Deep treatment method and device of coking wastewater

A technology for advanced treatment and coking wastewater, applied in the direction of oxidized water/sewage treatment, natural water treatment, chemical instruments and methods, etc., can solve the problems of high cost of advanced treatment, failure to achieve COD of effluent, poor biodegradability of wastewater, etc., to avoid Effects of unsafe factors and potential health hazards, reasonable process and device system design, and strong engineering application value

Inactive Publication Date: 2015-04-08
WUHAN IRON & STEEL (GROUP) CORP
View PDF3 Cites 12 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] Coking wastewater is a recognized industrial wastewater that is difficult to biodegrade. The difficulty lies in the poor biodegradability of the wastewater. In addition to inorganic pollutants such as ammonia, cyanide, and thiocyanate, it also contains impurities such as phenols, naphthalene, pyridine, and quinoline. Cyclic and polycyclic aromatic compounds (PAHS) are difficult to biodegrade. These substances can have long-term effects on the environment, and some of them have been confirmed as carcinogens by research. In addition, high concentrations of ammonia nitrogen have a strong inhibitory effect on microbial activity. Biodegradation Nitrogen is not effective
At present, the treatment of coking wastewater generally adopts biological treatment methods based on A/O or A/O/O, A/A/O, O/A/O and other biologically enhanced processes after A/O process improvement. The biological treatment method is often supplemented by coagulation and sedimentation treatment, which barely meets the discharge standard requirements. In addition, due to the high cost of advanced treatment, many coking plants in China are discouraged, so most coking wastewater is directly discharged after secondary treatment
However, although the wastewater has undergone the above-mentioned tr

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Deep treatment method and device of coking wastewater
  • Deep treatment method and device of coking wastewater

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] The method for advanced treatment of coking wastewater, its steps:

[0034] 1) Adjust the pH value of the wastewater after conventional biochemical and coagulation treatment to 7, and then enter the multimedia filter 7 for filtration;

[0035] 2) The wastewater filtered by the multimedia filter 7 enters the first-level ozone reaction tower 2, and ozone is added to the wastewater at a rate of 50 mg / L, stirred and the hydraulic retention time is 21 minutes, so that the wastewater and ozone can fully react;

[0036] 3) The wastewater from the first-level ozone reaction tower 2 enters the second-level ozone reaction tower 3, and without adding ozone, stir and make the hydraulic retention time 19 minutes, so that the wastewater and ozone can fully react again;

[0037] 4) The wastewater treated by the secondary ozone reaction tower 3 enters the corridor-shaped closed intermediate pool 8 for ozonolysis, and the hydraulic retention time of the wastewater in it is 35 minutes; ...

Embodiment 2

[0042] The method for advanced treatment of coking wastewater, its steps:

[0043] 1) Adjust the pH value of the wastewater after conventional biochemical and coagulation treatment to 8, and then enter the multimedia filter 7 for filtration;

[0044] 2) The wastewater filtered by the multimedia filter 7 enters the first-level ozone reaction tower 2, and ozone is added to the wastewater at a rate of 60 mg / L, stirred and the hydraulic retention time is 26 minutes, so that the wastewater and ozone can fully react;

[0045] 3) The wastewater from the first-level ozone reaction tower 2 enters the second-level ozone reaction tower 3, and ozone is added to the wastewater at a rate of 10 mg / L, stirred and the hydraulic retention time is 15 minutes, so that the wastewater and ozone can fully react again;

[0046] 4) The wastewater treated by the secondary ozone reaction tower 3 enters the corridor-shaped closed intermediate pool 8 for ozone decomposition, and the hydraulic retention t...

Embodiment 3

[0051] The method for advanced treatment of coking wastewater, its steps:

[0052] 1) Adjust the pH value of the wastewater after conventional biochemical and coagulation treatment to 8.5, and enter the multimedia filter 7 for filtration;

[0053] 2) The wastewater filtered by the multimedia filter 7 enters the first-level ozone reaction tower 2, and ozone is added to the wastewater at a rate of 70 mg / L, stirred and the hydraulic retention time is 30 minutes, so that the wastewater and ozone can fully react;

[0054] 3) The waste water from the first-level ozone reaction tower 2 enters the second-level ozone reaction tower 3, and ozone is added according to 20 mg / L of waste water, stirred and the hydraulic retention time is 21 minutes, so that the waste water and ozone can fully react again;

[0055] 4) The wastewater treated by the secondary ozone reaction tower 3 enters the corridor-shaped closed intermediate pool 8 for ozonolysis, and the hydraulic retention time of the wa...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention discloses a deep treatment method of coking wastewater. The method comprises the following steps of firstly adjusting pH of wastewater and filtering; reacting in a first-stage ozone reaction tower and a second-stage ozone reaction tower; carrying out ozonolysis in an enclosed intermediate water tank; treating in an aeration biological filtering tank; and introducing non-decomposed ozone into a tail gas absorber or destroyer. A treatment device mainly comprises a mixing sedimentation tank, the first-stage ozone reaction tower, the second-stage ozone reaction tower, the aeration biological filtering tank and conveying pipes, wherein the conveying pipe between the mixing sedimentation tank and the first-stage ozone reaction tower is connected with a multi-medium filter; and the conveying pipe between the second-stage ozone reaction tower and the aeration biological filtering tank is connected with the enclosed intermediate water tank and the tail gas absorber or destroyer is connected with two ozone reaction towers and the enclosed intermediate water tank. By combining ozone catalytic ozonation and the aeration biological filtering tank, non-biodegradable organic substances in wastewater are oxidized by virtue of ozone and mineralized or partially oxidized into easily degradable small molecular organic substances and the small molecular organic substances can be subjected to subsequent treatment by virtue of cheap organisms in the aeration biological filtering tank.

Description

technical field [0001] The invention relates to a wastewater treatment method and a treatment device, in particular to a coking wastewater advanced treatment method and device. Background technique [0002] Coking wastewater is a recognized industrial wastewater that is difficult to biodegrade. The difficulty lies in the poor biodegradability of the wastewater. In addition to inorganic pollutants such as ammonia, cyanide, and thiocyanate, it also contains impurities such as phenols, naphthalene, pyridine, and quinoline. Cyclic and polycyclic aromatic compounds (PAHS) are difficult to biodegrade. These substances can have long-term effects on the environment, and some of them have been confirmed as carcinogens by research. In addition, high concentrations of ammonia nitrogen have a strong inhibitory effect on microbial activity. Biodegradation Nitrogen does not work well. At present, the treatment of coking wastewater generally adopts biological treatment methods based on A / ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
IPC IPC(8): C02F9/14
CPCC02F9/00C02F1/001C02F1/66C02F1/78C02F3/02C02F2103/365
Inventor 王丽娜薛改凤盛军波黄建阳张垒吴高明刘璞王凯军刘尚超刘霞
Owner WUHAN IRON & STEEL (GROUP) CORP
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products