一种臭氧与双氧水协同氧化处理装置

By designing a vortex distributor and a two-stage jet mixer, the problem of low mixing efficiency of ozone and hydrogen peroxide was solved, achieving high-efficiency oxidation and improved ozone utilization in the wastewater treatment device, and reducing the ozone escape rate.

CN224513282UActive Publication Date: 2026-07-17SHANDONG LIYUAN HAIDA ENVIRONMENTAL ENG

Patent Information

Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
SHANDONG LIYUAN HAIDA ENVIRONMENTAL ENG
Filing Date
2025-07-11
Publication Date
2026-07-17

AI Technical Summary

Technical Problem

Existing wastewater treatment devices have low mixing efficiency of ozone and hydrogen peroxide, resulting in slow reaction start-up and serious ozone escape, causing waste and secondary pollution.

Method used

By employing a vortex water distributor and a two-stage jet mixer, combined with a circulating pump and an intelligent control system, uniform mixing and dynamic regulation of ozone and hydrogen peroxide are achieved, thereby improving dissolution efficiency and reducing ozone escape rate.

Benefits of technology

Accelerate the reaction start-up rate, improve oxidant utilization, reduce ozone escape rate, and achieve simultaneous optimization of mass transfer efficiency and reaction kinetics.

✦ Generated by Eureka AI based on patent content.

Smart Images

  • Figure CN224513282U_ABST
    Figure CN224513282U_ABST
Patent Text Reader

Abstract

本实用新型涉及一种臭氧与双氧水协同氧化处理装置,涉及污水处理设备技术领域,包括氧化池,氧化池上设有污水进管和出水渠,出水渠连接有出水管线,氧化池内设有旋流布水器,氧化池上设有循环泵,循环泵的出口连接有连通旋流布水器的循环管,循环管上设有一级双氧水射流混合器和二级臭氧射流混合器,一级双氧水射流混合器和二级臭氧射流混合器分别连接有双氧水投加装置和臭氧投加装置。本实用新型采用“臭氧‑双氧水”两级级射流混合及旋流布水器,加快反应启动速度,提高气体溶解效率,增长反应接触时间,提高氧化剂利用率,实现传质效率与反应动力学的同步优化,并且臭氧逃逸率降低。
Need to check novelty before this filing date? Find Prior Art

Claims

1. An ozone and hydrogen peroxide synergistic oxidation treatment device, comprising an oxidation tank (1), wherein a sewage inlet pipe (101) and a water outlet channel (102) are arranged on the oxidation tank (1), and a water outlet pipeline (104) is connected to the water outlet channel (102), characterized in that: The oxidation tank (1) is equipped with a vortex water distributor (103) and a circulation pump (2) on the oxidation tank (1). The outlet of the circulation pump (2) is connected to a circulation pipe (203) that connects to the vortex water distributor (103). The circulation pipe (203) is equipped with a primary hydrogen peroxide jet mixer (3) and a secondary ozone jet mixer (4). The primary hydrogen peroxide jet mixer (3) and the secondary ozone jet mixer (4) are respectively connected to a hydrogen peroxide dosing device and an ozone dosing device.

2. The device for ozone and hydrogen peroxide synergistic oxidation treatment according to claim 1, characterized in that, The vortex water distributor (103) includes a conveying pipe (105) fixed on the oxidation tank (1) and connected to the circulation pipe (203). The bottom outer side of the conveying pipe (105) is provided with at least one ring of distribution pipe (1031). The bottom of the conveying pipe (105) has a circular array of multiple guide pipes (1033). The other end of the guide pipe (1033) is fixed to the outermost ring of distribution pipe (1031). Each guide pipe (1033) is provided with a branch pipe (1034) connected to the other inner ring of distribution pipe (1031). The distribution ring pipe (1031) is provided with a distribution spray pipe (1032).

3. The device for ozone and hydrogen peroxide synergistic oxidation treatment according to claim 2, characterized in that, Multiple distribution spray pipes (1032) are evenly arranged on the outer side wall of the distribution ring pipe (1031), and each distribution spray pipe (1032) is arranged along the tangential direction of the distribution ring pipe (1031).

4. The device for ozone and hydrogen peroxide synergistic oxidation treatment according to claim 1, characterized in that, The inlet of the circulating pump (2) is connected to a water supply pipe 1 (201) and a water supply pipe 2 (202). The other ends of the water supply pipe 1 (201) and the water supply pipe 2 (202) are respectively connected to the bottom of the sewage inlet pipe (101) and the outlet channel (102).

5. The device for ozone and hydrogen peroxide synergistic oxidation treatment according to claim 4, characterized in that, The hydrogen peroxide dosing device includes a hydrogen peroxide storage tank (5), which is connected to a primary hydrogen peroxide jet mixer (3) via a pipeline, and a dosing pump (9) is installed on the pipeline.

6. The device for ozone and hydrogen peroxide synergistic oxidation treatment according to claim 5, characterized in that, The ozone dosing device includes an ozone generator (6), and the outlet pipe of the ozone generator (6) is connected to a secondary ozone jet mixer (4).

7. The device for ozone and hydrogen peroxide synergistic oxidation treatment according to claim 1, characterized in that, The top of the oxidation tank (1) is a closed structure. The top of the oxidation tank (1) is provided with a tail gas outlet pipe (701), and the tail gas outlet pipe (701) is connected to a tail gas destroyer (7).

8. The device for ozone and hydrogen peroxide synergistic oxidation treatment according to claim 5, characterized in that, The outlet channel (102) is equipped with an online UV254 detector (801), and the oxidation tank (1) is also equipped with an ORP sensor (802) and an ozone concentration monitor (803). The ORP sensor (802), the ozone concentration monitor (803) and the online UV254 detector (801) are connected to a PLC controller (8). The PLC controller (8) is connected to an ozone generator (6) and a dosing pump (9).