CN202038934U - Multi-stage serially-connected fluidized bed reclaimed water purification tower - Google Patents
Multi-stage serially-connected fluidized bed reclaimed water purification tower Download PDFInfo
- Publication number
- CN202038934U CN202038934U CN2011201561490U CN201120156149U CN202038934U CN 202038934 U CN202038934 U CN 202038934U CN 2011201561490 U CN2011201561490 U CN 2011201561490U CN 201120156149 U CN201120156149 U CN 201120156149U CN 202038934 U CN202038934 U CN 202038934U
- Authority
- CN
- China
- Prior art keywords
- water
- tower body
- purifying chamber
- tower
- water purifying
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 89
- 238000000746 purification Methods 0.000 title abstract description 14
- 239000002245 particle Substances 0.000 claims abstract description 8
- 239000003463 adsorbent Substances 0.000 claims abstract description 7
- 239000002594 sorbent Substances 0.000 claims description 20
- 230000002000 scavenging effect Effects 0.000 claims description 10
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical class O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 4
- 235000013162 Cocos nucifera Nutrition 0.000 claims description 3
- 244000060011 Cocos nucifera Species 0.000 claims description 3
- 239000003610 charcoal Substances 0.000 claims description 3
- 230000007420 reactivation Effects 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 5
- 238000012423 maintenance Methods 0.000 abstract description 2
- 230000008929 regeneration Effects 0.000 abstract 1
- 238000011069 regeneration method Methods 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 3
- 241000282326 Felis catus Species 0.000 description 3
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000003287 bathing Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Images
Classifications
-
- 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
Landscapes
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Water Treatment By Sorption (AREA)
Abstract
本实用新型涉及一种多级串联流化床中水净化塔，其特征在于：塔体内装有多级串联的净水室，净水室的上、下壳体有均布的直径小于吸附剂粒径的小孔，净水室外壁与塔体内壁留有通道，通道与净水室下部的圆锥形口连通，并与下一级净水室上部的倒锥形口连通，圆锥形的锥面和倒圆锥形的锥面有均布的直径小于吸附剂粒径的小孔，并与塔体内壁组成截面为三角形挡板，布水器安装在塔体下部并与泵连接，布料器安装在塔体上方的锥形口上方，塔体底部一级净水室的锥形口与吸附剂再生装置连接，该净化塔具有拆卸、组装、检修方便，费用低，吸附剂移动速度稳定、流化状态稳定，净化效果好的优点与效果。
The utility model relates to a multi-stage series fluidized bed water purification tower, which is characterized in that: the tower body is equipped with multi-stage series-connected water purification chambers, and the upper and lower shells of the water purification chambers have uniformly distributed diameters smaller than the adsorbent Small holes of particle size, there is a channel on the outer wall of the water purification chamber and the inner wall of the tower, the channel communicates with the conical mouth of the lower part of the water purification chamber, and communicates with the inverted conical mouth of the upper part of the next water purification chamber, the conical cone The conical surface and the inverted conical surface have evenly distributed small holes with a diameter smaller than the particle size of the adsorbent, and form a triangular baffle with the inner wall of the tower. The water distributor is installed at the lower part of the tower body and connected to the pump. The distributor is installed Above the conical port above the tower body, the conical port of the primary water purification chamber at the bottom of the tower body is connected to the adsorbent regeneration device. The purification tower has the advantages of convenient disassembly, assembly and maintenance, low cost, stable moving speed of adsorbent, and high flow rate. The advantages and effects of stable chemical state and good purification effect.
Description
Technical field
The utility model relates to water scavenging tower in a kind of plural serial stage fluidized-bed, and the deep purifying that is used for water is handled, and belongs to water treatment field.
Background technology
The water that obtains after the treated deep purifying of municipal effluent is handled, comprise water and the building of sewage work after second-stage treatment is deepened processing again, the bathing water of living community, vegetable washing waters etc. are concentrated water after treatment, water in the general designation, contain material such as ammonia-state nitrogen can make in water utilize again and be subjected to certain limitation, particularly process water or urban afforestation water all can not be used again, present moving-bed and the fluidized-bed water purifying plant that adopts, the used water-purifying material of fluidized-bed water purifying plant is difficult to keep uniform fluidized state, the water-purifying material bed of moving-bed water purifying plant moves down the bad control of speed, and bed moves instability, the bed skewness.
But the utility model purpose just for the shortcoming that overcomes above-mentioned prior art with not enough and design water scavenging tower in the plural serial stage fluidized-bed of the ammonia-state nitrogen in the water in a kind of active adsorption, thereby water can be used for process water or urban afforestation water in making.
The purpose of this utility model realizes by following technical scheme:
Water scavenging tower in a kind of plural serial stage fluidized-bed comprises tower body 1, distributor 2, water purifying chamber 3, water distributor 4, pump 5 and sorbent material,
The water purifying chamber of plural serial stage is housed in the tower body, every grade of water purifying chamber is by last, lower housing is formed, posticum 9 is arranged on the upper housing, in the water purifying chamber, lower housing has the aperture of uniform diameter less than the sorbent material particle diameter, water purifying chamber is fixed on the tower body inwall by the supported on both sides plate, water purifying chamber's outer wall and tower body inwall leave passage 6, passage is communicated with the conical mouth of water purifying chamber bottom, and be communicated with the back taper mouth on next stage water purifying chamber top, the conical conical surface and the obconic conical surface have the aperture of uniform diameter less than the sorbent material particle diameter, and to form the cross section with the tower body inwall be trilateral baffle plate 7, water distributor is installed in the tower body bottom and is connected with pump, distributor is installed in the bell top of tower body top, and the back taper outlet of the water purifying chamber of tower body bottom one-level is connected with adsorbent reactivation device 8.
The decontamination chamber of described plural serial stage is 3～5 grades; Described sorbent material is cocoanut active charcoal or modified zeolite.
Owing to take technique scheme, make compared with the prior art following advantage of the utility model and effect:
A) water purifying chamber at different levels dismounting, assembling, maintenance is convenient, and expense is low;
B) the sorbent material translational speed is stable, fluidized state is stable, good purification.
Description of drawings
Fig. 1 is an one-piece construction synoptic diagram of the present utility model.
Embodiment
Below in conjunction with accompanying drawing the utility model is further specified: water scavenging tower in a kind of plural serial stage fluidized-bed, by shown in Figure 1, comprise tower body 1, distributor 2, water purifying chamber 3, water distributor 4, pump 5 and sorbent material, the water purifying chamber of plural serial stage is housed in the tower body, every grade of water purifying chamber is by last, lower housing is formed, be convenient to dismounting, posticum 9 is arranged on the upper housing, being used for water purification discharges, in the water purifying chamber, lower housing has the aperture of uniform diameter less than the sorbent material particle diameter, prevent that sorbent material from entering water purifying chamber, water purifying chamber is fixed on the tower body inwall by the supported on both sides plate, water purifying chamber's outer wall and tower body inwall leave passage 6, it is the sorbent material passage, passage is communicated with the conical mouth of water purifying chamber bottom, and be communicated with the back taper mouth on next stage water purifying chamber top sorbent material is better contacted with middle water, the conical conical surface and the obconic conical surface have the aperture of uniform diameter less than the sorbent material particle diameter, and to form the cross section with the tower body inwall be trilateral baffle plate 7, not only porous but also can make the sorbent material uniform distribution, water distributor is installed in the tower body bottom and is connected with pump, distributor is installed in the bell top of tower body top, and the back taper outlet of the water purifying chamber of tower body bottom one-level is connected with adsorbent reactivation device 8.
The water purifying chamber of described plural serial stage is 3～5 grades; Sorbent material is cocoanut active charcoal or modified zeolite, and these two kinds of scavenging material centering water depths are handled good effect.Loading capacity is big, realizes the efficient absorption to ammonia nitrogen.
During work, pass through water distributor, under the effect of pump, make to be processed in water rise at the bottom of the tower and flow, and continuously by placed in-line one-level, secondary, three grades of water purifying chamber flow, until last step, with contact and carried out purifying treatment from the cat head water purifying chamber's peripheral channel moving phase that enters suitable for reading by distributor from the cat head sorbent material that enters suitable for reading, handle by stage purification, qualified middle water flows out by Link Port from the water purifying chamber of cat head last step, and sorbent material enters regenerating unit 8 from the one-level water purifying chamber outlet of tower body bottom when saturated and handles, according to the difference to requirements in water quality and flooding velocity flow velocity, can be chosen in different single-stage water outlets arbitrarily, as special requirement being arranged for water outlet, can install overflow device additional in the water outlet periphery, make water outlet even.
Handling ammonia-nitrogen content with the utility model is the middle water of 6mg/l, adopts three grades of series fluidized bed middle water scavenging tower, is sorbent material with modified zeolite, and water contains below the ammonia nitrogen 0.3mg/l in the processing back.Purification rate reaches 95%.
Claims (3)
1. water scavenging tower in the plural serial stage fluidized-bed comprises tower body (1), and distributor (2), water purifying chamber (3), water distributor (4), pump (5) and sorbent material is characterized in that:
The water purifying chamber of plural serial stage is housed in the tower body, every grade of water purifying chamber is by last, lower housing is formed, posticum (9) is arranged on the upper housing, in the water purifying chamber, lower housing has the aperture of uniform diameter less than the sorbent material particle diameter, water purifying chamber is fixed on the tower body inwall by the supported on both sides plate, water purifying chamber's outer wall and tower body inwall leave passage (6), passage is communicated with the conical mouth of water purifying chamber bottom, and be communicated with the back taper mouth on next stage water purifying chamber top, the conical conical surface and the obconic conical surface have the aperture of uniform diameter less than the sorbent material particle diameter, and to form the cross section with the tower body inwall be trilateral baffle plate (7), water distributor is installed in the tower body bottom and is connected with pump, distributor is installed in the bell top of tower body top, and the back taper outlet of the water purifying chamber of tower body bottom one-level is connected with adsorbent reactivation device (8).
2. water scavenging tower in according to claim 1, the water purifying chamber that it is characterized in that described plural serial stage is 3～5 grades.
3. water scavenging tower in according to claim 1 is characterized in that described sorbent material is cocoanut active charcoal or modified zeolite.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201561490U CN202038934U (en) | 2011-05-17 | 2011-05-17 | Multi-stage serially-connected fluidized bed reclaimed water purification tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201561490U CN202038934U (en) | 2011-05-17 | 2011-05-17 | Multi-stage serially-connected fluidized bed reclaimed water purification tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202038934U true CN202038934U (en) | 2011-11-16 |
Family
ID=44966391
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201561490U Expired - Fee Related CN202038934U (en) | 2011-05-17 | 2011-05-17 | Multi-stage serially-connected fluidized bed reclaimed water purification tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202038934U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104261580A (en) * | 2014-09-23 | 2015-01-07 | 深圳市博儒环境技术有限公司 | Pressure decontaminating water purifying device |
| CN118719772A (en) * | 2024-08-05 | 2024-10-01 | 光大环保技术装备（常州）有限公司 | Fly ash pyrolysis device and pyrolysis method thereof |
-
2011
- 2011-05-17 CN CN2011201561490U patent/CN202038934U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104261580A (en) * | 2014-09-23 | 2015-01-07 | 深圳市博儒环境技术有限公司 | Pressure decontaminating water purifying device |
| CN118719772A (en) * | 2024-08-05 | 2024-10-01 | 光大环保技术装备（常州）有限公司 | Fly ash pyrolysis device and pyrolysis method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US8758608B2 (en) | Continuously flowing, inner circulatory, quasi-fluidized-bed reactor for resin ion exchange and adsorption | |
| CN202497818U (en) | Multi-level comprehensive treatment system for foul gas | |
| CN107098427A (en) | A kind of method that utilization adsorption tank efficiently removes heavy metal pollution in farmland irrigating water | |
| CN202038934U (en) | Multi-stage serially-connected fluidized bed reclaimed water purification tower | |
| CN204509054U (en) | A kind of composite highly effective biological sewage treatment device | |
| CN201648186U (en) | A composite membrane bioreactor | |
| CN109603790A (en) | A kind of regeneration cycle filtration system | |
| CN205241467U (en) | Self -circulation biomembrane denitrogenation sewage treatment device | |
| CN204281406U (en) | A kind of membrane bioreactor based on fouling membrane in-situ control | |
| CN204625303U (en) | Effective integrated organic waste-water treating apparatus | |
| CN103073088B (en) | Continuous adsorption system for sewage treatment process | |
| CN203295249U (en) | Water purification and treatment device | |
| CN201056517Y (en) | Multi-layer dynamic film waste water purifying device | |
| CN103495296B (en) | Granular bed continuous filtration equipment | |
| CN202785783U (en) | Small-size integrated ozone/activated carbon experiment device | |
| CN103241815B (en) | Water purifying device | |
| CN205294956U (en) | Anaerobic reactor and breed effluent disposal system | |
| CN213171946U (en) | Circular biological aerated filter with precipitation function | |
| CN204369728U (en) | A kind of New foul water disposal facility | |
| CN204111360U (en) | A kind of device utilizing porous material to fix heavy metal in modified adsorbent filtering water | |
| CN204162521U (en) | A kind of integrated apparatus except fluorine, arsenic and microorganism | |
| CN207121446U (en) | A kind of advanced multi-stage absorption bed | |
| CN202063796U (en) | Three-dimensional top end gradation biological fluidized bed | |
| CN101830589B (en) | A continuous treatment device for toxic and harmful organic wastewater | |
| CN202519084U (en) | Porous steel slag filter material sink filter reactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| DD01 | Delivery of document by public notice |
Addressee: Lu Bodi Document name: Notification to Pay the Fees |
|
| DD01 | Delivery of document by public notice |
Addressee: Lu Bodi Document name: Notification of Termination of Patent Right |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111116 Termination date: 20120517 |