CN108751576A - A kind of complete system and method for cosmetic-producing wastewater processing - Google Patents

A kind of complete system and method for cosmetic-producing wastewater processing Download PDF

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Publication number
CN108751576A
CN108751576A CN201810528728.XA CN201810528728A CN108751576A CN 108751576 A CN108751576 A CN 108751576A CN 201810528728 A CN201810528728 A CN 201810528728A CN 108751576 A CN108751576 A CN 108751576A
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China
Prior art keywords
ultrasonic
sludge
cosmetic
electric
capping
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Withdrawn
Application number
CN201810528728.XA
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Chinese (zh)
Inventor
于丽春
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Beijing Xiangyun Zhihui Technology Co., Ltd.
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Foshan Meng Fa Jing Shui Technology Co Ltd
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Priority to CN201810528728.XA priority Critical patent/CN108751576A/en
Publication of CN108751576A publication Critical patent/CN108751576A/en
Withdrawn legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/122—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/34—Treatment of water, waste water, or sewage with mechanical oscillations
    • C02F1/36—Treatment of water, waste water, or sewage with mechanical oscillations ultrasonic vibrations
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/442—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by nanofiltration
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4672—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4676—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electroreduction
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F2001/007—Processes including a sedimentation step
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00—Specific treatment goals
    • C02F2303/04—Disinfection
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/02—Aerobic processes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/28—Anaerobic digestion processes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/28—Anaerobic digestion processes
    • C02F3/286—Anaerobic digestion processes including two or more steps
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used

Abstract

The invention discloses a kind of complete system and methods of cosmetic-producing wastewater processing, including thickness grille well, capping anaerobism regulating reservoir, ultrasonic electric Fenton electric adsorption device, anaerobic pond, sedimentation basin, ultrasonic film biofilter, vortex nanofiltration device and the clear water reserviors being sequentially communicated.The complete system and method for the processing fully has studied the characteristics of harmful substances such as organic matter, heavy metal contained in cosmetics waste water, the advantages of having given full play to various processing modes, realizes the circulating treatment procedure of continuous-stable.The structure also has hydraulic detention time short, and sludge yield is few, and chroma removal rate is high, the energy conservation and environmental protections such as operating cost is low, and floor space is small, and power consumption is low, the advantage of service life of equipment length.

Description

A kind of complete system and method for cosmetic-producing wastewater processing
Technical field
The present invention relates to field of environment protection more particularly to a kind of cosmetic-producing wastewater to handle complete system and method.
Background technology
With the development of China's economic, industrial water consumption increases, and so that limited water resource day is becoming tight, Chinese garbage loading embeading Field, waste incineration field, refuse transfer station, cosmetics, papermaking, metallurgy, printing and dyeing, pharmacy, leather, well-drilling waste water, oil refining, oil Work, fine chemistry industry, food processing brewing, coking, hardware cleaning, application, electroplating enterprise discharge make containing highly difficult industrial wastewater Water environment in China pollution aggravation；Finding new practical wastewater processing technology makes waste water energy minimizing, regeneration and recycling As the important channel of solution shortage of water resources.Traditional processing mode is generally by micro-filtration, ultrafiltration, nanofiltration reverse osmosis membrane skill Art, evaporator, burning, light electrolysis or low-voltage, the electrolysis of high current and biological treatment.These single treatment modes In the presence of wastewater treatment is not thorough, the processing equipment service life is low, of high cost the defects of, therefore be badly in need of seek it is a kind of efficiently, company The combined treatment process of the continuous stable a variety of processing modes of collection, so that processing of these sewage disposal systems in industrial wastewater It is popularized in work.
Invention content
The object of the invention is exactly to provide a kind of efficient, continuous-stable cosmetics life to make up the defect of prior art Produce wastewater treatment integrated system and method.
The present invention is achieved by the following technical solutions：
A kind of cosmetic-producing wastewater handles integrated system, including the thickness grille well that is sequentially communicated, capping anaerobism are adjusted Pond, ultrasonic electric Fenton electric adsorption device, anaerobic pond, sedimentation basin, ultrasonic film biofilter, vortex nanofiltration device and clear water reserviors；Institute It states integrated system lower end and is equipped with sludge concentration tank and filter press successively.
The ultrasonic electric Fenton electric adsorption device substitutes traditional electric flocculation flotation tank and first sedimentation basin, by high-frequency ultrasonic Dissolved iron (aluminium sheet) generates Galvanic interaction or plus high-pressure electro ultrafiltration generates electrochemical reaction, and ultraviolet light, electric energy are converted to Chemical energy carries out redox pretreatment to the object difficult to degrade in waste water.
The clear water reserviors are equipped with chlorination equipment, play the role of sterilizing and adjust processing water.
Ultrasonic electric Fenton electric adsorption device lower end dross sludge outlet is connected with sludge concentration tank entrance；The anaerobism Pond, sedimentation basin, the mixing reflux of ultrasonic film biofilter lower end；The ultrasound film biofilter lower end excess sludge outlet and sludge Concentration basin entrance is connected；The concentrated water outlet of vortex nanofiltration device lower end is connected with sludge concentration tank entrance.
The sludge concentration tank supernatant outlet is connected with capping anaerobism regulating reservoir；The filtrate (liquid of the filter press with plus Lid anaerobism regulating reservoir is connected.
A kind of cosmetic-producing wastewater processing method, includes the following steps：
(1) cosmetics waste water may block the coarseer suspension of water pump assembly and pipeline valve by the removal of thickness grille well Object carries out initial breakdown to wherein larger molecular organics into capping anaerobism regulating reservoir and water is adjusted, into ultrasonic electric After Fenton electric adsorption device carries out depth degradation flocculation for wherein highly difficult degradation of organic substances, upper layer dross sludge enters sludge Concentration basin, lower liquid enter anaerobic pond；
(2) it is hydrolyzed stage, fermentation stage, production acetic acid stage, methane phase four in the anaerobic bacteria in anaerobic pond A stage degradation process, supernatant liquid enter aerobic contact oxidation and leaching in sedimentation basin and set precipitation, and supernatant liquid enters ultrasonic film Biofilter is handled；
(3) liquid is promoted fully to be connect with biofilter microbial film by excusing from death immixture in ultrasonic film biofilter It touches, then supernatant liquid, leaching postpones after supernatant liquid enters the filtering of vortex nanofiltration device, and supernatant liquid, which enters, is equipped with chlorination equipment Clear water reserviors processing after qualified discharge；
(4) sludge of these device lower ends enters filter press press filtration into mud cake desiccation after entering sludge concentration tank concentration Outward transport is handled afterwards, and filtrate returns to capping anaerobism regulating reservoir.
It is an advantage of the invention that：
The present invention provides the complete system and methods of cosmetic-producing wastewater processing, and first choice is using thickness grille well to larger Particle suspensions carry out after tentatively removing, in conjunction with ultrasonic electric Fenton Electro Sorb, anaerobic degradation, aerobic contact oxidation, ultrasonic film A series of processing modes such as biofiltration, vortex nanofiltration are sequentially distributed combination, finally enter after clear water reserviors disinfect.It should Handle the spy that complete system and method fully has studied the harmful substances such as organic matter, heavy metal contained in cosmetics waste water Point, realizes the circulating treatment procedure of continuous-stable at the advantages of having given full play to various processing modes.The structure also has waterpower Residence time is short, and sludge yield is few, and chroma removal rate is high, and the energy conservation and environmental protections such as operating cost is low, and floor space is small, and power consumption is low are set Standby advantage with long service life, final outflow water water stabilization are kept under strict control area's new standard better than country.
Description of the drawings
Fig. 1 is present invention process flow chart.
Specific implementation mode
Integrated system is handled referring to a kind of cosmetic-producing wastewaters of Fig. 1, including the thickness grille well that is sequentially communicated, capping are detested Oxygen regulating reservoir, ultrasonic electric Fenton electric adsorption device, anaerobic pond, sedimentation basin, ultrasonic film biofilter, vortex nanofiltration device and clear water Pond；The integrated system lower end is equipped with sludge concentration tank and filter press successively.
The ultrasonic electric Fenton electric adsorption device substitutes traditional electric flocculation flotation tank and first sedimentation basin, by high-frequency ultrasonic Dissolved iron (aluminium sheet) generates Galvanic interaction or plus high-pressure electro ultrafiltration generates electrochemical reaction, and ultraviolet light, electric energy are converted to Chemical energy carries out redox pretreatment to the object difficult to degrade in waste water.
The clear water reserviors are equipped with chlorination equipment, play the role of sterilizing and adjust processing water.
Ultrasonic electric Fenton electric adsorption device lower end dross sludge outlet is connected with sludge concentration tank entrance；The anaerobism Pond, sedimentation basin, the mixing reflux of ultrasonic film biofilter lower end；The ultrasound film biofilter lower end excess sludge outlet and sludge Concentration basin entrance is connected；The concentrated water outlet of vortex nanofiltration device lower end is connected with sludge concentration tank entrance.
The sludge concentration tank supernatant outlet is connected with capping anaerobism regulating reservoir；The filtrate (liquid of the filter press with plus Lid anaerobism regulating reservoir is connected.
A kind of cosmetic-producing wastewater processing method, includes the following steps：
(1) cosmetics waste water may block the coarseer suspension of water pump assembly and pipeline valve by the removal of thickness grille well Object carries out initial breakdown to wherein larger molecular organics into capping anaerobism regulating reservoir and water is adjusted, into ultrasonic electric After Fenton electric adsorption device carries out depth degradation flocculation for wherein highly difficult degradation of organic substances, upper layer dross sludge enters sludge Concentration basin, lower liquid enter anaerobic pond；
(2) it is hydrolyzed stage, fermentation stage, production acetic acid stage, methane phase four in the anaerobic bacteria in anaerobic pond A stage degradation process, supernatant liquid enter aerobic contact oxidation and leaching in sedimentation basin and set precipitation, and supernatant liquid enters ultrasonic film Biofilter is handled；
(3) liquid is promoted fully to be connect with biofilter microbial film by excusing from death immixture in ultrasonic film biofilter It touches, then supernatant liquid, leaching postpones after supernatant liquid enters the filtering of vortex nanofiltration device, and supernatant liquid, which enters, is equipped with chlorination equipment Clear water reserviors processing after qualified discharge；
(4) sludge of these device lower ends enters filter press press filtration into mud cake desiccation after entering sludge concentration tank concentration Outward transport is handled afterwards, and filtrate returns to capping anaerobism regulating reservoir.

Claims (6)

1. a kind of cosmetic-producing wastewater handles integrated system, which is characterized in that including be sequentially communicated thickness grille well, capping Anaerobism regulating reservoir, ultrasonic electric Fenton electric adsorption device, anaerobic pond, sedimentation basin, ultrasonic film biofilter, vortex nanofiltration device and clear Pond；The integrated system lower end is equipped with sludge concentration tank and filter press successively.
2. a kind of cosmetic-producing wastewater according to claim 1 handles integrated system, which is characterized in that the ultrasonic electric Fenton electric adsorption device substitutes traditional electric flocculation flotation tank and first sedimentation basin, is generated by high-frequency ultrasonic dissolved iron (aluminium sheet) former Galvanic action or plus high-pressure electro ultrafiltration generate electrochemical reaction, ultraviolet light, electric energy are converted to chemical energy, to the difficulty in waste water Degradation product carries out redox pretreatment.
3. a kind of cosmetic-producing wastewater according to claim 1 handles integrated system, which is characterized in that the clear water reserviors Equipped with chlorination equipment, plays the role of sterilizing and adjust processing water.
4. a kind of cosmetic-producing wastewater according to claim 1 handles integrated system, which is characterized in that the ultrasonic electric Fenton electric adsorption device lower end dross sludge outlet is connected with sludge concentration tank entrance；The anaerobic pond, sedimentation basin, ultrasonic film life The mixing reflux of object filter tank lower end；The ultrasound film biofilter lower end excess sludge outlet is connected with sludge concentration tank entrance；Institute The concentrated water outlet of vortex nanofiltration device lower end is stated with sludge concentration tank entrance to be connected.
5. a kind of cosmetic-producing wastewater according to claim 1 handles integrated system, which is characterized in that the sludge is dense Contracting pond supernatant outlet is connected with capping anaerobism regulating reservoir；The filtrate (liquid of the filter press is connected with capping anaerobism regulating reservoir.
6. a kind of cosmetic-producing wastewater processing method, which is characterized in that include the following steps：
(1) cosmetics waste water may block the coarseer suspended matter of water pump assembly and pipeline valve by the removal of thickness grille well, Initial breakdown is carried out to wherein larger molecular organics into capping anaerobism regulating reservoir and water is adjusted, into ultrasonic electric Fenton After electric adsorption device carries out depth degradation flocculation for wherein highly difficult degradation of organic substances, upper layer dross sludge enters sludge condensation Pond, lower liquid enter anaerobic pond；
(2) it is hydrolyzed four stage, fermentation stage, production acetic acid stage, methane phase ranks in the anaerobic bacteria in anaerobic pond Section degradation process, supernatant liquid enter aerobic contact oxidation and leaching in sedimentation basin and set precipitation, and supernatant liquid enters ultrasonic film biology Filter tank is handled；
(3) liquid is promoted to be come into full contact with biofilter microbial film by excusing from death immixture in ultrasonic film biofilter, Then supernatant liquid, leaching postpone after supernatant liquid enters the filtering of vortex nanofiltration device, and supernatant liquid enters equipped with chlorination equipment Qualified discharge after clear water reserviors processing；
(4) sludge of these device lower ends enters filter press press filtration at outer after mud cake desiccation after entering sludge concentration tank concentration Fortune processing, filtrate return to capping anaerobism regulating reservoir.
CN201810528728.XA 2018-05-29 2018-05-29 A kind of complete system and method for cosmetic-producing wastewater processing Withdrawn CN108751576A (en)

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CN201810528728.XA CN108751576A (en) 2018-05-29 2018-05-29 A kind of complete system and method for cosmetic-producing wastewater processing

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Application Number Priority Date Filing Date Title
CN201810528728.XA CN108751576A (en) 2018-05-29 2018-05-29 A kind of complete system and method for cosmetic-producing wastewater processing

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109824172A (en) * 2019-03-25 2019-05-31 苏州希图环保科技有限公司 A kind of high concentrated acid alkali waste water combined treatment device and its technique
CN111847733A (en) * 2020-07-13 2020-10-30 久沛（上海）环保科技有限公司 Efficient treatment process for coating wastewater
CN112194290A (en) * 2020-06-30 2021-01-08 广州中科建禹环保有限公司 Physicochemical treatment system and method for cosmetic production waste liquid
CN114409204A (en) * 2022-02-17 2022-04-29 广州绿莱环保科技有限公司 Automatic wastewater treatment system and treatment method thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104529093A (en) * 2015-01-13 2015-04-22 樊利华 Garbage compression leachate comprehensive waste water treatment device and technological method
CN105417899A (en) * 2016-01-13 2016-03-23 樊利华 Ultrasonic electro-adsorption electro-Fenton and desalination and decoloration water treatment device and method

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104529093A (en) * 2015-01-13 2015-04-22 樊利华 Garbage compression leachate comprehensive waste water treatment device and technological method
CN105417899A (en) * 2016-01-13 2016-03-23 樊利华 Ultrasonic electro-adsorption electro-Fenton and desalination and decoloration water treatment device and method

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
曾郴林，刘情生主编: "《工业废水处理工程设计实例》", 31 October 2016, 中国环境出版社 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109824172A (en) * 2019-03-25 2019-05-31 苏州希图环保科技有限公司 A kind of high concentrated acid alkali waste water combined treatment device and its technique
CN112194290A (en) * 2020-06-30 2021-01-08 广州中科建禹环保有限公司 Physicochemical treatment system and method for cosmetic production waste liquid
CN111847733A (en) * 2020-07-13 2020-10-30 久沛（上海）环保科技有限公司 Efficient treatment process for coating wastewater
CN114409204A (en) * 2022-02-17 2022-04-29 广州绿莱环保科技有限公司 Automatic wastewater treatment system and treatment method thereof

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Address after: Room 934, floor 9, building 9, yard 16, Junying street, Shunyi District, Beijing

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Application publication date: 20181106