화학공학소재연구정보센터
Journal of the Korean Industrial and Engineering Chemistry, Vol.4, No.1, 82-93, March, 1993
회중석 정광의 염소화에 의한 텅스텐 성분의 추출
Extraction of tungsten component from the scheelite concentrate by the chlorination
초록
염소화 공정을 통해 batch-boat-system에서 회중석으로부터 텅스텐 성분을 추출하기 위해, 환원제인 탄소의 무게비, 반응온도, 반응시간, Cl2 gas의 유량 그리고 시료입도와 같은 주요 반응 변수들에 대한 영향을 조사하였다. 이 염소화 공정들에 대한 적정조건들은 반응온도 700℃ 이상, 광물시료에 대한 탄소의 무게비 0.08, 반응시간 20분, Cl2 gas의 유량 0.6ℓ/min, 광물시료의 입도 -200mesh였으며 위 조건하에서 광물중 99%의 tungsten성분이 추출되었다. 반응속도는 고온에서는 Cl2 gas의 확산단계가, 저온에서는 화학반응단계가 속도결정단계로 보이며 각각의 단계에서 활성화 에너지는 고온 부분에서는 7.98kca1/mo1이며 저온 부분에서는 31.2kca]/mol이었다.
To extract the tungsten component from the scheelite by the chlorination process, effects of major variables such as the reducing agent, reaction temperature, reaction time, flow rate of the Cl2 gas, and the particle size of the sample, were examined in the batch-boat system. The optimum conditions for this chlorination process were as follows ; reaction temperature above 700℃, carbon weight ratio to the scheelite 0.08, reaction time 20 min, flow rate of the Cl2 gas 0.6ℓ/min, particle size of scheelite ore -200 mesh. Under the above conditions, 99% of tungsten component was extracted from scheelite ore. The diffusion step and chemical reaction step were the rate-determining steps at high and low temperature, respectively. Activation energy was 7.98kca1/mo1 at high temperature region and 31.2kca1/mol at low temperature one.
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