环境卫生工程 ›› 2026, Vol. 34 ›› Issue (2): 42-48.doi: 10.19841/j.cnki.hjwsgc.2026.02.006

• 固体废物处理过程衍生污染控制 • 上一篇    下一篇

江苏某转运站压滤液协同填埋场渗滤液处理项目设计和研究

施至理   

  1. 上海环境卫生工程设计院有限公司
  • 出版日期:2026-04-28 发布日期:2026-04-28

Design and Research on the Treatment Project of Leachate from Transfer Station Combined with Landfill Leachate in Jiangsu

SHI Zhili   

  1. Shanghai Environmental Sanitation Engineering Design Institute Co. Ltd.
  • Online:2026-04-28 Published:2026-04-28

摘要: 针对封场后填埋场渗滤液老龄化难处理问题,利用中转站压滤液高COD、低氨氮的特点,对分散的中转站压滤液集中收集后运至填埋场进行协同处理。以江苏某市的中转站压滤液协同封场填埋场渗滤液为例,封场后填埋场渗滤液产生量为250 m3/d,中转站压滤液产生量为100 m3/d,现填埋场渗滤液处理站规模为600 m3/d,主要处理工艺为预处理+外置式MBR+超滤(NF)+反渗透(RO),NF和RO浓缩液进行减量化后蒸发处理,根据混合液的水质、水量对现有填埋场渗滤液的设备和设施进行核算。经核算,现有建构筑物和设备仅需部分开启,其余作为备用或部分设备降低日运行时间即可满足混合液的处理且能达标。根据测算,协同处理的渗滤液工艺段“预处理+外置式MBR+NF+RO+浓缩液减量化”运行成本为93.53元/m3;浓缩液蒸发段运行成本为365.27元/m3;与分散处理工艺相比,该协同处理工艺可节约成本196.74万元/a。协同处理系统整体运行良好,出水水质稳定达标,实现了集约化布置和节能的目标。

关键词: 中转站压滤液, 填埋场渗滤液, 老龄化, 碳源, 浓缩液蒸发, 运行成本

Abstract: According to the problems of landfill leachate aging and difficult treatment after closure, the scattered pressure filtrate from the transfer station was collected and transported to the landfill for synergistic treatment by using its characteristics of high COD and low ammonia nitrogen. Taking the leachate from transfer station combined with landfill leachate in a city of Jiangsu as an example, the landfill leachate production after the closure was 250 m3/d, the pressure filtrate production from the transfer station was 100 m3/d, and the processing scale of current landfill leachate treatment station was 600 m3/d. The main treatment process is pretreatment + external MBR + NF + RO. NF and RO concentrate are evaporated after reduction, and the equipment and facilities of the existing landfill leachate are calculated according to the water quality and quantity of the mixture. According to the calculation, the existing buildings and equipment only need to be partially opened, and the rest can be used as standby or part of the equipment to reduce the daily operation time to meet the treatment of the mixed liquid and meet the standard. According to the calculation, the operating cost of the leachate co-processing section of “pretreatment + external MBR + NF + RO + concentrate reduction” is 93.53 yuan/m3, the operation cost of the evaporation section of the concentrated liquid is 365.27 yuan/m3. Compared with the decentralized treatment process, the synergistic treatment process can save the cost of 1.967 4 million yuan per year. The overall operation of the collaborative treatment system is good, and the effluent quality is stable and up to standard, which achieves the goal of intensive layout and energy saving.

Key words: transfer station pressure filtrate, landfill leachate, aging, carbon source, concentrated liquid evaporation, running cost

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