首页> 外文会议>Waste management 2004 symposium (WM'04): waste management, energy security and a clean environment >CHALLENGES IN RETROFITTING OF CERAMIC MELTER IN PLACE OF LIQUID FED METALLIC MELTER
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CHALLENGES IN RETROFITTING OF CERAMIC MELTER IN PLACE OF LIQUID FED METALLIC MELTER

机译:液态金属熔炼炉改造陶瓷熔炉的挑战

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A modified pot glass process using induction heated liquid-fed metallic melter is adopted in India for vitrification of high-level radioactive wastes.Although all the operational vitrification plants are using this technology presently,it is recognized that induction of ceramic melters in place of metallic melters would be advantageous.The liquid fed metallic melter has limitations with respect to processing throughput and also calls for frequent remote replacement of the process pot.This replacement puts a heavy demand on the operations and is also not cost effective.Adoption of liquid fed ceramic melters in place of metallic melters calls for their retrofitting in the vitrification cell initially designed for metallic melter.This retrofitting is being carried out in one of the operating vitrification plants. rnConsiderations had to be given right from design to decommissioning of the ceramic melter, which had to be made compact without sacrificing the enhanced throughput.This involved critical analysis and design of the main electrodes with respect to their geometry and configuration.The options of slurry and frit feeding both had to be carefully designed keeping in view of the limited cell height.Side pouring of the molten glass from the melter could not be considered because of the constricted cell geometry and thus redundancy had to be provided by incorporating an additional bottom drain as stand by.In view of the compactness cylindrical geometry of the melter as against rectangular geometry was also considered. rnThe compactness of the melter was also dictated from decommissioning considerations.In view of the space constraints in the existing cell,it is necessary to lift the entire melter unit through the cell top and decommission it in a shielded environment,elsewhere.This called for limiting the entire weight of the melter including refractories within 10 tonnes and this was dictated by the availability of the material handling system in the existing cell. rnExisting waste management facilities are co-located with the reprocessing facilities at various reactor sites in India and as such do not call for vitrification plants with very high processing capacities.On successful operation of this ceramic melter,replacement of existing metallic melters with ceramic melters will be carried out in a phased manner. rnWM’04 Conference,February 29–March 4,2004,Tucson,AZ
机译:印度采用了一种采用感应加热液体进料金属熔化器的改进的锅玻璃工艺,对高放废物进行玻璃化。尽管目前所有运行中的玻璃化工厂都在使用这项技术,但人们已经认识到用陶瓷熔化器代替金属来熔化熔化器将是有利的。液体进给金属熔化器在处理产量方面存在局限性,还要求经常远程更换工艺罐,这种替换对操作有很高的要求,而且也不经济有效。熔炉代替金属熔炉需要在最初为金属熔炉设计的玻璃化单元中进行改造。这种改造是在其中一个运行中的玻璃化工厂中进行的。 rn从陶瓷熔化器的设计到退役必须予以考虑,必须在不牺牲产量的前提下使其紧凑,这涉及到主要电极的几何形状和配置的关键分析和设计。考虑到有限的孔高度,必须对熔料进料进行仔细设计。由于孔的几何形状受限制,不能考虑从熔化器中倒入熔融玻璃,因此必须通过增加底部排液来提供冗余。鉴于紧凑性,还考虑了熔化器的圆柱形几何形状而不是矩形几何形状。 rn熔化器的紧凑性也是由退役因素决定的。鉴于现有单元的空间限制,有必要将整个熔化器单元举升通过单元顶部,并在其他屏蔽环境中停用。这要求限制熔化炉的总重量(包括10吨以内的耐火材料),取决于现有单元中物料处理系统的可用性。 rn现有的废物管理设施与后处理设施位于印度各个反应堆地点,因此不需要高处理能力的玻璃化工厂。在该陶瓷熔炉成功运行后,将用陶瓷熔炉代替现有的金属熔炉分阶段进行。 WM’04会议,2004年2月29日至3月4日,亚利桑那州图森

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