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김병욱,김지동 한국화학공학회 1964 Korean Chemical Engineering Research(HWAHAK KONGHA Vol.2 No.2
The extraction rate during the formation of drops in the system of toluene-propinic acid-water and benzene-acetic acid-water has been studied and the results for each system were given. It has been considered that the resistance in the continious phase to solute transfer and the end effect are negligible, and that "the liquid-liquid extraction during drop formation" is not caused by molecular diffusion but by tublent diffusion.
回轉反應爐에 있어서 톱밥의 熱分解를 위한 流動特性의 硏究
李輔成,金志同,金惠榮 충남대학교 공업교육연구소 1982 論文集 Vol.5 No.2
This paper is a study of the fundamental design and operation preblems in Rotary Kilns for Biomass- pyrolysis. It is concerned especially with the flow pattern and mixing degree of solid reactants in Rotary Kilns. It was cleared that the mean residence time of solids was independent on the feed rate and the highest mixing degree could be obtained at 120 rpm. With a modified temperature profile in the Kiln and through pyrolysis of saw dust a gas mixture could be produced which has a calorific value of 3500 kcal/㎥ calculated.