Three-phase catalytic oxidization wastewater treatment method and reactor

A sewage treatment method and technology of the treatment method, which are applied in the directions of oxidized water/sewage treatment, water/sewage treatment, illumination water/sewage treatment, etc., can solve the problem of increasing the cost of the treatment process, the inability to generate three phases simultaneously, and the expensive cost of the catalytic unit. and other problems, to achieve the effect of improving the oxidation reaction efficiency, fully utilizing the oxidant, and prolonging the hydraulic retention time.

Inactive Publication Date: 2017-08-18
中化学朗正环保科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] However, in the current existing technology, the ultraviolet light treatment process and the ozone generator reaction stage are independent of each other and are carried out step by step. Although a catalytic unit is used in some processes, the cost of the catalytic unit is expensive.
Moreover, the existing equipment is limited by the physical state of the participating reactants. The three phases cannot be produced synchronously or cannot be fully contacted. The reaction efficiency is low, resulting in waste of oxidant, which not only increases the cost of the treatment process, but also causes a large amount of residual oxidant to be discharged, resulting in secondary pollution.

Method used

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  • Three-phase catalytic oxidization wastewater treatment method and reactor

Examples

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Embodiment 1

[0036] Comply with the above technical solutions, such as figure 1 As shown, this embodiment provides a three-phase catalytic oxidation sewage treatment method: first add ozone microbubbles to the sewage to be treated, and then use an air-dissolving device to dissolve ozone in the sewage to be treated, and release it in the reaction vessel For micro-bubbles, the air-holding equipment can be dissolved air pump, pressure dissolved air tank, etc., not limited to the above dissolved air methods;

[0037] While irradiating the solid catalyst with ultraviolet light, the sewage to be treated contacts the solid catalyst, and drives the solid catalyst to move upward in a fluidized state to react, the solid catalyst settles, and the ozone microbubbles are either consumed, broken, or attached to the catalytic particles On, or released, after the sewage to be treated is reacted, the refractory organic matter is effectively removed. After testing, using this method, the COD removal rate c...

Embodiment 2

[0039] This embodiment provides a reactor, which includes a columnar housing 1, the lower part of the housing 1 is provided with a water inlet 2, the upper part of the housing 1 is provided with a water outlet 3, and the central axis of the inner cavity of the housing 1 is provided with a columnar The diversion reaction cylinder 4, the diversion reaction cylinder 4 is not completely in contact with the bottom of the housing 1 and the height of the diversion reaction cylinder 4 is lower than the height of the housing 1, and the inner cavity of the housing 1 is provided with A plurality of ultraviolet generators 5 use ultraviolet photocatalytic oxidants to promote advanced oxidation reactions. In consideration of safety, a pressure relief hole 6 is processed on the top of the casing 1 .

[0040]The ultraviolet generator 5 includes an ultraviolet lamp tube or an industrial ultraviolet tube. The luminous wavelength of the ultraviolet generator 5 includes 254nm or 365nm, especially...

Embodiment 3

[0051] This example differs from Comparative Example 1 in that: the gas production rate of the ozone generator is 10g / h, the effective ozone volume is 945, and the sewage to be treated enters the reactor at a linear velocity of 1.5m / h and a water inlet pressure of 30kPa.

[0052] The sewage stays in the whole reaction process for 20 minutes and then enters the product water tank. The COD of the product water is 73.12, and the COD removal rate is 66.47%.

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Abstract

The invention provides a three-phase catalytic oxidization wastewater treatment method and a reactor; ozone is added to wastewater to be treated, the wastewater to be treated is brought in contact with a solid catalyst in ultraviolet and is driven to move up in fluidized form under the joint action of flotation of adhering microbubbles and a flow of central tube incoming liquid so as to carry out reaction, the ozone is consumed by organic pollutants, the solid catalyst precipitates, and biorefractory organic matters are removed effectively. A guide reaction barrel is arranged in the reactor and is not in full contact with the bottom of a shell, the height of the guide reaction barrel is not less than that of the shell, and a plurality of ultraviolet generators are arranged around the guide reaction barrel within the shell. Dissolved gas wastewater containing massive ozone microbubble s is formed by using ozone dissolved gas, the dissolved gas wastewater is subjected to contact reaction with the active carbon solid catalyst that carries catalytic ingredients such as TIO2, ultraviolet irradiation assists in catalysis, simultaneous full contact of solid, liquid and gas is achieved, and oxidative reaction efficiency is improved.

Description

technical field [0001] The invention belongs to the technical field of sewage treatment, and in particular relates to a three-phase catalytic oxidation sewage treatment method and a reactor based on the method. Background technique [0002] Ozone is a strong oxidant that can oxidize and decompose organic matter and reducing inorganic matter in water, and at the same time use biochemical oxidation reactions to kill bacteria and viruses, but the ability to decompose toxic and harmful substances with ozone alone is limited, especially those complex macromolecules , Ring structure pollutants. Therefore, people often introduce transition metals and their oxides such as TiO 2 The ozone oxidation catalyst is used to accelerate the reaction, which can oxidize and decompose pollutants into CO 2 、H 2 O and other non-toxic and harmless substances. [0003] However, in the current prior art, the ultraviolet light treatment process and the ozone generator reaction stage are independe...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/32C02F1/78
CPCC02F1/32C02F1/725C02F1/78C02F2201/3227
Inventor 卢伟戴雪峰章启粉
Owner 中化学朗正环保科技有限公司
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