. The project was formulated into five major program tasks as follows: Task 1: Project Management Plan Task 2: Feedstock Analysis Task 3: Co-Processing Reactivity Screening Task 4: Continuous Bench-Scale Operations Task 5: Cost Estimate of Conceptual Commercial Facility The first three tasks have been completed and the continuous Bench-Scale Operations task has recently been initiated. The balance of this paper will describe experimental methods, the LCI co-processing approach and the results of recent bench-scale unit operations. SOME JUSTIFICATIONS FOR CO-PROCESSING Since co-processing inherently requires two separate feedstocks, namely coal and petroleum resid, it is possible to assess any potential process advantages from two viewpoints. From the refiner's viewpoint, the aromatic-rich, coal-derived extracts, being well known hydrogen donor solvents, can improve the hydroprocessing conversion of heavy, low grade petroleum feedstocks. On a constant energy cost basis, the syncrude cost contribution from a coal feedstock may be less than that from a petroleum feedstock. For example, if one assumes a typical net syncrude yield of 0.0005 M3/Kg (3.0 bbl/ton) for a run-of-mine bituminous coal priced at $0.033[5g ($30/ton), then the coal feedstock cost of the coal syncrude is about f62/M (SlO.OO/bbl). This compares to petroleum cfude prices, even under the current suppressed spot market, in excess of $74-100/M ($12-16/bbl). The situation is even more pronounced in the case of a typical subbituminous, coal. Although the net yield of liq9ds from subbitumjnous coal is lower than 'that from bituminous coal (0.0003 M /Kg vs. 0.0005 M /Kg for bituminous), the corresponding subbituminous R.O.M. coal cost is not proportionately lower but rather about 73 percent lower than that of the bituminous coal ($O.OOSS/Kg vs. $0.033/Kg). This translyes to a subbituminous Coal feedstock cost of the coal liquids of about $32.6/M ($5.20/bbl). In both cases, it is envisioned that a relatively low level of coal-derived liquids would be blended with petroleum resid feedstock so as not to greatly alter the downstream refinery processability of the petroleum-coal liquid mixtures. 208
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BACKGROUND<br />
COAL LIQUEFACTION/RESID HYDROCRACKING<br />
VI A THO - STAGE INTEGRATED CO- PROCESS I NG<br />
Marvin Greene<br />
Avinash Gupta<br />
William Moon<br />
LUMMUS CREST INC.<br />
1515 BROAD STREET<br />
BLOOMFIELD, NEW JERSEY 07003<br />
Lummus Crest Inc. (LCI), a subsidiary <strong>of</strong> Combustion Engineering Inc., has been<br />
developing technology for the simultaneous <strong>processing</strong> <strong>of</strong> <strong>co</strong>al and heavy petroleum<br />
liquids under a joint development <strong>co</strong>ntract with the U. S. Department <strong>of</strong> Energy.<br />
The LCI <strong>co</strong>-<strong>processing</strong> route is an outgrowth <strong>of</strong> its Integr<strong>at</strong>ed Two-Stage<br />
<strong>Liquefaction</strong> (ITSL) technology developed over the past decade by LCI for <strong>co</strong>al<br />
liquefaction. A 33-month R&D <strong>co</strong>ntract was initi<strong>at</strong>ed in October 1984 with the<br />
objective <strong>of</strong> determining the technical and e<strong>co</strong>nomic feasibility <strong>of</strong> <strong>co</strong>al<br />
liquefaction via the LCI <strong>co</strong>-<strong>processing</strong> route.<br />
The project was formul<strong>at</strong>ed into five major program tasks as follows:<br />
Task 1: Project Management Plan<br />
Task 2: Feedstock Analysis<br />
Task 3: Co-Processing Reactivity Screening<br />
Task 4: Continuous Bench-Scale Oper<strong>at</strong>ions<br />
Task 5: Cost Estim<strong>at</strong>e <strong>of</strong> Conceptual Commercial Facility<br />
The first three tasks have been <strong>co</strong>mpleted and the <strong>co</strong>ntinuous Bench-Scale<br />
Oper<strong>at</strong>ions task has recently been initi<strong>at</strong>ed. The balance <strong>of</strong> this paper will<br />
describe experimental methods, the LCI <strong>co</strong>-<strong>processing</strong> approach and the results <strong>of</strong><br />
recent bench-scale unit oper<strong>at</strong>ions.<br />
SOME JUSTIFICATIONS FOR CO-PROCESSING<br />
Since <strong>co</strong>-<strong>processing</strong> inherently requires two separ<strong>at</strong>e feedstocks, namely <strong>co</strong>al and<br />
petroleum resid, it is possible to assess any potential process advantages from<br />
two viewpoints. From the refiner's viewpoint, the arom<strong>at</strong>ic-rich, <strong>co</strong>al-derived<br />
extracts, being well known hydrogen donor solvents, can improve the<br />
hydro<strong>processing</strong> <strong>co</strong>nversion <strong>of</strong> heavy, low grade petroleum feedstocks. On a<br />
<strong>co</strong>nstant energy <strong>co</strong>st basis, the syncrude <strong>co</strong>st <strong>co</strong>ntribution from a <strong>co</strong>al feedstock<br />
may be less than th<strong>at</strong> from a petroleum feedstock.<br />
For example, if one assumes a typical net syncrude yield <strong>of</strong> 0.0005 M3/Kg (3.0<br />
bbl/ton) for a run-<strong>of</strong>-mine bituminous <strong>co</strong>al priced <strong>at</strong> $0.033[5g ($30/ton), then the<br />
<strong>co</strong>al feedstock <strong>co</strong>st <strong>of</strong> the <strong>co</strong>al syncrude is about f62/M (SlO.OO/bbl). This<br />
<strong>co</strong>mpares to petroleum cfude prices, even under the current suppressed spot market,<br />
in excess <strong>of</strong> $74-100/M ($12-16/bbl). The situ<strong>at</strong>ion is even more pronounced in<br />
the case <strong>of</strong> a typical subbituminous, <strong>co</strong>al. Although the net yield <strong>of</strong> liq9ds from<br />
subbitumjnous <strong>co</strong>al is lower than 'th<strong>at</strong> from bituminous <strong>co</strong>al (0.0003 M /Kg vs.<br />
0.0005 M /Kg for bituminous), the <strong>co</strong>rresponding subbituminous R.O.M. <strong>co</strong>al <strong>co</strong>st is<br />
not proportion<strong>at</strong>ely lower but r<strong>at</strong>her about 73 percent lower than th<strong>at</strong> <strong>of</strong> the<br />
bituminous <strong>co</strong>al ($O.OOSS/Kg vs. $0.033/Kg). This translyes to a subbituminous<br />
Coal feedstock <strong>co</strong>st <strong>of</strong> the <strong>co</strong>al liquids <strong>of</strong> about $32.6/M ($5.20/bbl). In both<br />
cases, it is envisioned th<strong>at</strong> a rel<strong>at</strong>ively low level <strong>of</strong> <strong>co</strong>al-derived liquids would<br />
be blended with petroleum resid feedstock so as not to gre<strong>at</strong>ly alter the<br />
downstream refinery processability <strong>of</strong> the petroleum-<strong>co</strong>al liquid mixtures.<br />
208