CN2920976Y - Adsorption, sedimentation and separation integrated water treatment device - Google Patents
Adsorption, sedimentation and separation integrated water treatment device Download PDFInfo
- Publication number
- CN2920976Y CN2920976Y CN 200620105563 CN200620105563U CN2920976Y CN 2920976 Y CN2920976 Y CN 2920976Y CN 200620105563 CN200620105563 CN 200620105563 CN 200620105563 U CN200620105563 U CN 200620105563U CN 2920976 Y CN2920976 Y CN 2920976Y
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- CN
- China
- Prior art keywords
- valve
- links
- sedimentation
- water
- filtration
- Prior art date
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Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 46
- 238000004062 sedimentation Methods 0.000 title claims abstract description 17
- 238000000926 separation method Methods 0.000 title claims abstract description 16
- 238000001179 sorption measurement Methods 0.000 title abstract description 9
- 238000001914 filtration Methods 0.000 claims abstract description 38
- 230000000630 rising effect Effects 0.000 claims description 24
- 238000010521 absorption reaction Methods 0.000 claims description 12
- 230000008676 import Effects 0.000 claims description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 12
- 238000005516 engineering process Methods 0.000 abstract description 11
- 239000000725 suspension Substances 0.000 abstract description 9
- 230000010354 integration Effects 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- 239000006228 supernatant Substances 0.000 abstract description 2
- 239000002351 wastewater Substances 0.000 abstract description 2
- 239000002245 particle Substances 0.000 abstract 1
- 238000005194 fractionation Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 239000002594 sorbent Substances 0.000 description 3
- 230000001112 coagulating effect Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 230000001052 transient effect Effects 0.000 description 1
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- Water Treatment By Sorption (AREA)
Abstract
The utility model discloses a water treatment device integrating the adsorption, the sedimentation and the separation, which comprises a slop pail, a precoat barrel, a pump and a sedimentation and separation filter in which a septum drum is provided to divide the filter into an exterior sedimentation chamber and an interior filtration chamber in which a filtration element is provided. The equipment running, the high concentration suspension goes forward spirally in the sedimentation chamber to subside most particle suspended substance, and the supernatants enter the filtration chamber to participate in filtration. The introduction of the sedimentation chamber widens the application range of diatomite technology, so that the filtration of the wastewater with high concentration suspended matter is possible; and compared with the adsorption and separation integration technology, the utility model can effectively delay the raise of filtration water head and prolong the operating time. The utility model has the advantages of simple and close structure and high efficiency of water treatment.
Description
Technical field
The utility model relates to a kind of absorption, sedimentation, separation integrated water treatment device, belongs to environmental technology and water treatment field.
Background technology
Nowadays the diatomite filtration technology is widely used, especially diatomite filtration has caused concern widely especially with the combination of various technology, but the diatomite filtration technology is applied to in the water treatment more, the process object turbidity is low, water quality is better relatively, and this has just influenced the application of diatomite filtration technology in sewage and it is with absorption, the combination of coagulating, because can make in absorption or the coagulating process that concentration of suspension increases in the water, especially with absorption reaction for very.Adding of heavy dose of sorbent material makes that filtering cloth head rose rapidly when diatomite separated, and makes to make system operation time short by the filtering terminal point of the very fast arrival in diatomite filtration unit.
Summary of the invention
The purpose of this utility model provides a kind of absorption, sedimentation, separation integrated water treatment device, to realize the high efficiency separation processing to high suspended matter concentration sewage.
Absorption of the present utility model, sedimentation, separation integrated water treatment device comprise the slop pail of being with stirrer, precoating bucket, pump and the settlement separate strainer of band stirrer; Be provided with in the settlement separate strainer with settlement separator be separated into outside settling pocket and self-filtering chamber every tube, the center of self-filtering chamber is equipped with filter element, the top of settlement separate strainer is equipped with tensimeter and rising pipe, rising pipe is communicated with the precoating bucket through first valve, the water-in of pump also is connected to two water inlet pipes, article one, water inlet pipe links to each other through the outlet of the 3rd valve with the precoating bucket, and another water inlet pipe links to each other with the water outlet of slop pail through the 4th valve; The water outlet of pump also is connected to three rising pipes, article one, the outside settling pocket bottom of rising pipe in the 5th valve and settlement separate strainer links to each other, the self-filtering chamber bottom of second rising pipe in the 6th valve and settlement separate strainer links to each other, article three, rising pipe is divided into two-way through the 7th valve, wherein one the tunnel links to each other with the filter element water outlet, another road second valve links to each other with the under meter import, and the outlet of under meter is connected with water shoot, and the slop pail bottom links to each other with rising pipe through the 8th valve.
The device working condition:
Adopt diatomite as precoating paint, forming thick on filter element is the filtering layer of 1-5 millimeter, in slop pail with the online sorbent material that adds of amount of inlet water, stir formation suspension by stirrer, open the 4th valve, the 5th valve, squeeze into suspension in the outside settling pocket of fractionation by adsorption filtration chamber with pump, in the externally settling pocket internal screw rising of water inlet suspension liquid, the rising filtering velocity satisfies≤0.2mm/s, the sorbent material that the suspension of high density externally forms high density in the settling pocket band that suspends, in this effect that forms similar settling pond, the suspended substance that dams and rise, the supernatant liquor overflow enters the self-filtering chamber and participates in filtering, treated water effluxes through behind the under meter, show that when filtering the pressure value of reaching capacity solid-liquid separation finishes, stop filtration, close the 4th valve, the 5th valve.Open the 3rd valve, the 6th valve, oppositely water inlet is washed, and the high density adsorbent suspension of outside settling pocket is discharged by its bottom pipe.After finishing, back flushing begins the adsorption and sedimentation isolation integral cycle of a new round.
The beneficial effects of the utility model are:
The object that diatomite filtration is used often is a low-cloudy water, filtering cloth head rises fast in the adsorption separation technology operational process, the cycle of operation is short, is provided with every bucket in device, and the filtration chamber has been separated into outside settling pocket and self-filtering chamber, the introducing of settling pocket, enlarged the range of application of diatomite technology, make high suspended matter concentration waste water be filtered into for may, compare the fractionation by adsorption integrated technique, can effectively delay the rising of filtering cloth head, prolong working time.Absorption of the present utility model, sedimentation, separation integrated water treatment device, compact construction is simple, the processing efficiency height has solved fractionation by adsorption integration apparatus transient problems working time effectively, and the scope of application of diatomite filtration has been expanded to high turbid sewage by original low turbidity water.
Description of drawings
Fig. 1 is absorption of the present utility model, sedimentation, separation integrated water treatment device synoptic diagram;
Fig. 2 is the water treatment effect contrast figure of the utility model and prior art.
Embodiment
In order better to understand the utility model, be described further below in conjunction with accompanying drawing and specific embodiment.
With reference to Fig. 1, absorption of the present utility model, sedimentation, separation integrated water treatment device comprise the slop pail 1 of being with stirrer 2, precoating bucket 3, pump 11 and the settlement separate strainer 8 of band stirrer 20; Be provided with in the settlement separate strainer 8 with settlement separator 8 be separated into outside settling pocket and self-filtering chamber every tube 13, the center of self-filtering chamber is equipped with filter element 7, the top of settlement separate strainer 8 is equipped with tensimeter 6 and rising pipe, rising pipe is communicated with precoating bucket 3 through first valve 5, the water-in of pump 11 also is connected to two water inlet pipes, article one, water inlet pipe links to each other with the outlet of precoating bucket 3 through the 3rd valve 15, and another water inlet pipe links to each other with the water outlet of slop pail 1 through the 4th valve 14; The water outlet of pump also is connected to three rising pipes, article one, the outside settling pocket bottom of rising pipe in the 5th valve 16 and settlement separate strainer 8 links to each other, the self-filtering chamber bottom of second rising pipe in the 6th valve 18 and settlement separate strainer 8 links to each other, article three, rising pipe is divided into two-way through the 7th valve 19, wherein one the tunnel links to each other with filter element 7 water outlets, another road second valve 17 links to each other with the import of under meter 9, the outlet of under meter 9 links to each other with water shoot, and slop pail 1 bottom the 8th valve 12 links to each other with rising pipe.
Embodiment
Adopt diatomite as precoating paint, forming thick is the filtering layer of 1-5 millimeter, test with the tap water water distribution, add the 2g/L wilkinite in the tap water, add the auxiliary sedimentation of 200mg/L coagulating agent simultaneously, stir and form suspension, suspension is squeezed into settlement separate equipment with pump, adopt and filter filtering velocity 0.76m
3/ m
2H.
Absorption of the present utility model, sedimentation, separation integrated water treatment device and existing fractionation by adsorption integrated water treatment equipment are carried out the contrast of the situation of filtering, seen Fig. 2.
The utility model technical operation time is 255min, and prior art working time is 155min, and it is about 40% that the utility model more original technology working time increases, and effect is obvious.
Claims (1)
1. absorption, sedimentation, separation integrated water treatment device is characterized in that: comprise the slop pail (1) of band stirrer (2), precoating bucket (3), pump (11) and the settlement separate strainer (8) of band stirrer (20); Be provided with in the settlement separate strainer (8) with settlement separator (8) be separated into outside settling pocket and self-filtering chamber every tube (13), the center of self-filtering chamber is equipped with filter element (7), the top of settlement separate strainer (8) is equipped with tensimeter (6) and rising pipe, rising pipe is communicated with precoating bucket (3) through first valve (5), the water-in of pump (11) also is connected to two water inlet pipes, article one, water inlet pipe links to each other through the outlet of the 3rd valve (15) with precoating bucket (3), and another water inlet pipe links to each other through the water outlet of the 4th valve (14) with slop pail (1); The water outlet of pump also is connected to three rising pipes, article one, the outside settling pocket bottom of rising pipe in the 5th valve (16) and settlement separate strainer (8) links to each other, the self-filtering chamber bottom of second rising pipe in the 6th valve (18) and settlement separate strainer (8) links to each other, article three, rising pipe is divided into two-way through the 7th valve (19), wherein one the tunnel links to each other with filter element (7) water outlet, another road second valve (17) links to each other with the import of under meter (9), the outlet of under meter (9) links to each other with water shoot, and slop pail (1) bottom links to each other with rising pipe through the 8th valve (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620105563 CN2920976Y (en) | 2006-07-11 | 2006-07-11 | Adsorption, sedimentation and separation integrated water treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620105563 CN2920976Y (en) | 2006-07-11 | 2006-07-11 | Adsorption, sedimentation and separation integrated water treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2920976Y true CN2920976Y (en) | 2007-07-11 |
Family
ID=38253455
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620105563 Expired - Fee Related CN2920976Y (en) | 2006-07-11 | 2006-07-11 | Adsorption, sedimentation and separation integrated water treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2920976Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102232133B (en) * | 2007-11-25 | 2015-04-29 | 泰克赛普环境有限公司 | Device for treating rain water |
| CN105289067A (en) * | 2015-11-13 | 2016-02-03 | 东北农业大学 | Modified rice hull ash pre-coated film device used for treating rural high ammonia-nitrogen water source water, and method used for treating rural high ammonia-nitrogen water source water using modified rice hull ash pre-coated film device |
-
2006
- 2006-07-11 CN CN 200620105563 patent/CN2920976Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102232133B (en) * | 2007-11-25 | 2015-04-29 | 泰克赛普环境有限公司 | Device for treating rain water |
| CN105289067A (en) * | 2015-11-13 | 2016-02-03 | 东北农业大学 | Modified rice hull ash pre-coated film device used for treating rural high ammonia-nitrogen water source water, and method used for treating rural high ammonia-nitrogen water source water using modified rice hull ash pre-coated film device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20070711 Termination date: 20100711 |