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전해수,이제근 ( Hai Soo Chun,Jea Keun Lee ) 한국화학공학회 1978 Korean Chemical Engineering Research(HWAHAK KONGHA Vol.16 No.2
In recent years some noteworthy developments and the practical applications of fluidized beds to industry have been reported as the significance of fluidized bed has been recognized more and more. In this part Ⅱ, recent advances on applied parts of fluidized beds are reviewed and characteristics of some special types will be discussed.
전해수,강웅기 한국화학공학회 1981 Korean Chemical Engineering Research(HWAHAK KONGHA Vol.19 No.5
유도층 전극반응기내의 반응속도분포를 검토하였다. 산성구리용액중 구리전착반응계에서 연속상유효 비전기전도도(K_s)에 대한 분산상 유효비전기전도도(K_m)의 비 K_m/K_s = 4∼20 정도이면 반응의 대부분이 격막인접 영역(격막으로부터 약 0.8cm 까지)에서 일어나고 있으며, K_m/K_s = 0.07∼0.2 정도이면 반응은 거의 전류공급판 인접영역(전류공급판으로부터 약 0.6㎝까지)에서 일어나고 있다. 그리고 K_m○K_s=1 이면 반응기 양끝 부분이 활성영역임을 알았다. The distribution of the reaction rate in a fluidized bed electode reactor was studied. The distribution was strongly influenced by the effective specific electrical conductivities of the continuous electrolyte phase (K_s) and of the dispersed particle please (K_m). For the ratio of conductivities (K_m/K_s) in the range of 4∼20, the reaction mainly occurred in the diaphragm region (0∼0.8㎝ from the diaphragm). However, the main reaction occurred in the feeder region(0∼0.9㎝ from the feeder) for the ratio of K_m/K_s in the range of 0.07∼0.2. For the case of K_m○K_s, the reaction occurred mostly at both ends of the reactor.