CN205442787U - Embedded high concentration sewage treatment system - Google Patents
Embedded high concentration sewage treatment system Download PDFInfo
- Publication number
- CN205442787U CN205442787U CN201521075523.9U CN201521075523U CN205442787U CN 205442787 U CN205442787 U CN 205442787U CN 201521075523 U CN201521075523 U CN 201521075523U CN 205442787 U CN205442787 U CN 205442787U
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- Prior art keywords
- district
- anaerobic reaction
- reaction district
- highly effective
- aeration
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Abstract
The utility model relates to an embedded high concentration sewage treatment system comprises high - rate anaerobic reaction district, hydrolytic acidification district and aeration biochemical region, its characterized in that: aeration biochemical region sets up in the inside in hydrolytic acidification district, is equipped with the MBR membrane module in the aeration biochemical region, the hydrolytic acidification district sets up the inside in the high - rate anaerobic reaction district to it packs to be equipped with the suspension in hydrolytic acidification distinguishes, be equipped with annular baffle in the high - rate anaerobic reaction district to be provided with the filler in the baffle outside, and be equipped with the suspension in the baffle inboard and pack, be equipped with the dive mixer in high - rate anaerobic reaction district bottom. This device is with high - rate anaerobic reaction district, hydrolytic acidification district and the integrated as an organic wholeization pond of aeration biochemical region to the convenience is made in the mill in a complete set, easy transportation, and occupation of land province, the energy consumption is low, and the method of operation is nimble, is particularly suitable for high concentration sewage treatment device small -size, the dispersion processing, reaches industry high concentration organic sewage similar with it and handles.
Description
Technical field
This utility model relates to sewage disposal device, particularly relates to a kind of embedded high-concentration sewage treatment system.
Background technology
More existing integrated equipment for sewage treatments, not only complex process, long processing period, inconvenient operation, anaerobic pond and biochemistry pool separately being built, facility floor space is big, builds and operating cost remains high, it is unfavorable for popularizing, unaccommodated high-concentration sewage treatment facility, and energy consumption is high.So needing the high-concentration sewage that a kind of construction cost is low, treatment effect is high, energy consumption is low, operating cost is low, be suitable for dispersion disposes to process integration apparatus.
Utility model content
The purpose of this utility model is to provide a kind of embedded high-concentration sewage treatment system, this device is by highly effective anaerobic reaction district, hydrolysis acidification district and becoming one pond, aeration biochemical district, and it is convenient in the complete manufacture of factory, easily transport, taking up an area and save, energy consumption is low, and the method for operation is flexible, it is particularly suitable for small-sized, the high-concentration sewage processing equipment of dispersion disposal, and industry high-concentration organic sewage similar therewith processes.
This utility model solves the technical scheme is that this utility model of its technical problem and is made up of highly effective anaerobic reaction district, hydrolysis acidification district and aeration biochemical district；It is characterized in that: described aeration biochemical district is arranged on the inside in hydrolysis acidification district, is provided with MBR membrane module in aeration biochemical district；Described hydrolysis acidification district is arranged on the inside in highly effective anaerobic reaction district, and is provided with floating stuffing in hydrolysis acidification district；It is provided with the dividing plate of annular in described highly effective anaerobic reaction district, and outside dividing plate, is provided with filler, and inside dividing plate, be provided with floating stuffing, bottom highly effective anaerobic reaction district, be provided with diving mixer.
The top in described highly effective anaerobic reaction district is provided with three phase separator, and three phase separator is connected with water sealed tank by pipeline.
It is provided with taper bucket bottom described aeration biochemical district, and above bucket and the lower section of MBR membrane module is provided with aeration tube, aeration tube is connected with aerator by pipeline.
This utility model runs operation principle: first high-concentration sewage removes thick solid suspension in sewage by grid, to ensure the properly functioning of subsequent treatment facility, sewage quality, water yield fluctuation that regulating reservoir is discharged due to project are bigger, stop the regular hour so sewage uneven to water quality, the water yield is introduced in regulating reservoir, make waste water be sufficiently mixed in pond, with ensure subsequent treatment structures uniformly, stable operation.Sewage is drawn into water pipe by elevator pump, by entering highly effective anaerobic reaction district after water inlet cloth tank water distribution, it is provided with floating stuffing in highly effective anaerobic reaction district and hydrolysis acidification district, porous suspended filler is that microorganism provides carrier, macromolecular substances can be converted into small-molecule substance by microorganism, and circulus is converted into chain structure, further increases the BOD/COD ratio of waste water, add the biodegradability of waste water, create conditions for follow-up aerobic treatment.It is provided with diving mixer bottom highly effective anaerobic reaction district.Aerator is connected with the aeration tube bottom aeration biochemical district by pipeline, a part of Organic substance in sewage is used for synthesizing new cell under conditions of aerobic by the microorganism in biomembrane, another part Organic substance being carried out catabolism to obtain the energy needed for cell synthesis, its end product is CO2And H2The stable materials such as O.The aerobic metabolism of microorganism is in all working the dissolved organic matter in sewage and non-solubility Organic substance, and metabolite is harmless stable material.Reflux pump back hydrolysis acidification region sewage enters highly effective anaerobic reaction district.After the biochemical treatment of aeration biochemical district, taper bucket it is provided with bottom aeration biochemical district, and above bucket and the lower section of MBR membrane module is provided with aeration tube, aeration tube is connected with aerator by pipeline, water outlet is by water outlet pumped, dirt is discharged by discharge pipeline, and a part refluxes, and a part processes as excess sludge.Clean device and clean MBR membrane module.
This utility model is compared with prior art, have such advantages as and beneficial effect: this device is by highly effective anaerobic reaction district, hydrolysis acidification district and becoming one pond, aeration biochemical district, take full advantage of functional areas volume size, meet technological requirement, save space, this device is convenient in the complete manufacture of factory, easily transports；A whole set of integrated body equipment can imbed underground, can move, not take up an area surface area；Using contact oxidation method degree of purification high, porous suspended filler improves treatment effect, and denitrogenation dephosphorizing clearance is high, and whole system mud generation amount is low；Automaticity is high, and energy consumption is low, convenient management, it is not necessary to personal management；The noise produced is low, and abnormal flavour is few, little to the environmental effect of surrounding；It is particularly suitable for small-sized, the high-concentration sewage processing equipment of dispersion disposal, and industry high-concentration organic sewage similar therewith processes.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
Fig. 2 is top view of the present utility model.
In above figure: 1, water inlet pipe, 2, water inlet cloth tank, 3, highly effective anaerobic reaction district, 4, three phase separator, 5, water sealed tank, 6, hydrolysis acidification district, 7, device is cleaned, 8, go out water pump, 9, aeration biochemical district, 10, filler, 11, dividing plate, 12, diving mixer, 13, reflux pump, 14, aerator, 15, discharge pipeline, 16, aeration tube, 17, MBR membrane module, 18, floating stuffing.
Detailed description of the invention
Below in conjunction with embodiment, the utility model is described in further detail, but embodiment of the present utility model is not limited to this.
Embodiment: as shown in Figure 1 and Figure 2, this utility model is made up of highly effective anaerobic reaction district (3), hydrolysis acidification district (6) and aeration biochemical district (9)；It is characterized in that: described aeration biochemical district (9) is arranged on the inside of hydrolysis acidification district (6), is provided with MBR membrane module (17) in aeration biochemical district (9)；Described hydrolysis acidification district (6) is arranged on the inside of highly effective anaerobic reaction district (3), and is provided with floating stuffing (18) in hydrolysis acidification district (6)；The dividing plate (11) of annular it is provided with in described highly effective anaerobic reaction district (3), and dividing plate (11) outside is provided with filler (10), and it is provided with floating stuffing (18) in dividing plate (11) inner side, it is provided with diving mixer (12) in highly effective anaerobic reaction district (3) bottom.
The top of described highly effective anaerobic reaction district (3) is provided with three phase separator (4), and three phase separator (4) is connected with water sealed tank (5) by pipeline.
Described aeration biochemical district (9) bottom is provided with taper bucket, and above bucket and the lower section of MBR membrane module (17) is provided with aeration tube (16), aeration tube (16) is connected with aerator (14) by pipeline.
During this utility model operation work: first high-concentration sewage removes thick solid suspension in sewage by grid, to ensure the properly functioning of subsequent treatment facility, sewage quality, water yield fluctuation that regulating reservoir is discharged due to project are bigger, stop the regular hour so sewage uneven to water quality, the water yield is introduced in regulating reservoir, make waste water be sufficiently mixed in pond, with ensure subsequent treatment structures uniformly, stable operation.Sewage is drawn into water pipe (1) by elevator pump, by entering highly effective anaerobic reaction district (3) after water inlet cloth tank (2) water distribution, it is provided with floating stuffing (18) in highly effective anaerobic reaction district (3) and hydrolysis acidification district (6), porous suspended filler (18) is that microorganism provides carrier, macromolecular substances can be converted into small-molecule substance by microorganism, circulus is converted into chain structure, further increase the BOD/COD ratio of waste water, add the biodegradability of waste water, create conditions for follow-up aerobic treatment.It is provided with diving mixer (12) in highly effective anaerobic reaction district (3) bottom.Aerator (14) is connected by the aeration tube (16) of pipeline with aeration biochemical district (9) bottom, a part of Organic substance in sewage is used for synthesizing new cell under conditions of aerobic by the microorganism in biomembrane, another part Organic substance being carried out catabolism to obtain the energy needed for cell synthesis, its end product is CO2And H2The stable materials such as O.The aerobic metabolism of microorganism is in all working the dissolved organic matter in sewage and non-solubility Organic substance, and metabolite is harmless stable material.Reflux pump (13) back hydrolysis acidification region (6) sewage enters highly effective anaerobic reaction district (3).After aeration biochemical district (9) biochemical treatment, bottom, aeration biochemical district (9) is provided with taper bucket, and above bucket and the lower section of MBR membrane module (17) is provided with aeration tube (16), aeration tube (16) is connected with aerator (14) by pipeline, water outlet is extracted out by going out water pump (8), dirt is discharged by discharge pipeline (15), and a part refluxes, and a part processes as excess sludge.Clean device (7) and clean MBR membrane module (17).
As it has been described above, this utility model just can be realized well.
Claims (3)
1. an embedded high-concentration sewage treatment system, is made up of highly effective anaerobic reaction district (3), hydrolysis acidification district (6) and aeration biochemical district (9)；It is characterized in that: described aeration biochemical district (9) is arranged on the inside of hydrolysis acidification district (6), is provided with MBR membrane module (17) in aeration biochemical district (9)；Described hydrolysis acidification district (6) is arranged on the inside of highly effective anaerobic reaction district (3), and is provided with floating stuffing (18) in hydrolysis acidification district (6)；The dividing plate (11) of annular it is provided with in described highly effective anaerobic reaction district (3), and dividing plate (11) outside is provided with filler (10), and it is provided with floating stuffing (18) in dividing plate (11) inner side, it is provided with diving mixer (12) in highly effective anaerobic reaction district (3) bottom.
The embedded high-concentration sewage treatment system of one the most according to claim 1, it is characterised in that: the top of described highly effective anaerobic reaction district (3) is provided with three phase separator (4), and three phase separator (4) is connected with water sealed tank (5) by pipeline.
The embedded high-concentration sewage treatment system of one the most according to claim 1, it is characterized in that: described aeration biochemical district (9) bottom is provided with taper bucket, and above bucket and the lower section of MBR membrane module (17) is provided with aeration tube (16), aeration tube (16) is connected with aerator (14) by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521075523.9U CN205442787U (en) | 2015-12-22 | 2015-12-22 | Embedded high concentration sewage treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521075523.9U CN205442787U (en) | 2015-12-22 | 2015-12-22 | Embedded high concentration sewage treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205442787U true CN205442787U (en) | 2016-08-10 |
Family
ID=56585118
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521075523.9U Expired - Fee Related CN205442787U (en) | 2015-12-22 | 2015-12-22 | Embedded high concentration sewage treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205442787U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105417701A (en) * | 2015-12-22 | 2016-03-23 | 成都绿源新创环保科技有限公司 | Embedded high-concentration sewage treatment system |
-
2015
- 2015-12-22 CN CN201521075523.9U patent/CN205442787U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105417701A (en) * | 2015-12-22 | 2016-03-23 | 成都绿源新创环保科技有限公司 | Embedded high-concentration sewage treatment system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160810 Termination date: 20161222 |