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作 者:雷玉锋 刘忠 吴振山 高磊 张国强 程乐 Lei Yufeng;Liu Zhong;Wu Zhenshan;Gao Lei;Zhang Guoqiang;Cheng Le(Hefei Zhongke Juneng Engineering Technology Co.,Ltd.,Hefei 230601;Inner Mongolia Yitai Coal-to-Liquid Co.,Ltd.,Zhungeer 010321;Nanjing PaiRate New Material Technology Co.,Ltd.,Nanjing 210012)
机构地区:[1]合肥中科聚能工程科技有限公司,安徽合肥230601 [2]内蒙古伊泰煤制油有限责任公司,内蒙古准格尔旗010321 [3]南京湃率新材料科技有限公司,江苏南京210012
出 处:《大氮肥》2021年第2期120-123,126,共5页Large Scale Nitrogenous Fertilizer Industry
摘 要:碎煤气化产生的煤气废水富含酚、氨等有害物质,以脱酸、脱氨及萃取的酚氨回收工艺可从煤气废水中提炼出粗酚和氨水,并实现废水循环利用。通过对系统运营费用分析,得出走脱酸、脱氨及萃取的常规酚氨回收工艺路线,其经济盈亏平衡的前提是待处理废水中初始酚、氨含量同时达到9.2 g/L或以上。适当追加对脱氨塔和酚塔的设备投资,可显著降低运行费用。同时,还能有效降低满足盈亏平衡时的酚和氨初始浓度指标。The coal gas wastewater produced by crushed coal gasification is rich in harmful substances such as phenol and ammonia.The phenol-ammonia recovery process of deacidification,deamination and preextraction can extract crude phenol and ammonia from the coal gas wastewater,and can realize the wastewater recycling.Through the analysis of the operating cost of the system,the economic break-even point of the conventional phenol ammonia recovery process route is obtained.The break-even point is that the initial content of phenol and ammonia is 9.2 g/L at the same time.Appropriate additional investment in the ammonia tower and phenol tower can significantly reduce operating costs.At the same time,it can significantly reduce the index requirements for the initial concentration of phenol and ammonia in the wastewater.
分 类 号:X784[环境科学与工程—环境工程]
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