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 ...

25.10.2012 Views

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

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

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!