CN106517692A - Coal tar wastewater treatment method - Google Patents
Coal tar wastewater treatment method Download PDFInfo
- Publication number
- CN106517692A CN106517692A CN201611259340.1A CN201611259340A CN106517692A CN 106517692 A CN106517692 A CN 106517692A CN 201611259340 A CN201611259340 A CN 201611259340A CN 106517692 A CN106517692 A CN 106517692A
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- CN
- China
- Prior art keywords
- waste water
- sedimentation tank
- composite powder
- coal tar
- reactor
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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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
- C02F1/34—Treatment of water, waste water, or sewage with mechanical oscillations
- C02F1/36—Treatment of water, waste water, or sewage with mechanical oscillations ultrasonic vibrations
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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
-
- 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
-
- 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
- C02F3/30—Aerobic and anaerobic processes
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention discloses a coal tar wastewater treatment method. The coal tar wastewater treatment method comprises the processes of CO2 pressurization, reducing, anaerobic, aerobic and biological filter-tower treatment conducted on manganese zinc composite powder under the effect of ultrasonic waves and the like, and stable and up-to-standard discharge of wastewater obtained after treatment can be achieved.
Description
Technical field
The present invention relates to a kind of processing method of the waste water of coal tar processing and storage process generation.
Background technology
Coal tar is one of important source material of production of chemicals, the Pollutants in Wastewater that its processing and storage process are produced
COD concentration is high, complicated component, and toxicity is big, and contains a large amount of persistence organic pollutants(Containing phenyl ring and(Or)Heterocycle etc. it is organic
Thing), intractability is big.If the waste water is not processed is directly discharged into environment, severe contamination will be caused to environment.Current Coal Tar Wastewater
Processing method mainly have burning method and biological treatment.Burning method processing cost is high, and produces atmospheric pollution.Biological treatment
Method needs first to carry out advanced oxidation(Such as iron-carbon micro-electrolysis, metal powder reduction, Fenton methods etc.)Pretreatment, then carries out a biological disposal upon.
In advanced oxidation preprocessing process, need to add sulphuric acid, cause subsequent biological treatment(Such as anaerobism, hydrolysis acidification)During produce
Raw H2S, produces more serious secondary pollution;Simultaneously because SO4 2-Growth to microorganism has obvious inhibitory action, affects life
Thing treatment effect, waste water are difficult to stably reaching standard discharge.Exploitation secondary pollution is little, processing cost is low, the coal of energy stably reaching standard discharge
The processing method of tar and waste water has larger practical value.
The content of the invention
For the problem of current Coal Tar Wastewater processing method, the purpose of the present invention is that searching secondary pollution is little, can stablize
The processing method of the Coal Tar Wastewater of qualified discharge, it is characterised in that the Coal Tar Wastewater after adjusted pond is adjusted is sent into pressure
Cleaning MnZn composite powder is added reactor, and is passed through industrial CO by reactor2Reacted.The granularity of MnZn composite powder is less than
180 mesh, in MnZn composite powder, the content of every kind of metal is not less than 5%(The MnZn composite powder that return is used is not limited), per liter
It is 20min~40min that waste water adds MnZn composite powder 10g~50g, mechanical agitation the response time under ul-trasonic irradiation,
Reaction temperature is 25 DEG C~60 DEG C, and the power of every cubic metre of waste water input ultrasound wave is 2kW~8kW, CO2Pressure be
0.1MPa~1.0MPa.Reacted waste water carries out solid-liquor separation, the MnZn composite powder Returning reactor isolated.Solid-liquor separation
Waste water lime cream or other alkaline matters afterwards adjusts its pH value to 6.8~8.5, precipitates 1h~3h subsequently into sedimentation tank,
Irregularly extract sludge out from sedimentation tank to be filtered, filter cake makees dangerous disposition of solid waste, filtrate returns sedimentation tank.Precipitation
The supernatant waste water in pond send anaerobic reactor.Waste water stops 24h~120h in anaerobic reactor, and anaerobism temperature is 25 DEG C~55
℃.Into the process of biology aerobic pond room temperature, the Aerobic Process for Treatment time is 8h~16h to waste water after anaerobism.Waste water after Aerobic Process for Treatment
1h~3h being precipitated into sedimentation tank, irregularly sludge being extracted out from sedimentation tank and is filtered, filter cake is made at dangerous solid waste
Put, filtrate returns Aerobic Pond.The supernatant waste water of sedimentation tank send multi-layer biological filter tower to process.The filler of biological filtering tower combined working be activated carbon or
Porous ceramic grain, is 1.0m~2.0m per thickness degree, and gross thickness is 2m~6m.During the dominant bacteria of biological filtering tower combined working is photosynthetic bacteria
Rhodopseudomonas(Rhodopseudomonas).The hydraulic load of biological filtering tower combined working is 30 m3/m2.d~90m3/m2.d.Biological filter
The standard water discharge discharge of tower or reuse.
The object of the present invention is achieved like this, after Coal Tar Wastewater enters MnZn composite powder reduction reactor, in waste water
Larger molecular organicses, particularly persistence organic pollutant(Containing phenyl ring and(Or)The Organic substance of heterocycle etc.)It is compound by MnZn
Powder reduces the effect of the strong reduction free radical for producing and destroys, and is that subsequent biochemical process creates favorable conditions.It is passed through pressure CO2's
Purpose is to maintain MnZn composite powder to reduce suitable pH value(2.0~5.0), it is input into the mass transfer mistake that ultrasound wave can be accelerated to react
Journey.Waste water lime cream or other alkaline matters after reduction adjusts its pH value, to meet wanting for follow-up anaerobic and aerobic process
Ask.In anaerobic processes, by the effect of microorganism, larger molecular organicses further become small molecule to the premenstrual waste water for stating process
Organic substance, is that more favorable condition is created in subsequent bio oxidation.By biological oxidation process, remaining most of Organic substances are gone
Remove, while the pollutant such as removing to denitrogenate.Waste water finally enters activated carbon or porous ceramic grain biological filtering tower combined working, in microorganism, particularly red
In the presence of pseudomonass, the pollutant such as further organics removal and nitrogen, it is ensured that the waste water stably reaching standard discharge after 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
(Coal Tar Wastewater contains a small amount of 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;Burner, fuel combustion are all had in coal tar processing factory
Burn the CO for producing2Waste gas can make full use of, and can not only reduce processing cost, and can reduce carbon emission;Waste water after process
Energy stably reaching standard discharge, with obvious economic benefit and environmental benefit.
Specific implementation method
Embodiment 1:Day processes 1 cubic metre of Coal Tar Wastewater(Volatile phenol 2400mg/L, COD15500mg/L, CN-25.5mg/L、
NH3-N57mg/L), the reduction of Jing MnZns composite powder(20min、40℃、CO2Pressure 0.6MPa, every liter of waste water add MnZn composite powder
40g, the ultrasonic power 4kW of every cubic metre of waste water input), anaerobism(PH8.5,72h, 25 DEG C~35 DEG C), it is aerobic(12h)And life
Thing filter tower(Porous ceramic grain packing layer gross thickness 4m, hydraulic load 35m3/m2.d)After process, the pollutant levels of water outlet are respectively
CODCr 66mg/L、NH3- N 7.6mg/L, volatile phenol 0.3mg/L, CN-0.12mg/L。
Embodiment 2:Day processes 3 cubic metres of Coal Tar Wastewaters(Volatile phenol 920mg/L, COD8700mg/L, CN-17mg/L、
NH3-N48mg/L), the reduction of Jing MnZns composite powder(40min、25℃、CO2Pressure 0.1MPa, every liter of waste water add MnZn composite powder
10g, the ultrasonic power 2kW of every cubic metre of waste water input), anaerobism(PH6.8,24h, 35 DEG C~55 DEG C), it is aerobic(8h)And life
Thing filter tower(Active carbon filler layer gross thickness 2m, hydraulic load 90m3/m2.d)After process, the pollutant levels of water outlet are respectively
CODCr 49mg/L、NH3- N 6.8mg/L, volatile phenol 0.3mg/L, CN-0.08mg/L。
Claims (1)
1. a kind of processing method of Coal Tar Wastewater, it is characterised in that will adjusted pond adjust after Coal Tar Wastewater send into it is resistance to
Cleaning MnZn composite powder is added reactor, and is passed through industrial CO by pressure reactor2Reacted, the granularity of MnZn composite powder is little
In 180 mesh, MnZn composite powder, the content of every kind of metal is not less than 5%, and every liter of waste water adds MnZn composite powder 10g~50g, machine
Tool is stirred and the response time under ul-trasonic irradiation is 20min~40min, and reaction temperature is 25 DEG C~60 DEG C, per cubic metre
The power of waste water input ultrasound wave is 2kW~8kW, CO2Pressure be 0.1MPa~1.0MPa, reacted waste water carries out liquid
Gu separating, the MnZn composite powder Returning reactor isolated, the waste water lime cream or other alkaline matters after solid-liquor separation is adjusted
Its pH value is saved to 6.8~8.5,1h~3h is precipitated subsequently into sedimentation tank, irregularly extract sludge out from sedimentation tank and filtered,
Filter cake makees dangerous disposition of solid waste, and filtrate returns sedimentation tank, and the supernatant waste water of sedimentation tank send anaerobic reactor, waste water detesting
24h~120h is stopped in oxygen reactor, and anaerobism temperature is 25 DEG C~55 DEG C, and the waste water after anaerobism enters biology aerobic Chi Changwenchu
Reason, Aerobic Process for Treatment time are 8h~16h, and the waste water after Aerobic Process for Treatment enters sedimentation tank and precipitates 1h~3h, irregularly from sedimentation tank
Middle extraction sludge is filtered, and filter cake makees dangerous disposition of solid waste, and filtrate returns Aerobic Pond, and the supernatant waste water of sedimentation tank send
The process of multi-layer biological filter tower, the filler of biological filtering tower combined working is activated carbon or porous ceramic grain, and filler gross thickness is 2m~6m, biological filtering tower combined working
Dominant bacteria be rhodopseudomonas in photosynthetic bacteria, 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.
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CN201611259340.1A CN106517692A (en) | 2016-12-30 | 2016-12-30 | Coal tar wastewater treatment method |
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CN201611259340.1A CN106517692A (en) | 2016-12-30 | 2016-12-30 | Coal tar wastewater treatment method |
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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 CN201611259340.1A patent/CN106517692A/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 (6)
Title |
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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 * |
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 等编: "《爱国卫生运动工作手册》", 31 July 1986 * |
郑西来: "《地下水污染控制》", 30 July 2009 * |
陈武 等主编: "《环境污染治理的电化学技术》", 31 March 2013 * |
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Application publication date: 20170322 |