首页> 外文会议>Proceedings of Second International Conference on Electrical Systems, Technology and Information 2015 >Chapter 34 Recycling of the Ash Waste by Electric Plasma Treatment to Produce Fibrous Materials
【24h】

Chapter 34 Recycling of the Ash Waste by Electric Plasma Treatment to Produce Fibrous Materials

机译:第34章电等离子处理灰渣的回收生产纤维材料

获取原文
获取原文并翻译 | 示例

摘要

The article presents the results of processing of technogenic waste ash and slag in arc plasma. It performs calculations of the reactor core power generation capacity of the current density and voltage gradient. When calculating the diameter of the reactor chamber is adopted for determining the size and all the basic laws of the electric band are expressed through it. Research performed by methods of X-ray energy dispersive spectral analysis and electron microscopy. Experiments without additional charging melting ash show high refractoriness (above 2000 ℃) and viscosity during processing, so to reduce the melting temperature and reducing energy required additional charging dolomite (CaCO_3) to obtain homogenous melts for subsequent production of the melt and fiber materials its basis. Melting additional charging wastes conducted with 10-30 % CaCO_3 were investigated, thereby reducing melting time and thereby reduce energy costs in the future to receive fibers from the melt. When additional charging melting ash with 10 % CaCO_3 was observed a small gassing, approximate energy consumption for production of 1 kg of the melt was 4 kWh/kg. Melting additional charging with 20 % CaCO_3 further reduce the melting time by 25 % and reduce energy consumption to 2.8 kWh/kg, the process was easy to moderate gassing. Additional charging 30 % CaCO_3 and increased melting time respectively (compared with 20 % additional charging) energy to 3.4 kWh/kg, the melting took place violently with strong gas formation. Thus, the experimentally found optimum concentration additional charging make 20 % CaCO_3. There is present the principle possibility of melting the wastes with additional charging dolomite (CaCO_3) to produce a melt thereof and generation of thin mineral wool as a component of composite materials, and insulating materials for the fibrous structure.
机译:本文介绍了在电弧等离子体中处理技术废灰和矿渣的结果。它执行电抗器堆芯发电能力的电流密度和电压梯度的计算。在计算反应器腔室的直径时,采用它来确定尺寸,并由此表达出电带的所有基本定律。通过X射线能量色散光谱分析和电子显微镜的方法进行的研究。没有额外装料熔融灰分的实验显示出较高的耐火度(2000℃以上)和加工过程中的粘度,因此要降低熔融温度并降低能量,需要额外的装料白云石(CaCO_3)以获得均质的熔体,用于随后生产熔体和纤维材料。对使用10-30%CaCO_3进行的熔化其他装料废物进行了研究,从而减少了熔化时间,从而降低了将来从熔体中接收纤维的能源成本。当观察到有少量放气时额外充入的含10%CaCO_3的熔灰时,生产1千克熔体的大约能耗为4 kWh / kg。用20%CaCO_3熔化额外的装料进一步将熔化时间减少了25%,并将能耗降低到2.8 kWh / kg,该过程易于适度放气。额外充入30%CaCO_3并增加熔化时间(相比于额外充入20%)能量达到3.4 kWh / kg,熔化发生剧烈,形成了强烈的气体。因此,实验发现最佳浓度的额外电荷可产生20%CaCO_3。目前存在这样的原则可能性,即,将废料与附加的装料白云石(CaCO_3)熔融以产生废料,并产生细的矿棉作为复合材料的组成部分,以及用于纤维结构的绝缘材料。

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