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Title: Catalysts and process developments for two-stage liquefaction. Final technical report, October 1, 1989--September 30, 1992

Technical Report ·
DOI:https://doi.org/10.2172/10190862· OSTI ID:10190862

Research in this project centered upon developing and evaluating catalysts and process improvements for coal liquefaction in the two-stage, close-coupled catalytic process. The major results are summarized here and they are described in more detail under each Task. In tasks for coal pretreatment and beneficiation, it was shown for coal handling that drying of both lignite or subbituminous coals using warm air, vacuum oven or exposing to air for long time was detrimental to subsequent liquefaction. Both laboratory and bench-scale beneficiations indicated that in order to achieve increased liquefaction yield for Illinois No. 6 bituminous coal, size separation with in sink-float technique should be used. For subbituminous coal, the best beneficiation was aqueous SO{sub 2} treatment, which reduced mineral matter. In the case of lignite, the fines should be rejected prior to aqueous SO{sub 2} treatment and sink-float gravity separation. In liquefying coals with supported catalysts in both first and second stages, coal conversion was highest (93%) with Illinois No. 6 coal, which also had the highest total liquid yield of 80%, however, the product contained unacceptably high level of resid (30%). Both low rank coals gave lower conversion (85--87%) and liquid yields (57--59%), but lighter products (no resid). The analysis of spent first stage catalysts indicated significant sodium and calcium deposits causing severe deactivation. The second stage catalysts were in better condition showing high surface areas and low coke and metal deposits. The use of dispersed catalyst in the first stage would combat the severe deactivation.

Research Organization:
Amoco Oil Co., Naperville, IL (United States). Research and Development Dept.
Sponsoring Organization:
USDOE, Washington, DC (United States)
DOE Contract Number:
AC22-88PC88819
OSTI ID:
10190862
Report Number(s):
DOE/PC/88819-T12; ON: DE95001948; BR: AA2515150; TRN: AHC29427%%19
Resource Relation:
Other Information: PBD: [1992]
Country of Publication:
United States
Language:
English