化工进展 ›› 2025, Vol. 44 ›› Issue (1): 100-108.DOI: 10.16085/j.issn.1000-6613.2023-2298

• 化工过程与装备 • 上一篇    下一篇

基于两级微通道分离工艺的甲醇制烯烃废水深度处理

周渝1(), 唐甜1(), 熊子悠2, 韦奇2   

  1. 1.陕西化工研究院有限公司,陕西 西安 710061
    2.华东理工大学机械与动力工程学院,上海 200237
  • 收稿日期:2023-12-31 修回日期:2024-02-21 出版日期:2025-01-15 发布日期:2025-02-13
  • 通讯作者: 唐甜
  • 作者简介:周渝(1985—),女,硕士,高级工程师,研究方向为工业污水处理技术。E-mail:1321619445@qq.com

Methanol to olefin wastewater treatment based on a two-stage microchannel separation process

ZHOU Yu1(), TANG Tian1(), XIONG Ziyou2, WEI Qi2   

  1. 1.Shaanxi Institute of Chemical Technology Co. , Ltd. , Xi’an 710061, Shaanxi, China
    2.School of Mechanical and Power Engineering, East China University of Science and Technology, Shanghai 200237, China
  • Received:2023-12-31 Revised:2024-02-21 Online:2025-01-15 Published:2025-02-13
  • Contact: TANG Tian

摘要:

甲醇制烯烃(MTO)工艺中,因原始设计的缺陷,工艺水中的芳烃和重组分不能被汽提出来,导致污水汽提塔底部的净化水中仍含有一定量的悬浮态和胶体态污染物,化学需氧量(COD)含量较高,成为实现废水回用的障碍。针对当前MTO废水处理的这一技术短板,本文以现场实验为基础,提出了一种新型的旋流再生型微通道分离器串联流程用以分级处理MTO净化水,一级分离器用于去除净化水中的非溶解态污染物,降低部分COD含量,二级分离器用于深度去除COD。其中吸附剂选择一级MC-1、二级MC-4具有最佳的吸附效率,床层截面流速控制在2.5mm/s最为合适。经处理后的净化水平均浊度由18.3NTU降低至2NTU,悬浮物含量由进口的18mg/L降至2.79mg/L,分离效率基本高于80%,化学需氧量COD含量平均降低了318mg/L,分离净化效果明显,经处理后的净化水可替代透平凝液用于烯烃分离水洗塔或回用至其他用水单元。该工艺具有低成本,对悬浮态颗粒、胶体态颗粒、小分子有机物去除效率高,分离媒质再生彻底等特点,有效解决了甲醇制烯烃(MTO)工艺中废水回用难的问题,对减少环境污染节约水资源有着重要意义。

关键词: 甲醇制烯烃, 废水处理, 微通道分离, 旋流再生, 化学需氧量

Abstract:

In the methanol to olefins (MTO) process, the defects of the original design leads aromatic hydrocarbons and heavy components in the process water cannot to be proposed by steam, resulting in a certain amount of suspended and colloidal pollutants in the purified water at the bottom of the sewage stripper. The high content of chemical oxygen demand (COD) has become an obstacle to the reuse of wastewater. In view of the shortcomings of the current MTO wastewater treatment technology, this paper proposed a new type of cyclone regeneration microchannel separator series process based on field experiments, which was used to classify and treat MTO purified water. The primary separator was used to remove non-dissolved pollutants in purified water and reduce some COD content, and the secondary separator was used to deeply remove COD. The first-stage adsorbent MC-1 and the second-stage adsorbent MC-4 had the best adsorption efficiency, and the cross-sectional flow rate of the bed was most suitable to be controlled at 2.5mm/s. The average turbidity of the purified water after treatment was reduced from 18.3NTU to 2NTU, the suspended solids content was reduced from 18mg/L to 2.79mg/L, the separation efficiency was basically higher than 80%, and the chemical oxygen demand COD content was reduced by 318mg/L on average. The separation and purification effect was obvious. The purified water after treatment can replace the turbine condensate for olefin separation water washing tower or reuse to other water units. The process had the characteristics of low cost, high removal efficiency of suspended particles, colloidal particles and small molecular organic matter, and complete regeneration of separation media. It effectively solved the problem of difficult reuse of wastewater in the process of methanol to olefins (MTO). It was of great significance to reduce environmental pollution and save water resources.

Key words: methanol to olefins, wastewater treatment, microchannel separation, swirl regeneration, chemical oxygen demand (COD)

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