日本エネルギー学会誌
Online ISSN : 1882-6121
Print ISSN : 0916-8753
ISSN-L : 0916-8753
150t/d規模石炭液化パイロットプラントによる開発研究 (II)
鉄系石炭液化触媒の開発
平野 勝巳鈴木 喜夫三宅 義輝高津 淑人上田 成小林 正俊
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1999 年 78 巻 1 号 p. 42-52

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The catalyst production system has been developed for a 150t/d NEDOL process pilot plant (PP). The following results were obtained through the PP operation;
(1) Catalytic activity of pulverized pyrite in an inert atmosphere of 0.7μm of median diameter compares favorably with that of the synthetic pyrite.
(2) From a viewpoint of economical and operable efficiency, two stage pyrite pulverization system (wet-type ball mill-wet-type agitated mill) is the optimum catalyst production system.
(3) Catalyst slurry of pulverized pyrite characterizes high viscous and pseudo-plastic.
(4) It was confirmed through the PP operation that the catalyst production system designed from above test data operated stably and produced highly active catalyst.
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