CN206828249U - Integrated sewage water puies forward mark processing equipment - Google Patents
Integrated sewage water puies forward mark processing equipment Download PDFInfo
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- CN206828249U CN206828249U CN201720389495.0U CN201720389495U CN206828249U CN 206828249 U CN206828249 U CN 206828249U CN 201720389495 U CN201720389495 U CN 201720389495U CN 206828249 U CN206828249 U CN 206828249U
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- pond
- oxidant
- reducing agent
- processing equipment
- integrated sewage
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Abstract
The utility model discloses integrated sewage water to put forward mark processing equipment, including second pond, it is connected with automatic dosing apparatus, ozone devices, filter plant on the drainpipe of the second pond in turn, the controller that the automatic dosing apparatus includes the medicament pond being connected on second pond drainpipe and detector, is connected with the medicament pond and detector signal.The utility model has the advantage of：In drainpipe, medicament and sewage are quickly sufficiently mixed the direct dosing of automatic dosing apparatus；Device structure is simple, and floor space is few, and the cycle is short for transformation, cost is low；Can 24 hours left unguardeds, modularization operation, effectively solve the problems, such as COD, ammonia nitrogen, SS (suspension), heavy metals exceeding standard.
Description
Technical field
Sewage treatment area is the utility model is related to, more particularly to adapt to the equipment and technology that sewage carries mark and transformed.
Background technology
Conventional sewage disposal COD requirements are in below 100mg/L, typically in 80mg/L or so；After new environmental requirement proposes,
COD requirements are below 50mg/L, or even 30mg/L or so.Now to realize and carry mark, most direct idea is increase equipment, but due to
Increase equipment needs to use more construction areas, and many factories all without reserved unnecessary land used, can cause to put forward mark limitation
And risk.Different sewage will carry mark for different, have plenty of COD and carry mark, have plenty of ammonia nitrogen fluctuation, some heavy metals surpass
Mark, three problems are required for solving in time.
COD in sewage is exceeded, and some are that suspension is exceeded caused, that is, undissolved COD；Has plenty of dissolubility
COD it is exceeded caused by, handle deliquescent COD generally uses medicament and handled, but blindly a large amount of dosings, medicament dissolution
To a certain amount of saturation, repeat that to add any problems, its basic reason to be preferably PH Long-term Fluctuations, and
The demand of actual dilatation was not considered during plant design originally, equivalent to high load with small power；Mark is carried plus new environmental requirement, from
Original 80mg/L or so, even following close to 30mg/L till now, original design parameter equipment operation does not substantially reach
Target requirement is proposed, COD is solved the problems, such as with the method for simple biochemical anaerobism, preferable effect can not be reached.
Utility model content
The purpose of this utility model is that providing integrated sewage water puies forward mark processing equipment, and mark is carried to solve sewage disposal device
Transformation land used deficiency, cost is high, it is ineffective to carry mark, the problems such as limitation and risk be present.
The utility model adopts the following technical scheme that in order to achieve the above object：
Integrated sewage water carries mark processing equipment, including second pond, is connected with turn on the drainpipe of the second pond automatic
Medicine machine, ozone devices, filter plant, the automatic dosing apparatus include being connected to medicament pond on second pond drainpipe and
Detector, the controller being connected with the medicament pond and detector signal.
Further, the medicament pond includes oxidant pond and reducing agent pond.
Further, the oxidant pond is connected to by oxidant chemical feed pipe on the drainpipe of the second pond,
The oxidant chemical feed pipe is provided with oxidant measuring pump, the oxidant measuring pump and the controller
Signal connects, and the oxidant pond is connected with oxidant proof dry powder feeding machine.
Further, the oxidant chemical feed pipe is tributary form between oxidant pond and oxidant measuring pump, including
First oxidant Zhi Liuguan and the second oxidant Zhi Liuguan, the first oxidant Zhi Liuguan entrance point are higher than the second oxidant
Zhi Liuguan entrance point.
Further, the reducing agent pond is connected to by reducing agent chemical feed pipe on the drainpipe of the second pond, described
Reducing agent chemical feed pipe is provided with reductant metering pump, and the reductant metering pump is connected with the controller signals, the reduction
Agent pond is connected with reducing agent proof dry powder feeding machine.
Further, the reducing agent chemical feed pipe is tributary form between reducing agent pond and reductant metering pump, including
First reducing agent Zhi Liuguan and the second reducing agent Zhi Liuguan, the first reducing agent Zhi Liuguan entrance point are higher than the second reducing agent
Zhi Liuguan entrance point.
Further, the detector is located at the downstream in medicament pond.
Further, the detector is connected by signal amplifier with the controller.
Further, the detector can be conductivity meter, PH meters, quick phosphate analytical instrument, COD tables, ammonia nitrogen table,
One or more of streaming current analyzer, chlorine residue table.
Further, the filter plant is laminated filter, the laminated filter include laminated filter unit, two
Triple valve, water inlet, delivery port, sewage draining exit, pressure valve, water inlet pipe, outlet pipe, blow-off pipe and pressing device, described two three
Port valve connects laminated filter unit, water inlet pipe and blow-off pipe respectively, and outlet pipe is connected with laminated filter unit, and pressure valve is arranged on
On water inlet pipe, laminated filter unit outer layer is provided with pressing device, and laminated filter unit is internally provided with lamination, the lamination
Groove is carved with both sides, and lamination is laminated on lining in the filtering for the inwall for being arranged at filter element.
Further, the laminated filter includes being no less than 2 laminated filter units.
Further, lamination is nylon lamination or PP laminations.
The utility model has the advantage of：In outlet pipe, medicament and sewage quickly fill the direct dosing of automatic dosing apparatus
Divide mixing；Device structure is simple, and floor space is few, and the cycle is short for transformation, cost is low；Can 24 hours left unguardeds, modularization operation,
Effectively solve the problems, such as COD, ammonia nitrogen, SS (suspension), heavy metals exceeding standard.
Brief description of the drawings
Accompanying drawing described herein is used for providing further understanding to of the present utility model, forms the part of the application,
Do not form to improper restriction of the present utility model, in the accompanying drawings：
Fig. 1 is the utility model structure diagram；
Fig. 2 is laminated filter structural representation；
Fig. 3 is laminated filter overlooking the structure diagram.
Embodiment
The utility model is described in detail below in conjunction with accompanying drawing and specific embodiment, is shown herein with of the present utility model
Meaning property embodiment and explanation are used for explaining the utility model, but are not intended as to restriction of the present utility model.
As Figure 1-3, integrated sewage water carries mark processing equipment, including second pond, on the drainpipe 1 of the second pond according to
Secondary to be connected with automatic dosing apparatus, ozone devices 13, filter plant, the automatic dosing apparatus includes being connected to second pond draining
Medicament pond and detector 12 on pipe 1, the controller 10 being connected with the medicament pond and the signal of detector 12.
The medicament pond includes oxidant pond 3 and reducing agent pond 7.The oxidant pond 3 is connected by oxidant chemical feed pipe 27
It is connected on the drainpipe 1 of the second pond, the oxidant chemical feed pipe 27 is provided with oxidant measuring pump 2, the reducing agent pond 7
It is connected to by reducing agent chemical feed pipe 28 on the drainpipe 1 of the second pond, the reducing agent chemical feed pipe 28 is provided with reducing agent
Measuring pump 6, the oxidant measuring pump 2 and reductant metering pump 6 are connected with the signal of controller 10, the oxidant dosing
Pipe is tributary form between oxidant pond 3 and oxidant measuring pump 2, including the first oxidant Zhi Liuguan 4 and the second oxidant
Zhi Liuguan 5, the first oxidant Zhi Liuguan 4 entrance point are higher than the second oxidant Zhi Liuguan 5 entrance point；In oxidant pond
Different height of water level drug concentrations may be different, and oxidant measuring pump can extract the medicine of different water levels by different Zhi Liuguan
Agent, the drug concentration in addition drainpipe 1 is set to keep uniform, beneficial to sewage disposal；The reducing agent chemical feed pipe 28 is in reduction pond 7
It is tributary form between reductant metering pump 6, including the first reducing agent Zhi Liuguan 8 and the second reducing agent Zhi Liuguan 9, described
One reducing agent Zhi Liuguan 8 entrance point is higher than the second reducing agent Zhi Liuguan 9 entrance point, different heights of water level in reducing agent pond 7
Drug concentration may be different, and reductant metering pump 6 can extract the medicament of different water levels by different Zhi Liuguan, make addition draining
Drug concentration in pipe 1 keeps uniform, beneficial to sewage disposal；The oxidant pond 3 and reducing agent pond 7 are respectively connected with respective dry
Powder feeding machine.The detector 12 is located at the downstream in medicament pond.The detector 12 passes through signal amplifier and the controller
10 connections.The detector 12 can be conductivity meter, PH meters, quick phosphate analytical instrument, COD tables, ammonia nitrogen table, streaming current
One or more of analyzer, chlorine residue table.The selection of detector 12 determines by the dosing species of user, such as：Ammonification, detection
Conductivity meter can be selected in instrument 12 or quick phosphate analytical instrument can be selected in PH meters, the hydrochlorate that phosphorates, and neutralizes and PH meters can be selected, coordinate phosphorus
Hydrochlorate processing is then needed using COD tables, ammonia nitrogen table, and coagulation then uses streaming current analyzer, and chlorination then needs to configure chlorine residue table etc..
The filter plant 26 is laminated filter, and the laminated filter includes 2 laminated filter units 14, two three
Port valve 15, in addition to water inlet 16, delivery port 17, sewage draining exit 18, pressure valve 19, water inlet pipe 21, outlet pipe 22, the and of blow-off pipe 23
Pressing device 24, the two-position three-way valve 15 connect laminated filter unit 14, water inlet pipe 2 and blow-off pipe 23, outlet pipe 22 respectively
Connected with laminated filter unit 14, pressure valve 19 is arranged on water inlet pipe 21, and the outer layer of laminated filter unit 14 is provided with compression
Device 24, laminated filter unit 14 are internally provided with lamination 20, and groove is carved with the both sides of lamination 20, and lamination 20 is laminated on setting
In on the filtering liner 25 of the inwall of filter element 14.Lamination 20 is nylon lamination or PP laminations.
As for necessary parts such as appropriate pipeline valves, those skilled in the art can according to the content of this disclosure
Set on demand, here is omitted.
The utility model service condition is as follows：
First, before carrying out sewage disposal using the utility model, lab scale first is carried out in laboratory, to confirm using effect and use
Amount, method are as follows：
1st, 3 wastewater samples, each sample 100ml are measured；
2nd,, need to containing depending on raw water such as 1000ppm, 2000ppm, 3000ppm respectively toward COD inorganic agents are added in 3 samples
Amount carries out appropriate dosage or decreasing amount adjustment；Stirring 10 minutes or so, allows medicament fully to react；
3rd, detect water-quality COD and can obtain test data.
2nd, apply on the spot
After obtaining test data, in data input controller 10, concentration setting value is generated after recorder record, then
Appropriate medicament is put into stir in medicament pond using proof dry powder feeding machine and fully dissolved, sewage emits from second pond, together
When controller 10 send the measuring pump in signal driving medicament pond, medicament is injected in drainpipe 1, medicament about can in drainpipe 1
Stop 0.5h to react with sewage, the detector 12 for being arranged on downstream is flowed through with the reacted sewage of medicament, concentration is detected instrument
The electric signal proportional with concentration is input to adjuster in controller compared with setting value, obtained by 12 detections, detector 12
Deviation signal is carried out ratio, integral operation by deviation signal, adjuster in technological requirement, and its operation result signal is conveyed to frequency conversion
Device, the motor speed that frequency converter changes measuring pump change, and change injection Liquid traditional Chinese medicine dosage, make the drug concentration in sewage
Control is in optimum range.
While medicament is injected in sewage, the ozone equipment 13 in downstream produces ozone and is also aerated in drainpipe 1, makes smelly
Oxygen oxidized portion COD, while remove the stink of water body, sterilization, kill the bacteriums such as Escherichia coli, caused suspension, in addition water
Molecule colloidal sol particulate condenses because charge neutrality makes colloidal solid de- steady.The ammonia nitrogen COD of non-solubility is possible to be free in water
Particle, foundry loam, colloidal objects green alga biological living etc. are attached to, complexing that they are disposably flocculated, which is united, is deposited in water body, small
Alumen ustum becomes big alumen ustum, then is precisely got rid of with laminated filter 26, and the sewage of outflow can be with stably reaching standard.
The course of work of the filter sewage of laminated filter 26 is：The sewage handled by medicament and ozone is logical from water inlet 16
Cross water inlet pipe 21 and enter device, open two-position three-way valve 15, sewage enters laminated filter unit 14, and lamination 20 passes through spring and stream
Body pressure compresses, and pressure difference is bigger, and thrust is stronger.Sewage flows to the inner edge of lamination 20 by outer rim by groove, after in-depth filtration
Discharged from outlet pipe 22 by delivery port 17.
The technical scheme provided above the utility model embodiment is described in detail, used herein specifically
Individual example is set forth to the principle and embodiment of the utility model embodiment, and the explanation of above example is only applicable to help
Assistant solves the principle of the utility model embodiment；Meanwhile for those of ordinary skill in the art, implement according to the utility model
Example, the there will be changes in embodiment and application, in summary, this specification content should not be construed as
To limitation of the present utility model.
Claims (10)
1. integrated sewage water puies forward mark processing equipment, it is characterised in that including second pond, connects successively on the drainpipe of the second pond
Automatic dosing apparatus, ozone devices, filter plant are connected to, the automatic dosing apparatus includes being connected on second pond drainpipe
Medicament pond and detector, the controller being connected with the medicament pond and detector signal.
2. integrated sewage water puies forward mark processing equipment according to claim 1, it is characterised in that the medicament pond includes oxidant
Pond and reducing agent pond.
3. integrated sewage water puies forward mark processing equipment according to claim 2, it is characterised in that the oxidant pond passes through oxidation
Agent chemical feed pipe is connected on the drainpipe of the second pond, and the oxidant chemical feed pipe is provided with oxidant measuring pump, the oxygen
Agent measuring pump is connected with the controller signals, and the oxidant pond is connected with oxidant proof dry powder feeding machine.
4. integrated sewage water puies forward mark processing equipment according to claim 3, it is characterised in that the oxidant chemical feed pipe is in oxygen
It is tributary form between agent pond and oxidant measuring pump, including the first oxidant Zhi Liuguan and the second oxidant Zhi Liuguan, institute
The entrance point for stating the first oxidant Zhi Liuguan is higher than the second oxidant Zhi Liuguan entrance point.
5. mark processing equipment is carried according to any integrated sewage waters of claim 2-4, it is characterised in that the reducing agent pond leads to
Reducing agent chemical feed pipe to be crossed to be connected on the drainpipe of the second pond, the reducing agent chemical feed pipe is provided with reductant metering pump,
The reductant metering pump is connected with the controller signals, and the reducing agent pond is connected with reducing agent proof dry powder feeding machine.
6. integrated sewage water puies forward mark processing equipment according to claim 5, it is characterised in that the reducing agent chemical feed pipe is also
It is tributary form between former agent pond and reductant metering pump, including the first reducing agent Zhi Liuguan and the second reducing agent Zhi Liuguan, institute
The entrance point for stating the first reducing agent Zhi Liuguan is higher than the second reducing agent Zhi Liuguan entrance point.
7. integrated sewage water puies forward mark processing equipment according to claim 1, it is characterised in that the detector is located at medicament pond
Downstream, the detector is connected by signal amplifier with the controller.
8. mark processing equipment is carried according to any integrated sewage water of claim 1 or 7, it is characterised in that the detector can
By be conductivity meter, in terms of PH, one in quick phosphate analytical instrument, COD tables, ammonia nitrogen table, streaming current analyzer, chlorine residue table
It is or multiple.
9. integrated sewage water puies forward mark processing equipment according to claim 1, it is characterised in that the filter plant is lamination mistake
Filter, the laminated filter include laminated filter unit, two-position three-way valve, water inlet, delivery port, sewage draining exit, pressure valve, entered
Water pipe, outlet pipe, blow-off pipe and pressing device, the two-position three-way valve connect laminated filter unit, water inlet pipe and blowdown respectively
Pipe, outlet pipe are connected with laminated filter unit, and pressure valve is arranged on water inlet pipe, and laminated filter unit outer layer is provided with compression
Device, laminated filter unit are internally provided with lamination, and groove is carved with the lamination both sides, and lamination, which is laminated on, is arranged at filter element
Inwall filtering in lining.
10. integrated sewage water puies forward mark processing equipment according to claim 9, it is characterised in that the laminated filter includes
No less than 2 laminated filter units, lamination are nylon lamination or PP laminations.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720389495.0U CN206828249U (en) | 2017-04-14 | 2017-04-14 | Integrated sewage water puies forward mark processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720389495.0U CN206828249U (en) | 2017-04-14 | 2017-04-14 | Integrated sewage water puies forward mark processing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206828249U true CN206828249U (en) | 2018-01-02 |
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ID=60767018
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720389495.0U Expired - Fee Related CN206828249U (en) | 2017-04-14 | 2017-04-14 | Integrated sewage water puies forward mark processing equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206828249U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109574315A (en) * | 2018-12-28 | 2019-04-05 | 东莞市三人行环境科技有限公司 | A kind of PID waste water treatment system |
| CN110981023A (en) * | 2019-12-25 | 2020-04-10 | 江苏达格水务有限公司 | Water treatment system and process for realizing continuous cleaning by utilizing pressure ozone |
-
2017
- 2017-04-14 CN CN201720389495.0U patent/CN206828249U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109574315A (en) * | 2018-12-28 | 2019-04-05 | 东莞市三人行环境科技有限公司 | A kind of PID waste water treatment system |
| CN110981023A (en) * | 2019-12-25 | 2020-04-10 | 江苏达格水务有限公司 | Water treatment system and process for realizing continuous cleaning by utilizing pressure ozone |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20180102 Termination date: 20200414 |