DESIGN OF RECOVERABLE CATALYSTS FOR A MULTISTAGE COAL-LIQUEFACTION PROCESS

Citation
I. Mochida et al., DESIGN OF RECOVERABLE CATALYSTS FOR A MULTISTAGE COAL-LIQUEFACTION PROCESS, Energy & fuels, 8(1), 1994, pp. 25-30
Citations number
27
Categorie Soggetti
Engineering, Chemical","Energy & Fuels
Journal title
ISSN journal
08870624
Volume
8
Issue
1
Year of publication
1994
Pages
25 - 30
Database
ISI
SICI code
0887-0624(1994)8:1<25:DORCFA>2.0.ZU;2-8
Abstract
A multistage liquefaction scheme consisting of coal pretreatment, solv ent-mediated hydrogen-transfer dissolution, and catalytic hydrocrackin g steps was proposed in order to achieve the highest oil yields with c omplete conversion of organic components in coal and-to enable the rec overy and repeated use of the catalyst with its least deactivation. Th e deashing pretreatment enhanced the depolymerization of coal macromol ecules through the removal of bridging ion-exchangeable cations as wel l as the better contact of donor solvent with coal macromolecules. The highest oil plus asphaltene yield of ca. 75% was obtained through the two-step liquefaction of acid-treated Morwell coal by the reactions o f noncatalytic hydrogen transfer (donor solvent: tetrahydrofluoranthen e, solvent/coal = 1) at 430 degrees C-2 min in the first step and the following catalytic hydrogenation with a pyrite catalyst at 400 degree s C-20 min. The multistep liquefaction scheme is discussed in terms of the highest efficiency of utilization of solvent and catalyst at the respective step. Two types of recoverable catalysts were investigated to allow repeated use of the;catalyst in the primary liquefaction. The first type was an acid-proof iron catalyst which was recoverable from :a mixture with residual carbonates and chlorides that are soluble in acids. Such a catalyst was applicable to particular coals; such as an Australian brown coal which is completely liquefied,leaving calcium an d magnesium carbonates as the major residual minerals after the primar y liquefaction. The second type was characterized by its sulfur-proof ferromagnetism for the recovery from the minerals and carbons by gradi ent magnetic field. Fe3Al powder and carbon/ferrite composite catalyst s were found to maintain their ferromagnetism after the sulfiding to b e fairly active in the liquefaction of the brown coal. Procedures for activation, recovery, and repeated use of these recoverable catalysts were preliminarily examined.