CN201678563U - Device for purifying and treating high-concentration saline organic wastewater - Google Patents
Device for purifying and treating high-concentration saline organic wastewater Download PDFInfo
- Publication number
- CN201678563U CN201678563U CN201020168924XU CN201020168924U CN201678563U CN 201678563 U CN201678563 U CN 201678563U CN 201020168924X U CN201020168924X U CN 201020168924XU CN 201020168924 U CN201020168924 U CN 201020168924U CN 201678563 U CN201678563 U CN 201678563U
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- Prior art keywords
- tank
- organic wastewater
- pond
- high density
- mud
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
The utility model relates to a device for purifying and treating high-concentration saline organic wastewater, which has the characteristics of high purification effect, low treatment cost and easy popularization and application and adopts the technical scheme that the device for purifying and treating the high-concentration saline organic wastewater is sequentially provided with an adjusting facultative tank, a primary contact oxidation tank, a primary sedimentation tank, a facultative tank, a secondary contact oxidation tank and a secondary sedimentation tank along the sewage treatment process, wherein the adjusting facultative tank is provided with a grid, a tubular mixer and an inner mud-water separation tank; the primary contact oxidation tank is provided with combined packing and an aerator; the primary sedimentation tank is provided with an inclined solid-liquid separation tube; the facultative tank is provided with a stirrer; the secondary contact oxidation tank is provided with combined packing and an aerator; the secondary sedimentation tank is provided with an inclined solid-liquid separation tube; the altitude difference from high to low is maintained between every two adjacent tanks through a connecting water pipe; the primary sedimentation tank and the secondary sedimentation tank are respectively communicated with a sludge tank through pipelines with sludge pumps; and the sludge tank is connected with a filter press through a pipeline with a sludge pump. The tubular mixer is an integrated lengthened tubular mixer consisting of four tubular mixers connected in series.
Description
Technical field
The utility model relates to a kind of waste disposal plant, specifically is the device that purifies the high density salt-containing organic wastewater.
Background technology
The high density salt-containing organic wastewater is that a class total salinity (calculating with NaCl) is at least 1% waste water, its wastewater source mainly contains saliferous sanitary wastewater and trade effluent, wherein trade effluent mainly from the production of chemical reagent, print and dye, pickle and industries such as papermaking.High density salt-containing organic wastewater principal feature is the activity that its supersalinity suppresses microorganism, has the characteristics of difficult for biological degradation, and the sewage disposal difficulty is bigger, and working cost is higher.
2009 the 30th phases " Qingdao Technological University's journal " have been delivered three scholars' such as cold grade " experimental study of the high sea water salinity waste water of A/O art breading " literary composition, with A/O technology high salinity waste water are handled.This method need be tamed common micro-organisms, but microorganism is relatively poor for the adaptability that reaches high salinity, and the effect of disposing of sewage is not satisfactory.
The utility model content
The purpose of this utility model is at last disadvantages of background technology, design a kind of chemistry, physics, biological method three bonded high density salt-containing organic wastewater purifying processing devices, this device has the advantages that good purification, processing cost are low, be easy to apply.
The purpose of this utility model realizes by following technical solution: high density salt-containing organic wastewater purifying processing device, it is characterized in that this device is disposed with the band grid along the sewage disposal flow process, the adjusting oxygen compatibility pool in pond in tube mixer and the mud-water separation, the one-level contact-oxidation pool that has combined stuffing and aerator, the one-level settling tank of band solid-liquid separation inclined tube, the oxygen compatibility pool of band stirrer, the two-stage biological contact oxidation pond that has combined stuffing and aerator, the second-level settling pond of band solid-liquid separation inclined tube, keeping from high to low height fall by connecting water pipe between each adjacent pool, wherein one-level settling tank and second-level settling pond communicate with sludge sump by the pipeline that sludge pump is housed respectively, and sludge sump also links to each other with pressure filter by the pipeline that sludge pump is housed.
Said tube mixer is four king-size tube mixers of tube mixer series connection all-in-one-piece.
The pond is that a side has water-in in the said mud-water separation, and the interior pond of the container type mud-water separation at the mud extraction mouth of a river is arranged at the bottom.
Said combined stuffing is the string shape thing of plastic hoop and fibrous bundle combination.
Said aerator is formed by blower fan and airduct.
Said pressure filter is a plate-and-frame filter press.
The beneficial effects of the utility model are to handle the high density salt-containing organic wastewater effectively, and the saltiness that purifies the treating water of back discharging can be below 0.01%; And processing cost is low, is easy to apply.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Embodiment
The utility model is described in further detail below in conjunction with embodiment shown in the drawings:
As shown in the figure, waste water enters tube mixer 11 after removing big solid waste through grid 12, and sewage is carrying out mud-water separation through entering in the mud-water separation pond 13 after the mixing effect of tube mixer 11 by coagulating sedimentation.At grid 12 dosing coagulant PAC (polymerize aluminum chloride) to the sewage at position between the tube mixer, enter in the sewage at position between the pond to the mud-water separation at tube mixer and to add coagulant aids PAM (polyacrylamide).After the separation of pond, water outlet is (respectively by connecting water pipe A, B, C, D, E, F) flow through adjusting oxygen compatibility pool 1, one-level contact-oxidation pool 2, one-level settling tank 3, oxygen compatibility pool 4, two-stage biological contact oxidation pond 5, second-level settling pond 6 successively one by one in mud-water separation for waste water.Combined stuffing 21 and combined stuffing 52 are installed in aerator 22 and 51 oxygenation that two contact-oxidation pools 2 and 5 are all formed by blower fan and airduct respectively in the pond, agitator 41 also is set in the oxygen compatibility pool 4 stirs.Waste water carries out solid-liquid separation through behind a series of biochemical actions in settling tank 3 and 6, mud is sent into sludge sump 9 by sludge pump 7 in the settling tank, and part mud is back to regulates oxygen compatibility pool 1 and oxygen compatibility pool 4; Mud is after sludge pumping is gone into 10 processing of sheet frame pressure filter in the sludge sump 9, and mud cake is transported outward.
Principle of work of the present utility model is: after waste water is removed bigger solid waste through grid 12, water outlet enters tube mixer 11, dosing coagulant PAC in the outlet conduit before entering tube mixer 11, make the sufficient coagulation of sewage, water outlet through coagulation adds coagulant aids PAM before the pond 13 in flowing into mud-water separation, under the effect of PAM, the flco volume increases nature and sinks, the mud that deposits is sent into sludge sump 9 by pipeline by pump 8, supernatant liquor is excessive to regulating in the oxygen compatibility pool 1, is implemented in the purpose of carrying out mud-water separation in the mud-water separation in the pond 13.Pond 13 water outlets enter and regulate oxygen compatibility pool 1 in the mud-water separation, sewage is subjected to the dual function of regulating effect and microbiological deterioration at this, organism obtains the part degraded in the sewage, and improved the biodegradability of sewage, its water outlet enters the one-level contact-oxidation pool, and organism is attached on combined stuffing in the waste water microbial film absorption and oxygenolysis become CO
2And H
2O, 2 water outlets of one-level contact-oxidation pool enter settling tank 3 with the microbial film that comes off and carry out mud-water separation.Settling tank 3 adopts the higher settling tank that has solid-liquid separation inclined tube 31 of surface load, settling tank 3 water outlets enter oxygen compatibility pool 4, by microorganism in the oxygen compatibility pool 4 organism of difficult degradation is further degraded, continue to improve wastewater biodegradability, oxygen compatibility pool 4 water outlets enter two-stage biological contact oxidation pond 5, organism obtains continuing degraded by biomembranous effect in the waste water, finishes organic a large amount of removals.Settling tank 6 also adopts the higher settling tank that has solid-liquid separation inclined tube 61 of surface load, but settling tank 6 water outlet qualified discharges.
The available concrete of the construction in each pond is selected acclive plot, keeps reasonable drop according to adjacent two ponds of geographical environment, is convenient to gravity flow.The arrangement that should make the lift pump water lift that geographical conditions are not inconsistent.
The equal buyable of former device that the utility model is all; Wherein grid is by the production and sales of Zhucheng, Shandong market day Dong Beite environmental protection equipment company limited, tube mixer is the prosperous outstanding environmental engineering equipment of a Jiangsu Qidong City company limited production and selling, pond self-control in the mud-water separation, can make cylindric by stainless steel or glass reinforced plastic, the bucket shape mouth of spoil disposal water is established in the bottom, upper opening enlarges, filler is the combined stuffing of φ 150, good and the environment-friendly filler company limited production and selling by Yixing City, stirrer is by the safe profit of Yixing City environmental protection equipment company limited production and selling, inclined tube is the plastics inclined tube of φ 75mm, by the Zhejiang Yuhuan county prosperous water treating equipment of gold factory production and selling, plate-and-frame filter press is by Hangzhou dragon's pool pressure filter company limited production and selling.
Be example with the ability 20t that disposes of sewage day now, under the situation of surplus with due regard to, each pond reference volume is as follows: regulate oxygen compatibility pool 20m
3,, one-level contact-oxidation pool 10m
3, one-level settling tank 5m
3, oxygen compatibility pool 8m
3, two-stage biological contact oxidation pond 10m
3, second-level settling pond 5m
3,, sludge sump 10m
3, grid is selected the GSC300 type for use, and it is ZLS-32L that blower fan is selected model for use, and the air quantity of airduct is adjustable, and it is 50GW8-22 that sludge pump is selected model for use, and stirrer is selected the YJBG-0.75 type for use, and plate-and-frame filter press is selected the QJB0.85/8-260/3-740C type for use.
Still it should be noted that: all arrows are represented the sewage in the treating processes or the flow direction of mud among the figure.
Claims (6)
1. high density salt-containing organic wastewater purifying processing device, it is characterized in that being provided with band grid (12) successively along the sewage disposal flow process in this device, the adjusting oxygen compatibility pool (1) in pond (13) in tube mixer (11) and the mud-water separation, the one-level contact-oxidation pool (2) that has combined stuffing (21) and aerator (22), the one-level settling tank (3) of band solid-liquid separation inclined tube (31), the oxygen compatibility pool (4) of band stirrer (41), the two-stage biological contact oxidation pond (5) that has combined stuffing (52) and aerator (51), the second-level settling pond (6) of band solid-liquid separation inclined tube (61) is keeping from high to low height fall by connecting water pipe between each adjacent pool; One-level settling tank and second-level settling pond communicate with sludge sump (9) by the pipeline that sludge pump (7) is housed respectively in addition, and sludge sump also links to each other with pressure filter (10) by the pipeline that sludge pump is housed.
2. high density salt-containing organic wastewater purifying processing device according to claim 1 is characterized in that said tube mixer (11) is four king-size tube mixers of tube mixer series connection all-in-one-piece.
3. high density salt-containing organic wastewater purifying processing device according to claim 1 and 2 is characterized in that the pond is that a side has water-in in the said mud-water separation, and the interior pond of the container type mud-water separation at the mud extraction mouth of a river is arranged at the bottom.
4. high density salt-containing organic wastewater purifying processing device according to claim 3 is characterized in that said combined stuffing is the string shape thing of plastic hoop and fibrous bundle combination.
5. high density salt-containing organic wastewater purifying processing device according to claim 4 is characterized in that said aerator is by blower fan and airduct composition.
6. high density salt-containing organic wastewater purifying processing device according to claim 5 is characterized in that said pressure filter is a plate-and-frame filter press.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201020168924XU CN201678563U (en) | 2010-04-20 | 2010-04-20 | Device for purifying and treating high-concentration saline organic wastewater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201020168924XU CN201678563U (en) | 2010-04-20 | 2010-04-20 | Device for purifying and treating high-concentration saline organic wastewater |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201678563U true CN201678563U (en) | 2010-12-22 |
Family
ID=43343616
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201020168924XU Expired - Fee Related CN201678563U (en) | 2010-04-20 | 2010-04-20 | Device for purifying and treating high-concentration saline organic wastewater |
Country Status (1)
Country | Link |
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CN (1) | CN201678563U (en) |
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2010
- 2010-04-20 CN CN201020168924XU patent/CN201678563U/en not_active Expired - Fee Related
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101222 Termination date: 20120420 |