首页> 外文期刊>RSC Advances >Study on the pyrolysis treatment of HPF desulfurization wastewater using high-temperature waste heat from the raw gas from a coke oven riser
【24h】

Study on the pyrolysis treatment of HPF desulfurization wastewater using high-temperature waste heat from the raw gas from a coke oven riser

机译:焦炉立管原料气高温余热热解HPF脱硫废水的研究

获取原文
           

摘要

Thermogravimetric TG and a single riser from an industrial 4.3 m coke oven were used as pyrolysis reactors to systematically study the newly developed pyrolysis treatment of desulfurization wastewater. The TG study showed that the mixed salt in the desulfurization wastewater was transformed into the crystalline form of ammonium thiocyanate (in the temperature range 95.87–127.38 °C), followed by the isomerization of ammonium thiocyanate to thiourea (in the temperature range 127.38–246.26 °C), involving a total of five major stages. The final pyrolysis temperature was 540 °C, and the cumulative weight loss was 99.57%. The study on the single riser from an industrial 4.3 m coke oven showed that the relationship between the spray amount of desulfurization wastewater ( v ), the temperature drop (Δ T ) and the concentration of ammonium thiocyanate ( c ) in the coke-oven raw gas at the outlet of the rising pipe were respectively Δ T = ?2.939 v and c = f ( v ). The maximum desulfurization wastewater treatment capacity of the 4.3 m single riser was 61.98 kg h ~(?1) . The spraying optimization conditions were: spraying position, 3 m from the water seal cap of the riser; spraying amount, 50–55 L h ~(?1) ; spraying time, from 10 min after the coal loading to less than 20 h during the coking process. An industrial test device for treating 12?000 tons of desulfurization wastewater was constructed, which then ran normally, with the new technology for treating the high concentration polluted wastewater–desulfurization wastewater formed.
机译:热重法TG和工业4.3 m焦炉中的单个提升管被用作热解反应器,以系统地研究新开发的脱硫废水的热解处理。 TG研究表明,脱硫废水中的混合盐转变为硫氰酸铵的结晶形式(温度范围为95.87–127.38°C),然后将硫氰酸铵异构化为硫脲(温度范围为127.38–246.26)。 °C),共涉及五个主要阶段。最终热解温度为540℃,累积失重为99.57%。对4.3 m工业焦炉的单立管进行的研究表明,焦炉原料中脱硫废水的喷雾量(v),温度下降(ΔT)与硫氰酸铵浓度(c)之间的关系。上升管出口处的气体分别为ΔT =?2.939 v和c = f(v)。 4.3 m单立管的最大脱硫废水处理能力为61.98 kg h〜(?1)。喷涂的优化条件为:喷涂位置,距立管水封盖3 m。喷洒量,50-55 L h〜(?1);喷涂时间,从装煤后10分钟到焦化过程中少于20小时。建造了用于处理12,000吨脱硫废水的工业测试设备,然后该设备正常运行,并采用了新技术来处理高浓度污染废水-形成的脱硫废水。

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