首页> 外国专利> A METHOD FOR REMOVING TOTAL NITROGEN CONTENT IN WASTE WATER OF PROCESS FOR PREPARING COKE

A METHOD FOR REMOVING TOTAL NITROGEN CONTENT IN WASTE WATER OF PROCESS FOR PREPARING COKE

机译:一种去除焦炭过程中废水中总氮含量的方法

摘要

PURPOSE: Provided is a method for removing total nitrogen content in wastewater from coke manufacturing process which can prevent bad influences such as eutrophication due to nitrogen on environment when discharged in hydrospheres and can reduce the amount of sodium hydroxide used for the pH control of wastewater. CONSTITUTION: At first, control the pH of wastewater within the range of 8.8 to 9.5 by controlling the dosage of sodium hydroxide. If the concentration of non-degradable NH3-N is below 270 ppm in wastewater, transfer the wastewater into denitrification tank(200) and if the concentration of non-degradable NH3-N is over 270 ppm, return the wastewater to distilling equipment(100) and add sodium hydroxide to let down the concentration of NH3-N in the range of pH 8.8 to 9.5. The circulation of wastewater from denitrification tank to nitrification tank(300) converts NH3-N into NO3-N in nitrification tank and converts NO3-N to nitrogen gas in denitrification tank and if the concentration of NO3-N in the nitrification tank is below 1 ppm, transfer the wastewater into settler(400) and if the concentration of NO3-N is over 1 ppm, add electro donor into wastewater to let down the concentration. If the concentration of total nitrogen in wastewater from thickener(500) is below 60 ppm, discharge that and if the concentration is over 60 ppm, return that to the distilling equipment. The electron donor is selected from methanol, ethanol, acetic acid and acetone.
机译:目的:提供一种去除焦炭生产过程中废水中总氮含量的方法,该方法可防止排放到水圈中的氮对环境造成不良影响,例如因环境中的氮富营养化,并可减少用于废水pH值控制的氢氧化钠量。组成:首先,通过控制氢氧化钠的用量将废水的pH值控制在8.8至9.5之间。如果废水中不可降解的NH3-N的浓度低于270 ppm,则将废水转移到反硝化池(200)中,如果不可降解的NH3-N的浓度超过270 ppm,则将废水返回蒸馏设备(100) ),然后加入氢氧化钠,使NH3-N的浓度降低至pH 8.8至9.5。从硝化池到硝化池的废水循环(300)如果硝化池中的NO3-N浓度低于1,则在硝化池中将NH3-N转化为NO3-N,在硝化池中将NO3-N转化为氮气。 ,将废水转移到沉降器(400)中,如果NO3-N的浓度超过1 ppm,则将电施主添加到废水中以降低浓度。如果浓缩器(500)废水中的总氮浓度低于60 ppm,则将其排放;如果浓度超过60 ppm,则将其返回蒸馏设备。电子给体选自甲醇,乙醇,乙酸和丙酮。

著录项

  • 公开/公告号KR100468446B1

    专利类型

  • 公开/公告日2005-01-29

    原文格式PDF

  • 申请/专利权人

    申请/专利号KR20000081399

  • 发明设计人 나한길;김인곤;

    申请日2000-12-23

  • 分类号C02F9/14;

  • 国家 KR

  • 入库时间 2022-08-21 22:04:10

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

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