首页> 外文会议>International Mineral Processing Congress >Challenges and Chances in Operating the 'Copper Cooler Technology' Electric Smelting Furnace for Ferronickel Plant at UBPN Pomalaa
【24h】

Challenges and Chances in Operating the 'Copper Cooler Technology' Electric Smelting Furnace for Ferronickel Plant at UBPN Pomalaa

机译:UBPN Pomalaa镍铁厂使用“铜冷却器技术”电熔炉的挑战和机遇

获取原文

摘要

In September 2005, after 30 years experiencing in operating an ESF using a falling water film shell cooling system, Antam entered the new era in operating an ESF, after completely modernized its ESF No. 2 from a falling water film shell cooling system to a copper cooling system. Further, in the beginning of 2007, Ferronickel plant No. 3, where its ESF also uses copper coolers, was successfully commissioned. By operating an ESF using a copper cooling technology, Antam has to face some challenges to establish the operation stability. Besides that, the chances to maximize the furnace efficiency are greatly opened.The shielded-arc mode of electrode tip is selected to operate an ESF under relatively high furnace power to produce metal having tap temperature below 1500°C and slag having tap temperature below 1600°C. It leads to electric current unbalance. Further, operating an ESF using a copper cooler system under high voltage as consequence of the furnace power raise increases metal and slag tap temperature. This condition damages furnace integrity fast. Besides that, relatively high metal temperature increases its pressure during metal tapping. It leads to failure in closing the metal tap hole.The main different ways in operating an ESF using a falling water film shell cooling system and a copper cooling system lie in the electrode tip mode, the water specification used for cooler, metal tap block maintenance and allowed metal & slag level in furnace.Since a copper cooler system allows an ESF to be operated by consuming nickel ore having ratio Fe / Ni up to eight and producing slag having relatively high Fe content in slag, an undesirable silicon reversion phenomenon becomes an obstacle in reaching the operation stability.A copper cooler technology lets Antam to take a chance to increase its capacity. Modernizing the ESF No.2 had increased its furnace power from 17 MWh to 25 MWh. Meanwhile the ESF No. 3 can be operated up to 42 MWh. This technology allows an ESF to be operated under relatively high furnace power above 25 MWh safely as well as prolong the campaign life of ESF brick. Further,lowering ESF power consumption, extending the limitation of ratio S/M in nickel ore consumed and adjusting Ni grade in ferronickel product can be gained by applying this technology.
机译:在使用降水膜壳冷却系统运行ESF 30年后,2005年9月,Antam将ESF 2号从降水膜壳冷却系统完全改造为铜制后,进入了ESF操作的新时代。冷却系统。此外,在2007年初,三号镍铁工厂成功投产,该厂的ESF也使用铜冷却器。通过使用铜冷却技术运行ESF,Antam必须面对一些挑战才能建立运行稳定性。除此之外,极大地提高了炉子效率的机会。选择了电极头的屏蔽电弧模式,以在相对较高的炉子功率下运行ESF,以生产出出铁温度低于1500°C的金属和出渣温度低于1600°C的炉渣℃。导致电流不平衡。此外,由于炉功率的升高,在高压下使用铜冷却器系统运行ESF会增加金属和渣的出铁温度。这种情况会很快损坏熔炉的完整性。除此之外,较高的金属温度会在金属攻丝过程中增加其压力。使用下降的水膜壳冷却系统和铜冷却系统操作ESF的主要不同方式在于电极头模式,该水规格用于冷却器,金属水龙头块维护,这会导致无法关闭金属水龙头孔。由于铜冷却器系统允许通过消耗铁/镍比高达8的镍矿并产生炉渣中铁含量相对较高的炉渣来运行ESF,因此不希望有的硅转化现象成为一种达到运行稳定性的障碍。铜冷却器技术使Antam可以借此机会增加其容量。 ESF 2号现代化改造后,其熔炉功率从17 MWh增加到25 MWh。同时,ESF 3号最高可运行42 MWh。该技术可以使ESF安全地在25 MWh以上的较高熔炉功率下运行,并延长ESF砖的使用寿命。此外,通过应用该技术,可以降低ESF功耗,扩大镍矿消耗比S / M的限制以及调整镍铁产品中镍的品位。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号