CN205556393U - Sesame oil steep and waste water's processing apparatus of cooking - Google Patents
Sesame oil steep and waste water's processing apparatus of cooking Download PDFInfo
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- CN205556393U CN205556393U CN201620234961.3U CN201620234961U CN205556393U CN 205556393 U CN205556393 U CN 205556393U CN 201620234961 U CN201620234961 U CN 201620234961U CN 205556393 U CN205556393 U CN 205556393U
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Abstract
The utility model discloses a sesame oil steep and waste water's processing apparatus of cooking, pond, oxygen deficiency pond, contact oxidation tank are included according to the grid groove of preface intercommunication, equalizing basin, little electrolytic oxidation ware, aeration oxidation pond, neutralization pond, flocculation basin, air supporting pond, UASB anaerobic reactor, MBBR pond, are just sunk, two ponds, decoloration reaction tank and secondary clarifier are sunk, the grid groove with be provided with cylinder grid blowdown machine between the equalizing basin, the sewage process get into behind the cylinder grid blowdown machine the equalizing basin, the equalizing basin with be provided with the elevator pump between little electrolytic oxidation ware, little electrolytic oxidation utensil has the blender, the blender is connected with quantitative acid feeder. The utility model discloses each item index is up to standard after ensureing waste water treatment.
Description
Technical field
This utility model relates to technical field of waste water processing, the brewed processing means producing waste water with steaming and decocting of a kind of Semen Arecae.
Background technology
Semen Arecae waste water is mainly derived from the production waste water that Semen Arecae is brewed and produces in digestion process.
The leading indicator data result producing waste water is as follows:
1、CODCr: 8811 ~ 16840mg/l, average is 13200mg/l, totally 16 monitorings；
2、BOD5: 2017 ~ 3528 mg/l, average is 2876mg/l, totally 4 monitorings；
3, pH value: 4.3 ~ 4.8, average is 4.5, totally 16 monitorings；
4, float: 470 ~ 587 mg/l, average is 526 mg/l, totally 4 monitorings；
5, ammonia nitrogen: 103 ~ 112 mg/l, average is 108mg/l, totally 4 monitorings.
Data above shows, this project waste water is acidity, and biochemical index BOD/COD maintains that ammonia nitrogen index in about 0.22, and waste water is higher, and float is more, belongs to high concentration, difficult organic wastewater.
This organic wastewater can cause destruction greatly to environment after being discharged in environment, and does not has a kind of for the brewed processing means producing waste water with steaming and decocting of Semen Arecae at present.
Utility model content
This utility model is solved the technical problem that to be to provide a kind of Semen Arecae brewed and the processing means of steaming and decocting production waste water, thus solves the problem in above-mentioned background technology.
This utility model is solved the technical problem that and is realized by the following technical solutions:
The brewed processing means producing waste water with steaming and decocting of a kind of Semen Arecae, including the frame trough sequentially connected, regulating reservoir, light electrolysis catalytic oxidizer, aeration oxidation pool, neutralization pond, flocculation basin, flotation tank, UASB anaerobic reactor, MBBR pond, preliminary sedimentation tank, anoxic pond, contact-oxidation pool, second pond, decolorizing reaction tank and final deposition pool, cylinder grid blowdown machine it is provided with between described frame trough and described regulating reservoir, sewage enters described regulating reservoir after described cylinder grid blowdown machine, it is provided with elevator pump between described regulating reservoir and described light electrolysis catalytic oxidizer, described light electrolysis catalytic oxidizer has blender, described blender connects quantitative acid dosing device；The connection one of described flotation tank is in order to discharge the sludge concentration tank of scum silica frost, and described sludge concentration tank is connected with filter press；Described preliminary sedimentation tank, second pond and final deposition pool all utilize dredge pump to be connected to described sludge concentration tank, and described preliminary sedimentation tank has the tieback pipeline to described UASB anaerobic reactor, and described second pond has the tieback pipeline to described anoxic pond.
Light electrolysis catalytic oxidizer have employed FCM-III micro electrolysis tech, and FCM-III ferrum carbon integration micro-electrolysis material is immersed in waste water when carrying out light electrolysis, due to the difference in Electrode Potential between ferrum and carbon, can form numerous miniature galvanic cell in waste water.These trickle batteries are that the carbon that current potential is high does negative electrode using the low ferrum of current potential as anode, under conditions of catalytic elements M exists, electrochemical oxidation-reduction reaction occur in waste water aqueous solution.The result of reaction is poisonous, long-chain and cyclic heteroatomic Organic substance obtains electronics, there is the degradation reaction such as open loop, chain rupture, toxic organic compound functional group is destroyed, Ecotoxicology disappears, long-chain bio-refractory Organic substance chain rupture is converted into the small organic molecule being prone to biochemical degradation, ring-type and heterocycle Organic substance open loop is converted into the micromolecular compound being prone to biochemical treatment, and the iron ion that ferrum is become bivalence or trivalent by corrosion simultaneously enters solution.Owing to iron ion has coagulation, it with pollutant in the different electricity of microgranule with faint negative charge attracting, form stable flocculate and occur coprecipitated and remove.Micro electrolysis tech is to process high concentration, a kind of ideal technology of difficult biochemical organic wastewater at present, the common effect based on electrochemistry, oxidoreduction and flocculation sediment of its operation principle, this method has applied widely, high treating effect, with low cost, convenient operating maintenance, is not required to consume the advantages such as electric power resource.This technique, for the process of hard-degrading high concentrated waste water, can not only be greatly reduced COD, and be greatly improved the biodegradability of waste water.
In this utility model, MBBR pond, by adding a number of suspending carrier in reactor, is improved the Biomass in reactor and biological species, thus is improved the treatment effeciency of reactor.Owing to packing density is close to water, so aeration when, with water in being thoroughly mixed state, the environment of growth of microorganism is gas, liquid, solid three-phase.Carrier collision in water and shear action, make air bubble more tiny, add the utilization rate of oxygen.It addition, be respectively provided with different biological species inside and outside each carrier, some anaerobe of growth inside or double oxygen bacterium, outside bacteria preferably, the most each carrier is a microreactor, makes nitration reaction and anti-nitration reaction exist simultaneously, thus improves treatment effect.
In this utility model, as the preferred technical scheme of one, between described sludge concentration tank and described filter press, it is provided with screw pump.
In this utility model, as the preferred technical scheme of one, the filtrate (liquid of described filter press is connected to described regulating reservoir.
Owing to have employed above technical scheme, this utility model has the advantages that
This utility model passed through light electrolysis after 2 hours, in waste water, long-chain macromolecule organic compound such as has the unsaturated alkane of bio-toxicity, phenols and heterocyclic material by chain rupture, organic macromolecule changes into micromolecular compound, it is simple to subsequent cell microbial metabolism, improves microbial treatments efficiency；Removing oil removal and COD by waste water after light electrolysis in order to ensure maximum possible, this programme chooses air supporting as slag-liquid separation technique after pretreatment；Biochemical part uses the technique of " UASB+MBBR+ anoxia+aerobic " that waste water is carried out subsequent treatment, it is ensured that indices is up to standard.
Accompanying drawing explanation
Fig. 1 is this utility model equipment flowsheet schematic diagram.
Detailed description of the invention
For the technological means making this utility model realize, creation characteristic, reach purpose and be easy to understand with effect, below in conjunction with specific embodiment, this utility model is expanded on further.
nullSee Fig. 1，The brewed processing means producing waste water with steaming and decocting of a kind of Semen Arecae，Including the frame trough 1 sequentially connected、Regulating reservoir 2、Light electrolysis catalytic oxidizer 3、Aeration oxidation pool 4、Neutralization pond 5、Flocculation basin 6、Flotation tank 7、UASB anaerobic reactor 8、MBBR pond 9、Preliminary sedimentation tank 10、Anoxic pond 11、Contact-oxidation pool 12、Second pond 13、Decolorizing reaction tank 14 and final deposition pool 15，Cylinder grid blowdown machine 16 it is provided with between described frame trough 1 and described regulating reservoir，Sewage enters described regulating reservoir 2 after described cylinder grid blowdown machine 16，It is provided with elevator pump 17 between described regulating reservoir 2 and described light electrolysis catalytic oxidizer 3，Described light electrolysis catalytic oxidizer 3 has blender 18，Described blender 18 connects quantitative acid dosing device 19，Light electrolysis catalytic oxidizer 3 have employed FCM-III micro electrolysis tech，FCM-III ferrum carbon integration micro-electrolysis material is immersed in waste water when carrying out light electrolysis，Due to the difference in Electrode Potential between ferrum and carbon，Waste water can be formed numerous miniature galvanic cell.These trickle batteries are that the carbon that current potential is high does negative electrode using the low ferrum of current potential as anode, under conditions of catalytic elements M exists, electrochemical oxidation-reduction reaction occur in waste water aqueous solution.The result of reaction is poisonous, long-chain and cyclic heteroatomic Organic substance obtains electronics, there is the degradation reaction such as open loop, chain rupture, toxic organic compound functional group is destroyed, Ecotoxicology disappears, long-chain bio-refractory Organic substance chain rupture is converted into the small organic molecule being prone to biochemical degradation, ring-type and heterocycle Organic substance open loop is converted into the micromolecular compound being prone to biochemical treatment, and the iron ion that ferrum is become bivalence or trivalent by corrosion simultaneously enters solution.Owing to iron ion has coagulation, it with pollutant in the different electricity of microgranule with faint negative charge attracting, form stable flocculate and occur coprecipitated and remove.Micro electrolysis tech is to process high concentration, a kind of ideal technology of difficult biochemical organic wastewater at present, the common effect based on electrochemistry, oxidoreduction and flocculation sediment of its operation principle, this method has applied widely, high treating effect, with low cost, convenient operating maintenance, is not required to consume the advantages such as electric power resource.This technique, for the process of hard-degrading high concentrated waste water, can not only be greatly reduced COD, and be greatly improved the biodegradability of waste water；Described flotation tank 7 connects one in order to discharge the sludge concentration tank 20 of scum silica frost, and described sludge concentration tank 20 is connected with filter press 21；Described preliminary sedimentation tank 10, second pond 13 and final deposition pool 15 all utilize dredge pump to be connected to described sludge concentration tank 20, and described preliminary sedimentation tank 10 has the tieback pipeline to described UASB anaerobic reactor 8, and described second pond 13 has the tieback pipeline to described anoxic pond 11.MBBR pond, by adding a number of suspending carrier in reactor, is improved the Biomass in reactor and biological species, thus is improved the treatment effeciency of reactor.Owing to packing density is close to water, so aeration when, with water in being thoroughly mixed state, the environment of growth of microorganism is gas, liquid, solid three-phase.Carrier collision in water and shear action, make air bubble more tiny, add the utilization rate of oxygen.It addition, be respectively provided with different biological species inside and outside each carrier, some anaerobe of growth inside or double oxygen bacterium, outside bacteria preferably, the most each carrier is a microreactor, makes nitration reaction and anti-nitration reaction exist simultaneously, thus improves treatment effect.
In this utility model, being provided with screw pump 22 between described sludge concentration tank 20 and described filter press 21, the filtrate (liquid of described filter press 21 is connected to described regulating reservoir 2.
Of the present utility model ultimate principle and principal character and of the present utility model advantage have more than been shown and described.Skilled person will appreciate that of the industry; this utility model is not restricted to the described embodiments; described in above-described embodiment and description, principle of the present utility model is simply described; on the premise of without departing from this utility model spirit and scope; this utility model also has various changes and modifications, in the range of these changes and improvements both fall within claimed this utility model.This utility model claims scope and is defined by appending claims and equivalent thereof.
Claims (3)
1. the brewed processing means producing waste water with steaming and decocting of Semen Arecae, it is characterized in that: include the frame trough sequentially connected, regulating reservoir, light electrolysis catalytic oxidizer, aeration oxidation pool, neutralization pond, flocculation basin, flotation tank, UASB anaerobic reactor, MBBR pond, preliminary sedimentation tank, anoxic pond, contact-oxidation pool, second pond, decolorizing reaction tank and final deposition pool, cylinder grid blowdown machine it is provided with between described frame trough and described regulating reservoir, sewage enters described regulating reservoir after described cylinder grid blowdown machine, it is provided with elevator pump between described regulating reservoir and described light electrolysis catalytic oxidizer, described light electrolysis catalytic oxidizer has blender, described blender connects quantitative acid dosing device；The connection one of described flotation tank is in order to discharge the sludge concentration tank of scum silica frost, and described sludge concentration tank is connected with filter press；Described preliminary sedimentation tank, second pond and final deposition pool all utilize dredge pump to be connected to described sludge concentration tank, and described preliminary sedimentation tank has the tieback pipeline to described UASB anaerobic reactor, and described second pond has the tieback pipeline to described anoxic pond.
The brewed processing means producing waste water with steaming and decocting of a kind of Semen Arecae the most according to claim 1, it is characterised in that: it is provided with screw pump between described sludge concentration tank and described filter press.
The brewed processing means producing waste water with steaming and decocting of a kind of Semen Arecae the most according to claim 2, it is characterised in that: the filtrate (liquid of described filter press is connected to described regulating reservoir.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620234961.3U CN205556393U (en) | 2016-03-25 | 2016-03-25 | Sesame oil steep and waste water's processing apparatus of cooking |
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| CN201620234961.3U CN205556393U (en) | 2016-03-25 | 2016-03-25 | Sesame oil steep and waste water's processing apparatus of cooking |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107043195A (en) * | 2017-02-22 | 2017-08-15 | 长沙亿纳环保科技有限公司 | A kind of processing method of betel nut waste water |
| CN108101213A (en) * | 2016-11-25 | 2018-06-01 | 湖北水云涧环保工程有限公司 | Sewage combination biochemistry and sludge static state deposition separating treatment integrated apparatus |
-
2016
- 2016-03-25 CN CN201620234961.3U patent/CN205556393U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108101213A (en) * | 2016-11-25 | 2018-06-01 | 湖北水云涧环保工程有限公司 | Sewage combination biochemistry and sludge static state deposition separating treatment integrated apparatus |
| CN107043195A (en) * | 2017-02-22 | 2017-08-15 | 长沙亿纳环保科技有限公司 | A kind of processing method of betel nut waste water |
| CN107043195B (en) * | 2017-02-22 | 2020-04-24 | 湖南亿纳环保科技有限公司 | Treatment method of areca nut wastewater |
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Granted publication date: 20160907 |
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| CF01 | Termination of patent right due to non-payment of annual fee |