CN206502710U - Percolate concentrates liquid advanced treatment device - Google Patents
Percolate concentrates liquid advanced treatment device Download PDFInfo
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- CN206502710U CN206502710U CN201620877908.5U CN201620877908U CN206502710U CN 206502710 U CN206502710 U CN 206502710U CN 201620877908 U CN201620877908 U CN 201620877908U CN 206502710 U CN206502710 U CN 206502710U
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Abstract
The utility model is related to a kind of percolate concentration liquid advanced treatment device, common RO films concentrated water pond is filtered including sodium, the delivery port that sodium filters common RO films concentrated water pond is connected to regulating reservoir by pipeline, the delivery port of regulating reservoir is connected to the electric Fenton of ultrasonic wave by pipeline, the delivery port of ultrasonic wave electricity Fenton is connected to security filter by pipeline, the delivery port of security filter is connected to one-level high pressure counter-infiltration by plunger pump, the counter-infiltration of one-level high pressure is provided with the outlet of first-stage reverse osmosis concentrated water and by-pass filtration water out, described by-pass filtration water out is connected to water producing tank by pipeline, described first-stage reverse osmosis concentrated water outlet is connected to two grades of high pressure counter-infiltrations by high-pressure pump, two grades of high pressure counter-infiltrations are provided with the outlet of two-pass reverse osmosis concentrated water and secondary filtration water out, described two-pass reverse osmosis concentrated water outlet is connected to vaporising device by pipeline, described secondary filtration water out is connected to water producing tank.The utility model realizes different processing, so that water reaches zero-emission.
Description
Technical field
The utility model is related to field of waste water treatment, espespecially a kind of percolate concentration liquid advanced treatment device.
Background technology
Landfill, or the mode burned either are taken in garbage disposal, and the processing of percolate is all technology therein
Problem.Percolate belongs to high concentration hard-degraded organic waste water, is lost with complicated component, pollutant concentration height, biological nutrition ratio
Weighing apparatus, colourity are high, the characteristics of stink is big, biodegradability is poor, therefore, the processing of percolate be faced with always some be difficult to solve
Technical barrier certainly.At present, percolate mainly uses the main process of biochemical system+nanofiltration+reverse-osmosis treated, enables waste water
Reach discharge standard.Although the technique is largely used, the combination rate of recovery that also there is nanofiltration+reverse osmosis process is not higher than
65%.The waste water of a large amount of processing systems cannot recycle direct exhaust emission environment.
Utility model content
To solve the above problems, the utility model provides a kind of percolate concentration liquid advanced treatment device.
To achieve the above object, the utility model, which is adopted the following technical scheme that, is：A kind of percolate concentration liquid is deep
Processing equipment is spent, including sodium filters common RO films concentrated water pond, the delivery port that sodium filters common RO films concentrated water pond is connected to tune by pipeline
Pond is saved, the delivery port of regulating reservoir is connected to the electric Fenton of ultrasonic wave by pipeline, and the delivery port of ultrasonic wave electricity Fenton is connected by pipeline
Security filter is connected to, the delivery port of security filter is connected to one-level high pressure counter-infiltration, one-level high pressure reverse osmosis by plunger pump
Thoroughly provided with the outlet of first-stage reverse osmosis concentrated water and by-pass filtration water out, described by-pass filtration water out is connected to production by pipeline
Water tank, described first-stage reverse osmosis concentrated water outlet is connected to two grades of high pressure counter-infiltrations by high-pressure pump, and two grades of high pressure counter-infiltrations are set
There are the outlet of two-pass reverse osmosis concentrated water and secondary filtration water out, described two-pass reverse osmosis concentrated water outlet is connected to by pipeline
Vaporising device, described secondary filtration water out is connected to water producing tank.
Further, the electric Fenton of described ultrasonic wave includes housing, and housing is divided into upper chamber and lower chambers, described cavity of resorption
Room is provided with the solution that pH value is 3, and described epicoele chamber interior walls, which are provided with supersonic generator, described upper chamber, is provided with some
Crossbearer is filled with carbon particle between the iron plate in upper chamber, described iron plate.
FE2+, OH- plasma are produced by supersonic generator dissolving iron plate, COD in waste water (COD) is removed
Except 90-99%, and biochemistry is improved than (BOD/COD)>0.4, oil emulsion, suspended oil, SS, most of pollutant such as COD is from water body
Middle separation, recycles carbon particle absorption (have high efficient solid and liquid separation performance), the material of difficult degradation in the electric Fenton of ultrasonic wave not
Disconnected reaction and degraded, make water outlet safer, more stable, more smooth, more clarify.Go out water bacteria, suspension, turbidity close to zero,
Can direct reuse after sanitary sewage disposal.For the processing of polygamy high-concentration industrial-water, can more effectively remove COD in waste water,
The various noxious pollutants such as heavy metal, PVA, greasy dirt, phosphate, ion pigment, water outlet is that can reach discharging standards.
Further, the security filter includes housing, air bleeding valve, valve, filter core, and the filter core is located in housing,
The air bleeding valve and valve are located at case top.
Further, the one-level high pressure counter-infiltration includes putamina, filtration core, counter-infiltration frame, conductivity meter, flow
Meter, pressure gauge, pressure piping, low pressure pipeline, the putamina is in the counter-infiltration frame, and described filtration core is through in putamina
The heart, described filtration core includes deflector, film unit, the deflector being from top to bottom superimposed, described pressure piping, low-voltage tube
Road, conductivity meter, flowmeter, pressure gauge are outside putamina.
Utility model works principle：Sodium filters common RO films concentrated water pond and percolate concentration liquid is separated into two parts,
A part is the trapped fluid of main thing containing divalent inorganic (such as CaSO4) and organic matter, and another part mainly contains chloride
Water outlet, the water outlet of chloride enters regulating reservoir and after pH value neutralization enter through the electric Fenton of ultrasonic wave, and ultrasonic wave electricity Fenton is removed
COD (COD) in 95% oil and removal 90-99% waste water, by security filter；To improve the rate of recovery, one-level is high
Pressure counter-infiltration and two grades of high pressure counter-infiltrations can be run under 10-20MPa, can make the rate of recovery of reverse-osmosis treated percolate
More than 90% is brought up to from 80%, the concentrate devaporation concentration after processing, residue directly carries out desiccation or burning after concentration,
Water after filtering enters water producing tank.
The beneficial effects of the utility model are：The utility model is simple in construction, is effectively handled by the electric Fenton of ultrasonic wave
Biochemistry is than low highly difficult organic matter sewage, then the production water direct reuse after being handled by reverse osmosis unit, and the rate of recovery is up to
More than 90%.
Brief description of the drawings
Fig. 1 is the utility model structure chart.
Mark explanation：1. sodium filters common RO films concentrated water pond；2. regulating reservoir；3. ultrasonic wave electricity Fenton；4. security filter；5.
Plunger pump；6. one-level high pressure counter-infiltration；7. high-pressure pump；8. two grades of high pressure counter-infiltrations；9. water producing tank；10. vaporising device.
Embodiment
Refer to shown in Fig. 1, a kind of percolate concentrates liquid advanced treatment device, including sodium filters common RO films concentrated water pond
1, the delivery port that sodium filters common RO films concentrated water pond 1 is connected to regulating reservoir 2 by pipeline, and the delivery port of regulating reservoir 2 is connected by pipeline
The electric Fenton 3 of ultrasonic wave is connected to, the delivery port of ultrasonic wave electricity Fenton 3 is connected to security filter 4, security filter 4 by pipeline
Delivery port one-level high pressure counter-infiltration 6 is connected to by plunger pump 5, one-level high pressure counter-infiltration 6 goes out provided with first-stage reverse osmosis concentrated water
Mouth and by-pass filtration water out, described by-pass filtration water out are connected to water producing tank 9, described first-stage reverse osmosis by pipeline
Concentrated water outlet is connected to two grades of high pressure counter-infiltrations 8 by high-pressure pump 7, and two grades of high pressure counter-infiltrations 8 go out provided with two-pass reverse osmosis concentrated water
Mouth and secondary filtration water out, described two-pass reverse osmosis concentrated water outlet are connected to vaporising device 10, described two by pipeline
Level filtering water outlet is connected to water producing tank 9.
Further, the electric Fenton 3 of described ultrasonic wave includes housing, and housing is divided into upper chamber and lower chambers, it is described under
Chamber is provided with supersonic generator, described upper chamber provided with some provided with the solution that pH value is 3, described epicoele chamber interior walls
Bar crossbearer is filled with carbon particle between the iron plate in upper chamber, described iron plate.
FE2+, OH- plasma are produced by supersonic generator dissolving iron plate, COD in waste water (COD) is removed
Except 90-99%, and biochemistry is improved than (BOD/COD)>0.4, oil emulsion, suspended oil, SS, most of pollutant such as COD is from water body
Middle separation, recycles carbon particle absorption (have high efficient solid and liquid separation performance), the material of difficult degradation in the electric Fenton 3 of ultrasonic wave not
Disconnected reaction and degraded, make water outlet safer, more stable, more smooth, more clarify.Go out water bacteria, suspension, turbidity close to zero,
Can direct reuse after sanitary sewage disposal.For the processing of polygamy high-concentration industrial-water, can more effectively remove COD in waste water,
The various noxious pollutants such as heavy metal, PVA, greasy dirt, phosphate, ion pigment, water outlet is that can reach discharging standards.
Further, the security filter includes housing, air bleeding valve, valve, filter core, and the filter core is located in housing,
The air bleeding valve and valve are located at case top.
Further, the one-level high pressure counter-infiltration 6 includes putamina, filtration core, counter-infiltration frame, conductivity meter, flow
Meter, pressure gauge, pressure piping, low pressure pipeline, the putamina is in the counter-infiltration frame, and described filtration core is through in putamina
The heart, described filtration core includes deflector, film unit, the deflector being from top to bottom superimposed, described pressure piping, low-voltage tube
Road, conductivity meter, flowmeter, pressure gauge are outside putamina.
Utility model works principle：Sodium filters common RO films concentrated water pond 1 and percolate concentration liquid is separated into two parts,
A part is the trapped fluid of main thing containing divalent inorganic (such as CaSO4) and organic matter, and another part mainly contains chloride
Water outlet, the water outlet of chloride enters regulating reservoir 2 and after pH value neutralization enter through the electric Fenton 3 of ultrasonic wave, and ultrasonic wave electricity Fenton 3 is gone
Except COD (COD) in 95% oil and removal 90-99% waste water, by security filter 4；To improve the rate of recovery, one-level
High pressure counter-infiltration 6 and two grades of high pressure counter-infiltrations 8 can be run under 10-20MPa, can make returning for reverse-osmosis treated percolate
Yield brings up to more than 90% from 80%, concentrate devaporation after processing concentration, after concentration residue directly carry out desiccation or
Burn, the water after filtering enters water producing tank 9.
The beneficial effects of the utility model are：The utility model is simple in construction, is effectively handled by the electric Fenton of ultrasonic wave
Biochemistry is than low highly difficult organic matter sewage, then the production water direct reuse after being handled by reverse osmosis unit, and the rate of recovery is up to
More than 90%.
Embodiment of above is only that preferred embodiment of the present utility model is described, not to the utility model
Scope be defined, on the premise of the utility model design spirit is not departed from, this area ordinary skill technical staff to this
Various modifications and improvement that the technical scheme of utility model is made, all should fall into the guarantor that claims of the present utility model are determined
In the range of shield.
Claims (4)
1. a kind of percolate concentrates liquid advanced treatment device, it is characterised in that：Common RO films concentrated water pond, sodium filter are filtered including sodium
The delivery port in common RO film concentrated waters pond is connected to regulating reservoir by pipeline, and the delivery port of regulating reservoir is connected to ultrasonic wave by pipeline
Electric Fenton, the delivery port of ultrasonic wave electricity Fenton is connected to security filter by pipeline, and the delivery port of security filter passes through post
Plug pump is connected to one-level high pressure counter-infiltration, and the counter-infiltration of one-level high pressure goes out provided with the outlet of first-stage reverse osmosis concentrated water and by-pass filtration water
Mouthful, described by-pass filtration water out is connected to water producing tank by pipeline, and described first-stage reverse osmosis concentrated water outlet passes through high pressure
Pump is connected to two grades of high pressure counter-infiltrations, and two grades of high pressure counter-infiltrations are exported and secondary filtration water out provided with two-pass reverse osmosis concentrated water,
Described two-pass reverse osmosis concentrated water outlet is connected to vaporising device by pipeline, and described secondary filtration water out is connected to production water
Case.
2. a kind of percolate concentration liquid advanced treatment device according to claim 1, it is characterised in that：Described is super
Sound wave electricity Fenton includes housing, and housing is divided into upper chamber and lower chambers, and described lower chambers are described provided with the solution that pH value is 3
Epicoele chamber interior walls be provided with supersonic generator, some crossbearers are provided with described upper chamber in the iron plate in upper chamber, institute
Carbon particle is filled between the iron plate stated.
3. a kind of percolate concentration liquid advanced treatment device according to claim 1, it is characterised in that：The security
Filter includes housing, air bleeding valve, valve, filter core, and the filter core is in housing, and the air bleeding valve and valve are located at housing top
Portion.
4. a kind of percolate concentration liquid advanced treatment device according to claim 1, it is characterised in that：The one-level
High pressure counter-infiltration includes putamina, filtration core, counter-infiltration frame, conductivity meter, flowmeter, pressure gauge, pressure piping, low-voltage tube
Road, the putamina is in counter-infiltration frame, and described filtration core is through putamina center, and described filtration core is included by up to
Deflector, film unit, the deflector of lower superposition, described pressure piping, low pressure pipeline, conductivity meter, flowmeter, pressure gauge are set
In outside putamina.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620877908.5U CN206502710U (en) | 2016-08-13 | 2016-08-13 | Percolate concentrates liquid advanced treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620877908.5U CN206502710U (en) | 2016-08-13 | 2016-08-13 | Percolate concentrates liquid advanced treatment device |
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| Publication Number | Publication Date |
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| CN206502710U true CN206502710U (en) | 2017-09-19 |
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ID=59843030
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| CN201620877908.5U Active CN206502710U (en) | 2016-08-13 | 2016-08-13 | Percolate concentrates liquid advanced treatment device |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108218069A (en) * | 2018-02-09 | 2018-06-29 | 威士邦（厦门）环境科技有限公司 | A kind of landfill leachate treatment equipment and technique |
| CN109231319A (en) * | 2018-09-06 | 2019-01-18 | 上海焓净电力技术有限公司 | Leachate/waste water/waste oil atomization return evaporation burning zero-emission treatment device |
| CN109970232A (en) * | 2017-12-28 | 2019-07-05 | 江苏久吾高科技股份有限公司 | A kind of processing method and processing device of effluent brine |
| CN110316893A (en) * | 2019-07-18 | 2019-10-11 | 烟台金正环保科技有限公司 | A kind of integrated treatment process of landfill leachate |
| CN111646599A (en) * | 2020-06-18 | 2020-09-11 | 厦门嘉戎技术股份有限公司 | System and method for integrated treatment of leachate of garbage transfer station |
| WO2023072097A1 (en) * | 2021-10-25 | 2023-05-04 | 梁维安 | Fenton process and ceramic membrane filtering-integrated sewage treatment unit |
-
2016
- 2016-08-13 CN CN201620877908.5U patent/CN206502710U/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109970232A (en) * | 2017-12-28 | 2019-07-05 | 江苏久吾高科技股份有限公司 | A kind of processing method and processing device of effluent brine |
| CN109970232B (en) * | 2017-12-28 | 2023-06-16 | 江苏久吾高科技股份有限公司 | Treatment method and device for waste brine |
| CN108218069A (en) * | 2018-02-09 | 2018-06-29 | 威士邦（厦门）环境科技有限公司 | A kind of landfill leachate treatment equipment and technique |
| CN109231319A (en) * | 2018-09-06 | 2019-01-18 | 上海焓净电力技术有限公司 | Leachate/waste water/waste oil atomization return evaporation burning zero-emission treatment device |
| CN110316893A (en) * | 2019-07-18 | 2019-10-11 | 烟台金正环保科技有限公司 | A kind of integrated treatment process of landfill leachate |
| CN111646599A (en) * | 2020-06-18 | 2020-09-11 | 厦门嘉戎技术股份有限公司 | System and method for integrated treatment of leachate of garbage transfer station |
| WO2023072097A1 (en) * | 2021-10-25 | 2023-05-04 | 梁维安 | Fenton process and ceramic membrane filtering-integrated sewage treatment unit |
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