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Recovery of Al and Na Values from Red Mud by BaO-Na2CO3Sinter Process

机译:Bao-Na2Co3sinite过程中红泥的Al和Na值恢复

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The red mud BaO-Na2CO3sinter process can be used in combination with the Bayer process to recover sodium and aluminium from the red mud waste and direct it back to the process stream. This is facilitated by the high temperature reaction of BaO-Na2CO3and De-silication product (Sodalite) (DSP) in the red mud to produce an insoluble di-barium silicate, barium titanate, barium ferrite and a soluble sodium aluminate. A variation of the red mud BaO-Na2CO3sintering process using half the barium oxide of existing methods has been investigated. The barium to silicon ratio was reduced from 2 to 1 producing a sodium barium silicate (Na2BaSiO4) rather than the di-barium silicate (Ba2SiO4) insoluble phase produced in the existing BaO-Na2CO3sinter method. Synthetic BaO-Na2CO3sinter products were investigated to understand the phases produced during sintering at varying temperatures and the chemistry of extraction. The target phases and morphological behaviors of sinter products were seen in XRD and SEM and the highest extractions were produced from a sinter temperature of 1000 °C for 4 h. A two-stage (105 °C / 60 min, 105 °C / 240 min) water or caustic leaching process was found to be most effective for extraction. Sodium and aluminium extractions were 99% and 99.5% respectively. The experimental method devised was then used to treat red mud and the target phases were produced. An extraction of sodium and aluminium of 94% and 87% respectively was achieved. Silicon extractions were below 2%. Production benefits include sodium hydroxide savings, liquor burning, increased aluminium extraction and reduced cost of waste handling.
机译:红泥BaO-Na2CO3Sinite方法可以与拜耳工艺组合使用,以从红泥浪废物中回收钠和铝,并将其引导回工艺流。通过红色泥浆中的BaO-Na 2 CO 3和脱硅(DSP)的高温反应,以生产不溶性二钡硅酸盐,钛酸钡,铁酸钡和铝酸钠的高温反应促进。研究了使用现有方法的一半氧化钡的红色泥浆BaO-Na 2 CO 3晶体的变化。硅比的钡从2至1中减少,生产硅酸钠(Na2BasiO4),而不是在现有的BaO-Na 2 CO 3Sint方法中产生的二钡硅酸盐(Ba2SiO 4)不溶性相。研究了合成的BaO-Na 2 CO 3Sinitter产品以了解在不同温度和提取的化学过程中烧结过程中产生的相。在XRD和SEM中看到烧结产物的靶阶段和形态学行为,并从1000℃的烧结温度下产生最高提取物4小时。发现两阶段(105°C / 60分钟,105°C / 240分钟)水或腐蚀性浸出过程对提取最有效。钠和铝萃取分别为99%和99.5%。然后,设计的实验方法用于治疗红泥,并产生靶阶段。达到94%和87%的溶液和铝的提取。硅提取物低于2%。生产效益包括氢氧化钠储蓄,白酒燃烧,铝提取增加和减少废物处理成本。

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