CN212293187U - Nitrogen and phosphorus removal device with advanced targeting function - Google Patents
Nitrogen and phosphorus removal device with advanced targeting function Download PDFInfo
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- CN212293187U CN212293187U CN202020248221.1U CN202020248221U CN212293187U CN 212293187 U CN212293187 U CN 212293187U CN 202020248221 U CN202020248221 U CN 202020248221U CN 212293187 U CN212293187 U CN 212293187U
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Abstract
The utility model discloses a denitrification and dephosphorization device with advanced upgrading function, which is formed by connecting a dense medium loading high-efficiency flocculation clarification tank, a denitrification deep bed V-shaped filter tank and a clean water tank in series in sequence; the heavy medium loading high-efficiency flocculation clarification tank comprises a heavy medium feeding system, a coagulant feeding system, a flocculant feeding system, a mixing unit, a flocculation unit, a clarification unit, a heavy medium sludge backflow system, a residual sludge discharge system and a heavy medium recovery system; by adopting the utility model, the problems that the filter head of the traditional aerobic nitrification biological filter is easy to block, the traditional upflow denitrification filter has high operating pressure and the ceramsite filter material layer is easy to harden due to fibrous impurities are solved, and the problem that the SS of the effluent of the denitrification filter is difficult to reach the standard lower than 5mg/L is broken through; the problem of drop-level oxygenation of the denitrification deep-bed V-shaped filter is solved, a carbon source is greatly saved, and the method has great popularization and application values for sewage upgrading.
Description
Technical Field
The utility model belongs to the technical field of water pollution control, concretely relates to target nitrogen and phosphorus removal device is carried to degree of depth.
Background
With the increasingly prominent water pollution problem in China, the improvement of the discharge standard of urban sewage treatment is a great trend. From the requirement of improving the quality of the current water environment, the effluent treated by a plurality of municipal sewage treatment plants is often discharged into a municipal river to become a water body of the river. The effluent of the existing sewage treatment plant in China has the discharge standard which is mainly referred to primary B or primary A in GB18918-2002 discharge Standard of pollutants for municipal wastewater treatment plants. However, for the class B or class A standard, the quality of water is only equivalent to the poor class V water of surface water. The water quality is discharged into the water body environment without self-purification capacity, so that the water body is not repaired but polluted, and the phenomenon of 'treating more and more dirty' occurs. The water pollution is increasingly aggravated, and the effluent of a sewage treatment plant is urgently required to reach the IV-class standard of the surface class.
At present, practice is carried out continuously all over the country, the requirements on total nitrogen, total phosphorus and the like of effluent of sewage plants are higher, and the existing IV-class water process is difficult to reach the full index standard practically; the prior treatment device and the prior treatment process mainly have the following problems: (1) traditionally, front-section fibrous substances of an upflow biological filter or PAC or PAM (polyaluminium chloride) remained in a pretreatment process are adhered to the surfaces of filter gaps of biological filter heads, biological membranes adhered to the surfaces block the filter gaps, forced backwashing of the filter heads is difficult to wash and remove, and then the filter heads are blocked, and finally the filter heads are paralyzed; (2) the SS of the effluent of a traditional upward flow aeration biological filter (including an aerobic biological filter and a denitrification biological filter) is generally 10-20 mg/L, and the SS of the effluent is difficult to reach below 5 mg/L; (3) the traditional chemical dephosphorization coagulating sedimentation tank has too low surface load, easily causes the problem of filter head blockage of the filter tank, and occupies larger area. At present, practice is carried out continuously all over the country, the requirements on total nitrogen, total phosphorus and the like of effluent of sewage plants are higher, and the existing IV-class water process is difficult to actually meet the IV-class water effluent index requirements. Therefore, a new technical solution needs to be developed to solve the above problems.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to solve the above-mentioned problem, provide a target nitrogen and phosphorus removal device is carried to the degree of depth to break through the difficult problem that meets at present. The specific contents are as follows: the utility model provides a nitrogen and phosphorus removal device of mark is carried to degree of depth which characterized in that: the device is formed by sequentially connecting a dense medium loading high-efficiency flocculation clarification tank, a denitrification deep bed V-shaped filter tank and a clean water tank in series; the heavy medium loading high-efficiency flocculation clarification tank comprises a heavy medium feeding system, a coagulant feeding system, a flocculant feeding system, a mixing unit, a flocculation unit, a clarification unit, a heavy medium sludge backflow system, a residual sludge discharge system and a heavy medium recovery system; the denitrification deep bed V-shaped filter is provided with water inlet and distribution holes, a surface sweeping and air-water backwashing system, a constant water level control system and an organic carbon source dosing system.
The heavy medium loading high-efficiency flocculation settling pond is a magnetic coagulation sedimentation pond or a sand loading high-efficiency sedimentation pond.
The mixing unit is provided with a mixing and stirring system; the flocculation unit is provided with a guide cylinder and a flocculation stirring system; the clarification unit is provided with a mud bucket, a mud scraper, a sludge concentration area, an inclined pipe and a clarification area.
The sludge return system is respectively connected with a sludge hopper at the lower part of the clarification unit and a guide cylinder of the flocculation unit.
The denitrification deep bed V-shaped filter body sequentially comprises a water inlet, a biological filter material reaction layer, a bearing layer, a collecting region, a water outlet pipe and a water outlet electric valve from top to bottom, wherein a short-handle filter head and a filter plate are arranged in the collecting region, and the bearing layer and the biological filter material reaction layer are arranged on the short-handle filter head.
The heavy medium adding system is a magnetic seed adding system or a sand seed adding system.
The dense medium recovery system is a magnetic seed recovery system or a sand seed recovery system.
The method is characterized in that: the thickness of the biological filter material layer of the V-shaped filter of the denitrification deep bed is 1.5-1.8 m, and the diameter of the biological filter material is 1.5-3.0 mm.
The agent added by the organic carbon source dosing system is preferably methanol or sodium acetate.
Drawings
FIG. 1 is a schematic structural diagram of a denitrification and dephosphorization apparatus with advanced upgrading function.
Wherein: feeding water 0; the system comprises a dense medium loading high-efficiency flocculation clarification tank 1, a dense medium adding system 1-1, a coagulant adding system 1-2, a flocculant adding system 1-3, a mixing unit 1-4 (a mixing and stirring system 1-4-1), a flocculation unit 1-5 (a guide cylinder 1-5-1 and a flocculation and stirring system 1-5-2), a clarification unit 1-6 (a mud bucket 1-6-1, a mud scraper 1-6-2, a sludge concentration zone 1-6-3, an inclined tube 1-6-4 and a clarification zone 1-6-5), a dense medium sludge reflux system 1-7, a residual sludge discharge system 1-8, a dense medium recovery system 1-9, a dense medium (magnetic seeds or sand seeds) 1-10 and stripped residual sludge 1-11; the denitrification deep bed V-shaped filter comprises a denitrification deep bed V-shaped filter 2, a water inlet and distribution hole 2-1, an organic carbon source dosing system 2-2, a biological filter material reaction layer 2-3, a support layer 2-4, a collection region 2-5, a water outlet pipe 2-6, a water outlet electric valve 2-7, a short handle filter head 2-8, a filter plate 2-9 and a constant water level control system 2-10; a clean water tank 3; and 4, yielding water after reaching the standard.
Detailed Description
The present invention will be further explained with reference to fig. 1:
a denitrification and dephosphorization device with advanced scaling is composed of a dense medium loading high-efficiency flocculation clarification tank 1, a denitrification deep bed V-shaped filter tank 2 and a clean water tank 3 which are connected in series in sequence; the heavy medium loading efficient flocculation clarification tank 1 comprises a heavy medium feeding system 1-1, a coagulant feeding system 1-2, a flocculant feeding system 1-3, a mixing unit 1-4, a flocculation unit 1-5, a clarification unit 1-6, a heavy medium sludge backflow system 1-7, an excess sludge discharge system 1-8 and a heavy medium recovery system 1-9; the denitrification deep bed V-shaped filter 2 is provided with a water inlet and distribution hole 2-1, a surface sweeping and air water backwashing system 2-10, a constant water level control system and an organic carbon source dosing system 2-2.
The heavy medium loading high-efficiency flocculation settling pond 1-9 is a magnetic coagulation sedimentation pond or a sand loading high-efficiency sedimentation pond.
The mixing unit 1-4 is provided with a mixing and stirring system 1-4-1; the flocculation unit 1-5 is provided with a guide cylinder 1-5-1 and a flocculation stirring system 1-5-2; the clarifying unit 1-6 is provided with a mud bucket 1-6-1, a mud scraper 1-6-2, a sludge concentration area 1-6-3, an inclined pipe 1-6-4 and a clarifying area 1-6-5.
The sludge return system 1-7 is respectively connected with a sludge hopper 1-6-1 at the lower part of the clarification unit and a guide cylinder 1-5-1 of the flocculation unit.
The denitrification deep bed V-shaped filter 2 is composed of a water inlet uniform distribution hole 2-1, a biological filter material reaction layer 2-3, a support layer 2-4, a collection region 2-5, a water outlet pipe 2-6 and a water outlet electric valve 2-7 from top to bottom in sequence, wherein a short handle filter head 2-8 and a filter plate 2-9 are arranged in the collection region 2-5, and the support layer 2-4 and the biological filter material reaction layer 2-3 are arranged on the support layer 2-4.
The heavy medium adding system 1-1 is a magnetic seed adding system or a sand seed adding system.
The medicament correspondingly added by the dense medium recovery system 1-9 is magnetic seeds or sand seeds.
The method is characterized in that: the biological filter material layer 2-3 of the V-shaped filter 2 of the denitrification deep bed has the thickness of 1.5-1.8 m and the diameter of 1.5-3.0 mm.
The agent added by the organic carbon source dosing system 2-1 is preferably methanol or sodium acetate.
The sewage treatment steps of the denitrification and dephosphorization device for deeply upgrading mainly comprise:
(1) heavy medium loading high-efficiency flocculation clarification tank 1: the secondary biochemical effluent 0 is firstly treated by a dense medium loading high-efficiency flocculation clarification tank 1 to remove suspended matters, TP and fibrous substances; the secondary biochemical effluent 0 is subjected to a mixing reaction in a mixing unit 1-4, is subjected to a flocculation reaction with heavy medium sludge refluxed by the sludge in a flocculation unit 1-5, is subjected to sludge-water separation in a clarification unit 1-6, has a surface load of 15-40 m/h, and enters a next-stage denitrification deep-bed V-shaped filter 2; the precipitated heavy medium sludge is partially refluxed through a heavy medium sludge reflux system 1-7, and the sludge reflux ratio is 1.5-6%; after the heavy medium and the sludge are stripped by the heavy medium sludge partially precipitated through the residual sludge discharge system 1-8 and the heavy medium recovery system 1-9, the recovered heavy medium 1-10 enters the mixing unit 1-5, and the stripped sludge 1-11 is discharged as residual sludge.
(2) A denitrification deep bed V-shaped filter 2: the organic carbon source dosing system 2-1 feeds an organic carbon source to be mixed with clarified effluent and then enters the denitrification deep bed V-shaped filter 2, and the opening degree of an electric water outlet valve 2-7 of a constant water level water inlet system is synchronously controlled by detecting a drop water level check of a clear water area on the surface of the filter, so that constant water level water inlet is ensured, drop water and drop water oxygenation are prevented, extra organic carbon source consumption is prevented, and the denitrification effect is reduced; the filtration speed is controlled to be 5-12 m/h, a large amount of denitrifying microbial membranes are attached to a biological filter material layer 2-3 in the denitrifying deep-bed V-shaped filter 2, deep denitrification is completed through denitrification (TN is less than 5mg/L), and meanwhile, the stability of suspended matters is realized through the filtration and interception functions of the filter material layer (SS is less than 5 mg/L); backwashing by adopting a method of 'air washing → air washing + water washing → water washing + surface sweeping', wherein the backwashing period is 6-12 h, wherein the air washing is 70-100m/h, and the water washing is 15-25 m/h; the effluent of the denitrification deep bed V-shaped filter 2 enters a clean water tank 3, the sewage part in the clean water tank 3 is used as the backwashing water of the denitrification deep bed V-shaped filter 2, and the rest part is used as the final standard-reaching discharge water 4 of the system.
Example 1:
the treatment flow of a sewage treatment plant in Jiangsu province is 150000m3And d, the prokaryotic core process is an oxidation ditch and secondary sedimentation tank process, and the pollutant indexes before the secondary treatment effluent enters the process are as follows: TN 18mg/L, SS 80mg/L, TP 3.5 mg/L; after the treatment by the process, the effluent quality indexes are as follows: TN 2.5mg/L, SS 2mg/L, and TP 0.1 mg/L.
Example 2:
the treatment flow of a municipal sewage treatment plant in Anhui province is 50000m3The original main process is 'AAO + secondary sedimentation tank' process, and the pollutant indexes before the secondary treatment effluent enters the process are as follows: TN 18mg/L, SS 30mg/L, TP 2.5 mg/L; after the treatment of the process device, the effluent quality indexes are as follows: TN 2.5mg/L, SS 3mg/L, and TP 0.1 mg/L.
Example 3:
the treatment flow of a sewage treatment plant in a certain chemical industry park of Suzhou of Jiangsu province is 15000m3The original main process is 'hydrolysis acidification + AAO + secondary sedimentation tank + ozone', and the pollutant indexes before the secondary treatment effluent enters the process are as follows: TN is 13mg/L, SS is 30mg/L, TP is 2.7 mg/L; after the treatment of the process device, the effluent quality indexes are as follows: TN 2.6mg/L, SS 3mg/L, and TP 0.1 mg/L.
The utility model solves the problem that the filter head of the traditional aerobic nitrification biological filter is easy to block due to fibrous impurities; the denitrification deep-bed V-shaped filter is adopted to replace the traditional upflow denitrification filter, so that the problems that the traditional upflow denitrification filter is high in operating pressure and easy to harden a ceramsite filter layer and the SS of the effluent of the denitrification filter is difficult to be lower than 5mg/L and reaches the standard are solved; by utilizing the denitrification constant water level technology, the problem of drop level oxygenation of the denitrification deep bed V-shaped filter is solved, and a carbon source is greatly saved; solves the problem of the traditional process of nitrogen and phosphorus removal, can carry out deep upgrading on the sewage containing high nitrate and has great popularization and application values for sewage upgrading.
The above-mentioned embodiments are only for illustrating the technical concept and features of the present invention, and the purpose thereof is to enable those skilled in the art to understand the contents of the present invention and to implement the present invention, which cannot limit the protection scope of the present invention. All equivalent changes and modifications made according to the spirit of the present invention should be covered by the protection scope of the present invention.
Claims (9)
1. The utility model provides a nitrogen and phosphorus removal device of mark is carried to degree of depth which characterized in that: the device is formed by sequentially connecting a dense medium loading high-efficiency flocculation clarification tank, a denitrification deep bed V-shaped filter tank and a clean water tank in series; the heavy medium loading high-efficiency flocculation clarification tank comprises a heavy medium feeding system, a coagulant feeding system, a flocculant feeding system, a mixing unit, a flocculation unit, a clarification unit, a heavy medium sludge backflow system, a residual sludge discharge system and a heavy medium recovery system; the denitrification deep bed V-shaped filter is provided with water inlet and distribution holes, a surface sweeping and air-water backwashing system, a constant water level control system and an organic carbon source dosing system.
2. The apparatus of claim 1, wherein the apparatus comprises: the heavy medium loading high-efficiency flocculation settling pond is a magnetic coagulation sedimentation pond or a sand loading high-efficiency sedimentation pond.
3. The apparatus of claim 1, wherein the apparatus comprises: the mixing unit is provided with a mixing and stirring system; the flocculation unit is provided with a guide cylinder and a flocculation stirring system; the clarification unit is provided with a mud bucket, a mud scraper, a sludge concentration area, an inclined pipe and a clarification area.
4. The apparatus of claim 1, wherein the apparatus comprises: the sludge return system is respectively connected with a sludge hopper at the lower part of the clarification unit and a guide cylinder of the flocculation unit.
5. The apparatus of claim 1, wherein the apparatus comprises: the denitrification deep bed V-shaped filter body sequentially comprises a water inlet, a biological filter material reaction layer, a bearing layer, a collecting region, a water outlet pipe and a water outlet electric valve from top to bottom, wherein a short-handle filter head and a filter plate are arranged in the collecting region, and the bearing layer and the biological filter material reaction layer are arranged on the short-handle filter head.
6. The apparatus of claim 1, wherein the apparatus comprises: the heavy medium adding system is a magnetic seed adding system or a sand seed adding system.
7. The apparatus of claim 1, wherein the apparatus comprises: the agent correspondingly added by the dense medium recovery system is a magnetic seed or a sand seed.
8. The apparatus of claim 1, wherein the apparatus comprises: the thickness of the biological filter material layer of the V-shaped filter of the denitrification deep bed is 1.5-1.8 m, and the diameter of the biological filter material is 1.5-3.0 mm.
9. The apparatus of claim 1, wherein the apparatus comprises: the added medicaments of the organic carbon source medicament adding system are methanol and sodium acetate.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111138047A (en) * | 2020-03-03 | 2020-05-12 | 安徽绿衡环保科技有限公司 | Denitrification and dephosphorization device with advanced standard improvement and treatment process thereof |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111138047A (en) * | 2020-03-03 | 2020-05-12 | 安徽绿衡环保科技有限公司 | Denitrification and dephosphorization device with advanced standard improvement and treatment process thereof |
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