矿冶工程
礦冶工程
광야공정
2014年
4期
67-69,74
,共4页
钨粗精矿%氯化%挥发
鎢粗精礦%氯化%揮髮
오조정광%록화%휘발
tungsten rough concentrate%chlorination%volatilization
研究了气相氯化法从钨粗精矿中挥发多金属的影响因素。研究结果表明:稀盐酸可以适当地提高钨品位,并可以除去40%的钙;钨粗精矿经过盐酸预处理后,主要元素的氯化挥发率高于未处理精矿。最佳氯化工艺条件为:温度700℃,保温时间1 h,活性碳用量为原矿的20%,在此条件下还原氯化,钨的氯化挥发率大于99%,钼、锡的氯化挥发率大于97%;同时,铁、铝挥发率也较高,导致氯化物中的铁、铝含量较高;氯化残留矿样为熔融的盐状,结块严重。
研究瞭氣相氯化法從鎢粗精礦中揮髮多金屬的影響因素。研究結果錶明:稀鹽痠可以適噹地提高鎢品位,併可以除去40%的鈣;鎢粗精礦經過鹽痠預處理後,主要元素的氯化揮髮率高于未處理精礦。最佳氯化工藝條件為:溫度700℃,保溫時間1 h,活性碳用量為原礦的20%,在此條件下還原氯化,鎢的氯化揮髮率大于99%,鉬、錫的氯化揮髮率大于97%;同時,鐵、鋁揮髮率也較高,導緻氯化物中的鐵、鋁含量較高;氯化殘留礦樣為鎔融的鹽狀,結塊嚴重。
연구료기상록화법종오조정광중휘발다금속적영향인소。연구결과표명:희염산가이괄당지제고오품위,병가이제거40%적개;오조정광경과염산예처리후,주요원소적록화휘발솔고우미처리정광。최가록화공예조건위:온도700℃,보온시간1 h,활성탄용량위원광적20%,재차조건하환원록화,오적록화휘발솔대우99%,목、석적록화휘발솔대우97%;동시,철、려휘발솔야교고,도치록화물중적철、려함량교고;록화잔류광양위용융적염상,결괴엄중。
Contributing factors to metals volatilized from rough tungsten concentrate by gas phase chlorination were studied. Results showed that diluted hydrochloric acid can not only increase tungsten grade to some extent but also remove 40% of calcium. After pre-treatment with hydrochloric acid, predominant elements in rough tungsten concentrate have a higher volatilizing rate than that without pre-treatment. From the research, it is found the optimal conditions for chlorination are as follows:reduction-chlorination process at a temperature of 700 ℃ and being hold for 1 h, with the dosage of active carbon at 20% of raw ore, resulted in the tungsten volatilizing rate after chlorination over 99%, more than 97% for the volatilizing rate of molybdenum and tin, as well as both higher for iron and aluminum, leading to the chloride with a higher content of iron and aluminum, and the residual slag looking like molten salt and seriously agglomerated.