CN106673310A - Treatment method of chemical organic waste water - Google Patents
Treatment method of chemical organic waste water Download PDFInfo
- Publication number
- CN106673310A CN106673310A CN201611254338.5A CN201611254338A CN106673310A CN 106673310 A CN106673310 A CN 106673310A CN 201611254338 A CN201611254338 A CN 201611254338A CN 106673310 A CN106673310 A CN 106673310A
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- China
- Prior art keywords
- waste water
- sedimentation tank
- zinc powder
- reactor
- combined working
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Classifications
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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
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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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
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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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/70—Treatment of water, waste water, or sewage by reduction
- C02F1/705—Reduction by metals
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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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F2003/001—Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms
-
- 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
- C02F2003/001—Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms
- C02F2003/003—Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms using activated carbon or the like
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/32—Hydrocarbons, e.g. oil
- C02F2101/322—Volatile compounds, e.g. benzene
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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
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
- C02F2301/046—Recirculation with an external loop
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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
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
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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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
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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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
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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
- 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 relates to a treatment method of chemical organic waste water. The method comprises the steps of CO2 pressurizing zinc powder reduction, anaerobic treatment, aerobic treatment, biofilter treatment and the like. The treated waste water can be discharged stably to reach the standard.
Description
Technical field
The present invention relates to a kind of processing method of chemical industrial organic wastewater.
Background technology
Organic chemical industry is one of mainstay of the national economy industry, the organic waste water pollutant COD concentration that its production is produced
Height, complicated component particularly contains persistence organic pollutant(Containing phenyl ring and(Or)The Organic substance of heterocycle etc.)When, intractability
Greatly.If the waste water is not processed is directly discharged into environment, severe contamination will be caused to environment.At present containing persistence organic pollutant
The processing method of chemical industrial organic wastewater mainly first carries out advanced oxidation(Such as iron-carbon micro-electrolysis, metal powder reduction, Fenton methods
Deng)Pretreatment, then carries out a biological disposal upon.In advanced oxidation preprocessing process, sulphuric acid is generally needed to be added, caused at subsequent bio
Reason(Such as anaerobism, hydrolysis acidification)During produce H2S, produces more serious secondary pollution;Simultaneously because SO4 2-To microorganism
Growth has obvious inhibitory action, affects biological treatment effect, waste water to be difficult to stably reaching standard discharge.Exploitation secondary pollution is little, energy
The processing method of the chemical industrial organic wastewater of stably reaching standard discharge has larger practical value.
The content of the invention
For the problem of current chemical industrial organic wastewater processing method, the purpose of the present invention be find secondary pollution it is little, can be steady
Determine the processing method of the chemical industrial organic wastewater of qualified discharge, it is characterised in that pH value is more than into 5.0, and after adjusted pond is adjusted
Chemical industrial organic wastewater containing persistence organic pollutant sends into voltage-resistant reactor, and cleaning zinc powder is added into reactor, and is passed through work
Industry CO2Reacted, the granularity of zinc powder is less than 180 mesh, every liter of waste water adds zinc powder 5g~30g, the stirring reaction time be 1h~
3h, reaction temperature is 25 DEG C~60 DEG C, CO2Pressure be 0.1MPa~1.0MPa.Reacted waste water carries out solid-liquor separation, point
The zinc powder Returning reactor for separating out.Waste water lime cream or other alkaline matters after solid-liquor separation adjust its pH value to 6.8~
8.5,1h~3h is precipitated subsequently into sedimentation tank, irregularly to extract sludge out from sedimentation tank and filtered, filter cake makees dangerous solid
Waste treatment, filtrate returns sedimentation tank.The supernatant waste water of sedimentation tank send anaerobic reactor.Waste water is stopped in anaerobic reactor
24h~120h, anaerobism temperature is 25 DEG C~55 DEG C.Waste water after anaerobism is processed into biology aerobic pond room temperature, during Aerobic Process for Treatment
Between be 6h~16h.Waste water after Aerobic Process for Treatment enters sedimentation tank and precipitates 1h~3h, and irregularly extracting sludge out from sedimentation tank is carried out
Filter, filter cake makees dangerous disposition of solid waste, filtrate returns Aerobic Pond.The supernatant waste water of sedimentation tank is sent at multi-layer biological filter tower
Reason.The filler of biological filtering tower combined working is activated carbon or porous ceramic grain, is 1.0m~2.0m per thickness degree, and gross thickness is 2m~6m.It is biological
The dominant bacteria of filter tower is the rhodopseudomonas in photosynthetic bacteria(Rhodopseudomonas).The hydraulic load of biological filtering tower combined working is
30 m3/m2.d~90m3/m2.d.The standard water discharge discharge of biological filtering tower combined working or reuse.
The object of the present invention is achieved like this, and chemical industrial organic wastewater is entered after Zinc Powder Reduction device, big in waste water
Molecular organic, particularly persistence organic pollutant(Containing phenyl ring and(Or)The Organic substance of heterocycle etc.)Produced by zinc powder reduction
Strong reduction free radical effect and destroy, be subsequent biochemical process create favorable conditions.It is passed through pressure CO2Purpose be maintain
The suitable pH value of zinc powder reduction(2.0~5.0), the waste water lime cream or other alkaline matters after reduction adjust its pH value, with
Meet the requirement of follow-up anaerobic and aerobic process.The premenstrual waste water for stating process in anaerobic processes, by the effect of microorganism, greatly
Molecular organic further becomes small organic molecule, is that more favorable condition is created in subsequent bio oxidation.At biological oxidation
Reason, remaining most of Organic substances are removed, while going to denitrogenate the pollutant such as phosphorus.Waste water finally enters activated carbon or porous ceramic grain
Biological filtering tower combined working, in the presence of microorganism, particularly rhodopseudomonas, the pollutant such as further organics removal and nitrogen phosphorus are protected
Waste water stably reaching standard discharge after card process.
Relative to existing method(Iron-carbon micro-electrolysis, metal powder reduction, Fenton methods etc.), the outstanding advantages of the present invention are to adopt
Use CO2Replace now widely used sulphuric acid to make acidulant, do not introduce SO4 2-Ion, essentially eliminates generation H2The material base of S
(Part chemical industrial organic wastewater contains S), so as to significantly reduce H2The pollution of S, while it also avoid SO4 2-To anaerobic and aerobic mistake
The inhibitory action of microorganism in journey, greatly improves the efficiency of biological treatment;Chemical plant all has boiler, what fuel combustion was produced
CO2Waste gas can make full use of, and can not only reduce processing cost, and can reduce carbon emission;Waste water energy after process stably reaches
Mark discharge, with obvious economic benefit and environmental benefit.
Specific implementation method
Embodiment 1:1m is processed daily3Chemical industrial organic wastewater(Composition:pH6.7、CODCr11400mg/L、T-N52.5 mg/L、T-
P35.1mg/L, colourity 250), Jing zinc powder reductions(1h、40℃、CO2Pressure 0.6MPa, every liter of waste water add zinc powder 25g), anaerobism
(PH8.5,72h, 25 DEG C~35 DEG C), it is aerobic(12h)And biological filtering tower combined working(Porous ceramic grain packing layer gross thickness 4m, hydraulic load
35m3/m2.d)The COD of water outlet after processCrFor 55mg/L, T-N13.2mg/L, T-P0.5mg/L, colourity 14.
Embodiment 2:5m is processed daily3Synthesis pharmaceutical organic wastewater(Composition:pH5.7、CODCr6500 mg/L、T-N31.3
Mg/L, T-P23.2mg/L, colourity 300), Jing zinc powder reductions(3h、25℃、CO2Pressure 0.1MPa, every liter of waste water add zinc powder
5g), anaerobism(PH6.8,24h, 35 DEG C~55 DEG C), it is aerobic(6h)And biological filtering tower combined working(Active carbon filler layer gross thickness 2m, waterpower are born
Lotus 90m3/m2.d)The COD of water outlet after processCrFor 53mg/L, T-N10.1mg/L, T-P0.5mg/L, colourity 12.
Claims (1)
1. a kind of processing method of chemical industrial organic wastewater, it is characterised in that pH value is more than into 5.0, and after adjusted pond is adjusted
Chemical industrial organic wastewater containing persistence organic pollutant sends into voltage-resistant reactor, and cleaning zinc powder is added into reactor, and is passed through work
Industry CO2Reacted, the granularity of zinc powder is less than 180 mesh, every liter of waste water adds zinc powder 5g~30g, the stirring reaction time be 1h~
3h, reaction temperature is 25 DEG C~60 DEG C, CO2Pressure be 0.1MPa~1.0MPa, reacted waste water carries out solid-liquor separation, point
The zinc powder Returning reactor for separating out, the waste water lime cream or other alkaline matters after solid-liquor separation adjust its pH value to 6.8~
8.5,1h~3h is precipitated subsequently into sedimentation tank, irregularly to extract sludge out from sedimentation tank and filtered, filter cake makees dangerous solid
Waste treatment, filtrate returns sedimentation tank, and the supernatant of sedimentation tank send anaerobic reactor, waste water to stop 24h in anaerobic reactor
~120h, anaerobism temperature is 25 DEG C~55 DEG C, and the waste water after anaerobism is into the process of biology aerobic pond room temperature, Aerobic Process for Treatment time
6h~16h, the waste water after Aerobic Process for Treatment enters sedimentation tank and precipitates 1h~3h, and irregularly extracting sludge out from sedimentation tank was carried out
Filter, filter cake makees dangerous disposition of solid waste, and filtrate returns Aerobic Pond, and the supernatant waste water of sedimentation tank is sent at multi-layer biological filter tower
Reason, the filler of biological filtering tower combined working is activated carbon or porous ceramic grain, and filler gross thickness is 2m~6m, and the dominant bacteria of biological filtering tower combined working is light
The rhodopseudomonas in antibacterial are closed, the hydraulic load of biological filtering tower combined working is 30 m3/m2.d~90m3/m2.d, the water outlet of biological filtering tower combined working
Qualified discharge or reuse.
Priority Applications (1)
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CN201611254338.5A CN106673310A (en) | 2016-12-30 | 2016-12-30 | Treatment method of chemical organic waste water |
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CN201611254338.5A CN106673310A (en) | 2016-12-30 | 2016-12-30 | Treatment method of chemical organic waste water |
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CN201611254338.5A Pending CN106673310A (en) | 2016-12-30 | 2016-12-30 | Treatment method of chemical organic waste water |
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Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101665311A (en) * | 2009-09-24 | 2010-03-10 | 中南大学 | Catalysis and micro-electrolysis combined technology for high-concentration refractory organic wastewater |
-
2016
- 2016-12-30 CN CN201611254338.5A patent/CN106673310A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101665311A (en) * | 2009-09-24 | 2010-03-10 | 中南大学 | Catalysis and micro-electrolysis combined technology for high-concentration refractory organic wastewater |
Non-Patent Citations (7)
Title |
---|
宋志伟等: "《水污染控制工程》", 31 July 2013 * |
张修正: "《化工厂电气手册》", 31 December 1994 * |
徐根良: "《废水控制及治理工程》", 30 June 1999, 浙江大学出版社 * |
施悦等: "《环境氧化还原处理技术原理与应用》", 31 August 2013 * |
湖南省爱国卫生运动委员会办公室等: "《爱国卫生运动工作手册》", 31 July 1986, 湖南人民出版社 * |
蒋克彬: "《污水处理工艺与应用》", 31 March 2014, 中国石化出版社 * |
郑西来: "《地下水污染控制》", 31 July 2009 * |
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