CN106673324A - Treatment method of sweet potato alcohol wastewater - Google Patents
Treatment method of sweet potato alcohol wastewater Download PDFInfo
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- CN106673324A CN106673324A CN201611255024.7A CN201611255024A CN106673324A CN 106673324 A CN106673324 A CN 106673324A CN 201611255024 A CN201611255024 A CN 201611255024A CN 106673324 A CN106673324 A CN 106673324A
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- waste water
- composite powder
- solid
- radix ipomoeae
- mnzn
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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
- 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
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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
- C02F2001/007—Processes including a sedimentation step
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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
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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
- 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
-
- 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
- C02F2103/36—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds
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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
-
- 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
-
- 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
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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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)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Removal Of Specific Substances (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The invention provides a treatment method of sweet potato alcohol wastewater. The treatment method comprises the following procedures of carrying out solid-liquid separation, reducing by CO2 pressurized manganese-zinc composite powder, carrying out anaerobic treatment, carrying out aerobic treatment, treating by a biological filter tower and the like; treated wastewater can stably reach emission standards and then is discharged.
Description
Technical field
The present invention relates to a kind of processing method of Radix Ipomoeae alcohol waste water.
Background technology
Radix Ipomoeae is to produce one of primary raw material of ethanol, and the organic waste water pollutant COD concentration that its production is produced is high, into
Divide complexity, intractability is big.If the waste water is not processed is directly discharged into environment, severe contamination will be caused to environment.Current sweet potato wine
The processing method of smart waste water is mainly biological treatment.Due to containing persistence organic pollutant in Radix Ipomoeae alcohol waste water（Containing benzene
Ring and（Or）Heterocycle Organic substance）, especially with fresh sweet potatoes be primary raw material when, the concentration of persistence organic pollutant is higher,
Thereby result in Biochemical method Radix Ipomoeae alcohol waste water and be difficult stably reaching standard discharge.The Radix Ipomoeae ethanol of exploitation energy stably reaching standard discharge gives up
The processing method of water has larger practical value.
The content of the invention
For the problem of current Radix Ipomoeae ethanol method of wastewater treatment, the purpose of the present invention is to find energy stably reaching standard discharge
The processing method of Radix Ipomoeae alcohol waste water, it is characterised in that Radix Ipomoeae alcohol waste water is carried out solid-liquor separation, the waste water isolated are entered
Regulating reservoir, the solid isolated make feedstuff.Radix Ipomoeae alcohol waste water after adjusted pond is adjusted sends into voltage-resistant reactor, will clean manganese
Zinc composite powder adds reactor, and is passed through industrial CO2Reacted, the granularity of MnZn composite powder is less than 180 mesh, and cleaning MnZn is multiple
The content for closing each metal in powder is not less than 5%（The MnZn composite powder that return is used is not limited）, every liter of waste water addition
MnZn composite powder 5g~30g, stirring reaction time are 1h~3h, and reaction temperature is 25 DEG C~60 DEG C, CO2Pressure be 0.1MPa
~0.6MPa.Reacted waste water carries out solid-liquor separation, the MnZn composite powder Returning reactor isolated.It is useless after solid-liquor separation
Water lime cream or other alkaline matters adjust its pH value to 7.0~8.5, subsequently into anaerobic reactor.Waste water is anti-in anaerobism
Device is answered to stop 24h~120h, anaerobism temperature is 25 DEG C~55 DEG C.Waste water after anaerobism is into the process of biology aerobic pond room temperature, good
Oxygen process time is 4h~12h.Waste water after Aerobic Process for Treatment enters sedimentation tank, and the sedimentation time is 1h~3h.Irregularly from precipitation
Extract sludge out to be filtered in pond, filter cake makees general disposition of solid waste, filtrate returns Aerobic Pond.The supernatant waste water of sedimentation tank
Multi-layer biological filter tower is sent to process.The filler of biological filtering tower combined working is activated carbon or porous ceramic grain, is 0.5m~1.0m per thickness degree, total thickness
Spend for 1m~3m.The dominant bacteria of biological filtering tower combined working is the rhodopseudomonas in photosynthetic bacteria（Rhodopseudomonas）.It is biological
The hydraulic load of filter tower is 50 m3/m2.d~150m3/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 the solid matter of Radix Ipomoeae alcohol waste water is more, into MnZn composite powder
Before reduction reactor, solid-liquor separation is carried out, it is to avoid the impact that solid matter is reduced to MnZn composite powder, be also beneficial to unreacted complete
MnZn composite powder recycling.After waste water enters MnZn composite powder reduction reactor, the larger molecular organicses in waste water are special
It is not persistence organic pollutant（Containing phenyl ring and（Or）The Organic substance of heterocycle etc.）The strong also of generation is reduced by MnZn composite powder
The effect of former free radical and destroy, be subsequent biochemical process create favorable conditions.It is passed through pressure CO2Purpose be to maintain MnZn multiple
Close powder and reduce suitable pH value（2.0~5.0）, the waste water lime cream or other alkaline matters after reduction adjusts its pH, with full
The requirement of the follow-up anaerobic and aerobic process of foot.The premenstrual waste water for stating process is in anaerobic processes, by the effect of microorganism, big to divide
Sub- Organic substance further becomes small organic molecule, is that more favorable condition is created in subsequent bio oxidation.By biological oxidation process,
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 life
Thing filter tower, in the presence of microorganism, particularly rhodopseudomonas, the pollutant such as further organics removal and nitrogen phosphorus, it is ensured that
Waste water stably reaching standard discharge after process.
Relative to existing method, the outstanding advantages of the present invention are reduced using MnZn composite powder, by the persistency in waste water
Pollutant are destroyed, and are that subsequent biological treatment creates favorable conditions, so as to ensure the waste water stably reaching standard discharge after processing；Relative to
Metal deoxidization used in other wastewater treatments, using CO2Replace now widely used sulphuric acid to make acidulant, do not introduce
SO4 2-Ion, eliminates generation H2The material base of S, so as to avoid H2The pollution of S, while it also avoid SO4 2-To anaerobism and
The inhibitory action of microorganism in aerobic process, greatly improves the efficiency of biological treatment；Boiler, fuel combustion are all had in Radix Ipomoeae Alcohol Plant
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 1：1m is processed daily3Radix Ipomoeae alcohol waste water（Composition： CODCr38500 mg/L、T-N42.2m/L、
SS28000mg/L, T-P4.5mg/L, colourity 750）, Jing solid-liquor separations, the reduction of MnZn composite powder（1h、40℃、CO2Pressure
0.6MPa, every liter of waste water add MnZn composite powder 15g）, anaerobism（PH8.5,72h, 25 DEG C~35 DEG C）, it is aerobic（4h）And biological filter
Tower（Porous ceramic grain packing layer gross thickness 1m, hydraulic load 50m3/m2.d）The COD of water outlet after processCrFor 49mg/L, T-
N7.0mg/L, T-P0.4mg/L, colourity 27.
Embodiment 2：5m is processed daily3Radix Ipomoeae alcohol waste water（Composition:CODCr40500 mg/L、T-N45.1m/L、
SS31500mg/L, T-P4.2mg/L, colourity 780）, Jing solid-liquor separations, the reduction of MnZn composite powder（2.5h、25℃、CO2Pressure
0.1MPa, every liter of waste water add MnZn composite powder 5g）, anaerobism（PH7.0,24h, 35 DEG C~55 DEG C）, it is aerobic（6h）And biological filter
Tower（Active carbon filler layer gross thickness 2m, hydraulic load 150m3/m2.d）The COD of water outlet after processCrFor 57mg/L, T-N7.6mg/
L, T-P0.4mg/L, colourity 30.
Claims (1)
1. a kind of processing method of Radix Ipomoeae alcohol waste water, it is characterised in that Radix Ipomoeae alcohol waste water is carried out into solid-liquor separation, is isolated
Waste water enter regulating reservoir, the solid isolated makees feedstuff, and the Radix Ipomoeae alcohol waste water after adjusted pond is adjusted sends into pressure reaction
Cleaning MnZn composite powder is added reactor, and is passed through industrial CO by device2Reacted, the granularity of MnZn composite powder is less than 180
Mesh, the content for cleaning each metal in MnZn composite powder are not less than 5%, and every liter of waste water adds MnZn composite powder 5g~30g,
The stirring reaction time is 1h~3h, and reaction temperature is 25 DEG C~60 DEG C, CO2Pressure be 0.1MPa~0.6MPa, it is reacted
Waste water carries out solid-liquor separation, the MnZn composite powder Returning reactor isolated, waste water lime cream after solid-liquor separation or other
Alkaline matter adjusts its pH value to 7.0~8.5, subsequently into anaerobic reactor, waste water anaerobic reactor stop 24h~
120h, anaerobism temperature are 25 DEG C~55 DEG C, and into the process of biology aerobic pond room temperature, the Aerobic Process for Treatment time is 4h to the waste water after anaerobism
~12h, the waste water after Aerobic Process for Treatment enter sedimentation tank, and the sedimentation time is 1h~3h, irregularly extracts sludge out from sedimentation tank and enters
Row is filtered, and filter cake makees general disposition of solid waste, and filtrate returns Aerobic Pond, and the supernatant waste water of sedimentation tank send multi-layer biological filter tower
Process, the filler of biological filtering tower combined working is activated carbon or porous ceramic grain, filler gross thickness is 1m~3m, the dominant bacteria of biological filtering tower combined working is
Rhodopseudomonas in photosynthetic bacteria, the hydraulic load of biological filtering tower combined working is 50 m3/m2.d~150m3/m2.d, biological filtering tower combined working goes out
Water qualified discharge or reuse.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611255024.7A CN106673324A (en) | 2016-12-30 | 2016-12-30 | Treatment method of sweet potato alcohol wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611255024.7A CN106673324A (en) | 2016-12-30 | 2016-12-30 | Treatment method of sweet potato alcohol wastewater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106673324A true CN106673324A (en) | 2017-05-17 |
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ID=58872312
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611255024.7A Pending CN106673324A (en) | 2016-12-30 | 2016-12-30 | Treatment method of sweet potato alcohol wastewater |
Country Status (1)
| Country | Link |
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| CN (1) | CN106673324A (en) |
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 CN201611255024.7A patent/CN106673324A/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 (5)
| Title |
|---|
| 宋志伟 等: "《水污染控制工程》", 31 July 2013, 中国矿业大学出版社 * |
| 张修正: "《化工厂电气手册》", 31 December 1994, 化学工业出版社 * |
| 施悦 等: "《环境氧化还原处理技术原理与应用》", 31 August 2013, 哈尔滨工业大学出版社 * |
| 湖南省爱国卫生运动委员会办公室 等: "CO2中和", 《爱国卫生运动工作手册》 * |
| 郑西来: "《地下水污染控制》", 31 July 2009, 华中科技大学出版社 * |
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Application publication date: 20170517 |