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Method and device for ultraviolet-ozone synergistic oxidation pretreatment of high-concentration wastewater

A high-concentration wastewater and collaborative oxidation technology, applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve the destructive impact of biological treatment systems, pollutant deposition, ozone dissolution Low efficiency and other problems, to achieve the effect of reducing the pressure of biochemical treatment, high treatment efficiency, and meeting the requirements of subsequent biochemical influent

Active Publication Date: 2017-04-12
CHINA NAT OFFSHORE OIL CORP +3
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, due to the high concentration of biodegradable substances and even biotoxic substances in refining wastewater, such as polycyclic compounds such as phenol, naphthalene, anthracene, and benzopyrene, etc., it will cause destructive impact on the biological treatment system.
[0003] In order to solve the problem of high-concentration chemical wastewater treatment, UV-ozone synergistic oxidation of organic pollutants is a multi-effect coupling advanced oxidation technology with mild reaction conditions, high removal efficiency, and no secondary pollution. However, this technology has ozone dissolution efficiency in wastewater. Low, pollutant deposition on the surface of ultraviolet lamps, etc.

Method used

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  • Method and device for ultraviolet-ozone synergistic oxidation pretreatment of high-concentration wastewater

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Embodiment 1

[0021] A refinery in Guangdong handles 600m of refinery wastewater per day 3 , in order to achieve the standard discharge of wastewater after treatment, investigate and investigate to find a suitable treatment process. On-site pilot test is carried out by adopting the process method of forced circulation ultraviolet-ozone synergistic oxidation pretreatment of high-concentration wastewater of the present invention, and the processing capacity of the device is 10m 3 / h, when the ozone gas concentration is 150mg / L, the dosage of 30% hydrogen peroxide is 55g / L, the pH in the reaction tank is adjusted to 3.0, and the circulation pump flow rate is 100m 3 / h, the COD drops from 21000mg / L to 4500mg / L, and the COD removal rate of the device is 78.57%, which meets the water requirements of the subsequent biochemical and advanced oxidation treatment system. After the subsequent biochemical and advanced oxidation treatment system is treated, the effluent can reach the discharge standard ...

Embodiment 2

[0023] A refinery in Shandong, daily treatment of refinery wastewater 1000m 3 , COD is still as high as 12000mg / L after degreasing, flocculation and sedimentation, and the load of the biochemical system is relatively heavy. The process method of forced circulation UV-ozone synergistic oxidation pretreatment of high-concentration wastewater of the present invention is used to carry out on-site pilot test, and the processing capacity of the device is 15m 3 / h, the concentration of ozone gas is 125mg / L, the dosage of 30% hydrogen peroxide is 24g / L, the pH in the reaction tank is adjusted to 4.5, and the circulation pump flow rate is 150m 3 / h, the COD drops from 12000mg / L to 3200mg / L, and the effluent meets the influent requirements of the subsequent biochemical treatment, reducing its treatment load.

Embodiment 3

[0025] A knitting factory in Shandong, daily treatment of printing and dyeing wastewater 800m 3 , COD between 13000-16000mg / L, dark brown. On-site pilot test is carried out by adopting the process method of forced circulation ultraviolet-ozone synergistic oxidation pretreatment of high-concentration wastewater of the present invention, and the processing capacity of the device is 10m 3 / h, the concentration of ozone gas is 100mg / L, the dosage of 30% hydrogen peroxide is 31.2g / L, the pH in the reaction tank is adjusted at about 2.5, and the flow rate of the circulating pump is 120m 3 / h, the COD drops from 15000mg / L to 4200mg / L, and the effluent is basically colorless, meeting the requirements for subsequent treatment of influent water.

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Abstract

The invention provides a method and device for pretreating high-concentration wastewater through ultraviolet-ozone co-oxidation. The method comprises the steps that high-concentration wastewater in a raw water tank and ozone are mixed to obtain milk white effluent water with ozone microbubbles, the milk white effluent water flows into a reaction tank provided with a vertical partition board, the vertical partition board divides the reaction tank into a water inlet side and a water outlet side, sulfuric acid and hydrogen peroxide are added into the water inlet side of the reaction tank, and organic pollutants are degraded under the joint action of the ozone and the hydrogen peroxide; one part of effluent water from the lower portion of the water outlet side of the reaction tank cyclically flows to the raw water tank to be subjected to another reaction, the other part of effluent water flows into an intensified reactor to be subjected to a photochemical reaction, the organic pollutants are degraded through synergistic effect of the effluent water subjected to the photochemical reaction and ozone produced subsequently, and the effluent water returns to the water inlet side of the reaction tank for a continuous reaction; produced water overflows into a produced water tank from the upper portion of the water outlet side of the reaction tank,and the subsequent biochemical treatment process is conducted after the pH value of the produced water is adjusted to range from 6 to 9. By means of the method, the treatment efficiency is high, and the treatment effect is good; the device can operate stably and is less in investment and low in operating cost.

Description

technical field [0001] The invention relates to a wastewater treatment process, in particular to a method and device for pretreating high-concentration wastewater by forced circulation ultraviolet-ozone synergistic oxidation. Background technique [0002] With the deepening of petroleum refining and the processing of low-quality crude oil, the high-concentration organic wastewater that is difficult to biodegrade is correspondingly increased, and they enter the water body and cause serious pollution to the environment. Biological treatment is often used to treat this kind of wastewater, and the aerobic method or improved aerobic method is the main method, and some also use anaerobic biological treatment. However, due to the high concentration of biodegradable substances and even biotoxic substances in refining wastewater, such as polycyclic compounds such as phenol, naphthalene, anthracene, and benzopyrene, etc., it will cause destructive impact on the biological treatment sy...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/08
Inventor 李亮滕厚开吴青郭宗斌张艳芳肖立光付春明李超郝润秋
Owner CHINA NAT OFFSHORE OIL CORP
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