Method and device for sewage treatment

Patent metadata

Field	Value
Publication number	US-11352271-B2
Application number	US-201916578119-A
Country	US
Kind code	B2
Filing date	Sep 20, 2019
Priority date	Jun 26, 2019
Publication date	Jun 7, 2022
Grant date	Jun 7, 2022

Abstract

A device for sewage treatment comprises a treatment tank, a power and electric control unit, a gas supply and tail gas recovery unit and a circular reaction treatment unit; the treatment tank is provided with a liquid inlet, a liquid outlet, a gas intake port and a tail gas exhaust port; the gas supply and tail gas recovery unit is communicated with the treatment tank through the gas intake port; the tail gas exhaust port is communicated with the gas supply and tail gas recovery unit; the circular reaction treatment unit comprises an external circulating device and a reaction treatment element arranged inside the treatment tank.

First claim

What is claimed is:

1. A device for treating sewage, comprising a treatment tank, a power and electric control unit, a gas supply and tail gas recovery unit, an external circulating device for making water circulation and a reaction treatment element, wherein the treatment tank is provided with a liquid inlet ( 30 ), a liquid outlet ( 18 ), a gas intake port and a tail gas exhaust port; the gas supply and tail gas recovery unit is communicated with the treatment tank through the gas intake port; the tail gas exhaust port is communicated with the gas supply and tail gas recovery unit; the reaction treatment element is arranged inside the treatment tank; the external circulating device is arranged outside the treatment tank and is communicated with the liquid inlet ( 30 ) and the liquid outlet ( 18 ) respectively; the power and electric control unit is connected with the reaction treatment element; and sewage to be processed enters the treatment tank through the liquid inlet ( 30 ) and reacts with ferrites in the reaction treatment element;
wherein the power and electric control unit comprises a wind power generator ( 1 ), a solar panel ( 2 ), a Uninterruptible Power Supply ( 3 ), a constant current meter ( 4 ), a first electrode switch ( 5 ), a second electrode switch ( 6 ) and a third electrode switch ( 7 ); the gas supply and tail gas recovery unit comprises an oxygen carrier ( 11 ), an ozone generator ( 10 ), a tail gas exhaust valve ( 25 ) and a tail gas absorption device ( 26 ); the external circulating device a liquid flowmeter ( 31 ) and a peristaltic pump ( 32 ); and the reaction treatment element comprises a micro-nano aeration disk, an electrochemical cathode, a three-dimensional particle electrode and an electrochemical anode.

2. The device according to claim 1 , wherein the micro-nano aeration disk, the electrochemical cathode, the three-dimensional particle electrode and the electrochemical anode are arranged in the treatment tank from front to back in sequence; the power and electric control unit is respectively connected with the electrochemical cathode and the electrochemical anode; the gas intake port is communicated with the treatment tank and is connected with the micro-nano aeration disk; and a persulfate layer is filled between the electrochemical cathode and the electrochemical anode.

3. The device according to claim 2 , wherein the electrochemical cathode is selected from the group consisting of a ferrite-modified Mxene layered gas diffusion electrode and a ferrite-modified carbon fiber cloth electrochemical cathode; the three-dimensional particle electrode is an electrode formed by an in-situ growing MOFs nano-material of a magnetic carbon material;
and the electrochemical anode is a stainless steel mesh electrode, a platinum mesh electrode and/or a titanium mesh electrode.

4. The device according to claim 3 , wherein the micro-nano aeration disk discharges micro-nano bubbles and the micro-nanobubbles have a size of 200 nm to 500 nm.

5. The device according to claim 4 , wherein the peristaltic pump ( 32 ) is communicated with the liquid inlet ( 30 ) on the treatment tank through the liquid flowmeter ( 31 ); and the liquid outlet ( 18 ) on the treatment tank is communicated with the peristaltic pump ( 32 ).

6. The device according to claim 5 , wherein the oxygen carrier ( 11 ) is communicated with the treatment tank through the ozone generator ( 10 ) and the gas intake port in sequence; the oxygen carrier ( 11 ) is communicated with the treatment tank through the gas intake port; and the tail gas exhaust port is communicated with the tail gas absorption device ( 26 ) through the tail gas exhaust valve ( 25 ).

7. The device according to claim 6 , wherein the wind power generator ( 1 ) is connected with the Uninterruptible Power Supply (UPS) ( 3 ) through the solar panel ( 2 ); the UPS ( 3 ) is respectively connected with the first electrode switch ( 5 ) and the second electrode switch ( 6 ) through the constant current meter ( 4 ); and the first electrode switch ( 5 ) and the second electrode switch ( 6 ) are respectively connected with the reaction treatment element arranged inside the treatment tank.

Assignees

• Univ Central South

Inventors

• Li Haipu
• Yao Jingjing
• Yang Zhaoguang
• Dong Qingqing
• Dai Ximei
• Pan Siyuan
• Yuan Nadi

Classifications

• C02F2209/40

  Liquid flow rate · CPC title

• C02F2305/023

  Reactive oxygen species, singlet oxygen, OH radical · CPC title

• C02F1/46109 Primary

  Electrodes · CPC title

• C02F1/722

  Oxidation by peroxides · CPC title

• C02F2201/46165

  Special power supply, e.g. solar energy or batteries · CPC title