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System and method for advanced treatment of coking wastewater

A technology for advanced treatment and coking wastewater, used in water/sewage treatment, natural water treatment, chemical instruments and methods, etc., can solve the problem of ineffective coking wastewater treatment, improve the biological denitrification effect and treatment efficiency, strengthen the Electric neutralization ability, the effect of improving the flocculation effect

Inactive Publication Date: 2019-11-26
SICHUAN DAXING ENERGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The purpose of the present invention is to provide an advanced treatment system and treatment method for coking wastewater, so as to solve the problem that the treatment effect of existing coking wastewater is not obvious

Method used

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  • System and method for advanced treatment of coking wastewater
  • System and method for advanced treatment of coking wastewater
  • System and method for advanced treatment of coking wastewater

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Experimental program
Comparison scheme
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Embodiment 1

[0036] Please refer to figure 1 and figure 2 , the advanced treatment system of coking wastewater in this embodiment, which includes: an initial pretreatment unit, an enhanced pretreatment unit, a biological denitrification unit, and a biological desulfurization unit connected in sequence, and an arrangement between the pretreatment unit and the enhanced pretreatment unit With dissolved air flotation device;

[0037] The initial pretreatment unit includes: a degreasing pool and a regulating pool connected in sequence.

[0038] The enhanced preprocessing unit includes a first AS enhanced pool and a second AS enhanced pool connected in sequence. The sludge in the second AS strengthening tank is partially returned to the first AS strengthening tank.

[0039] The biological denitrification unit includes: the facultative A-section pool, the aerobic O-section pool, the MBR membrane biological reaction pool and the coagulation pool connected in sequence.

[0040]The biological d...

Embodiment 2

[0042] The advanced treatment method of coking wastewater of the present embodiment adopts the above-mentioned advanced treatment system of coking wastewater, comprising the following steps:

[0043] (1) The coking wastewater is passed into the degreasing tank to remove the oil and suspended solids in the wastewater, and then passed into the regulating tank through aeration and stirring for homogenization; among them, the main indicators of the coking wastewater are as follows: COD: 5000mg / L; SS: 150mg / L; pH: 6; Volatile phenols: 1000mg / L; Ammonia nitrogen: 200mg / L; Sulfide: 20mg / L; Cyanide: 10mg / L.

[0044] (2) Under the action of the dissolved air flotation device, the wastewater treated by the primary pretreatment unit is sequentially transported to the first AS intensification pool and the second AS intensification pool for treatment; the sludge generated in the second AS intensification pool is partially returned to The first AS strengthening pool;

[0045] (3) Pass the...

Embodiment 3

[0054] The advanced treatment method of coking wastewater of the present embodiment adopts the above-mentioned advanced treatment system of coking wastewater, comprising the following steps:

[0055] (1) The coking wastewater is passed into the degreasing tank to remove the oil and suspended solids in the wastewater, and then passed into the regulating tank through aeration and stirring for homogenization; among them, the main indicators of the coking wastewater are as follows: COD: 7000mg / L; SS: 350mg / L; pH: 7; Volatile phenols: 2000mg / L; Ammonia nitrogen: 350mg / L; Sulfide: 35mg / L; Cyanide: 20mg / L.

[0056] (2) Under the action of the dissolved air flotation device, the wastewater treated by the primary pretreatment unit is sequentially transported to the first AS intensification pool and the second AS intensification pool for treatment; the sludge generated in the second AS intensification pool is partially returned to The first AS strengthening pool;

[0057] (3) Pass the...

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Abstract

The invention discloses a system and method for advanced treatment of coking wastewater, and belongs to the technical field of coking industrial wastewater treatment. The system comprises a primary pretreatment unit, an enhanced pretreatment unit, a biological denitrification unit and a biological desulfurization unit which are connected in sequence, and a dissolved air flotation device is arranged between the pretreatment unit and the enhanced pretreatment unit; the primary pretreatment unit comprises an oil removal tank and an adjusting tank which are connected in sequence; the enhanced pretreatment unit comprises a first AS enhanced tank and a second AS enhanced tank which are connected in sequence; the biological denitrification unit comprises a facultative anaerobic A-section tank, anaerobic O-section tank, an MBR tank and a coagulation tank which are connected in sequence; and the biological desulfurization unit comprises a first BDS pool, a second BDS pool, a third BDS pool anda biological fluidized bed which are connected in sequence. The system and the method have the advantages of high biodegradability, high removal rate of total nitrogen and total sulfur, high treatment effect, realization of deep denitrification and deep desulfurization of coking wastewater, and meeting of high requirements of coking wastewater treatment.

Description

technical field [0001] The invention relates to the technical field of coking industrial wastewater treatment, in particular to an advanced treatment system and treatment method for coking wastewater. Background technique [0002] Coking wastewater is mixed wastewater produced in the process of coke oven raw coal gasification production and recovery, which contains a large amount of volatile phenols, polycyclic aromatic hydrocarbons and heterocyclic compounds such as oxygen, sulfur, nitrogen, etc., and has high COD, high nitrogen, high chroma, Refractory to degradation and other characteristics, which mainly come from the ammonia distillation process. In addition, a stream of waste liquid will be produced during the alkali washing process of the vacuum potassium carbonate desulfurization process, which contains a large amount of sulfide, cyanide, phenol, etc. Although the amount of waste water is not large, However, the concentration of pollutants is extremely high, which ha...

Claims

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Application Information

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IPC IPC(8): C02F9/14C02F101/10C02F101/16C02F103/34
CPCC02F9/00C02F1/40C02F1/24C02F3/30C02F1/5245C02F1/5236C02F1/56C02F2101/101C02F2101/16C02F2103/34
Inventor 吴映忠李正清张光辉王新星龙素安王晨晖
Owner SICHUAN DAXING ENERGY