CN105036233A - High-efficiency double-decker parallel type wastewater purifier - Google Patents
High-efficiency double-decker parallel type wastewater purifier Download PDFInfo
- Publication number
- CN105036233A CN105036233A CN201510367991.1A CN201510367991A CN105036233A CN 105036233 A CN105036233 A CN 105036233A CN 201510367991 A CN201510367991 A CN 201510367991A CN 105036233 A CN105036233 A CN 105036233A
- Authority
- CN
- China
- Prior art keywords
- efficiency double
- refining plant
- porous filter
- waste water
- supervisor
- 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.)
- Granted
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 38
- 238000007670 refining Methods 0.000 claims description 37
- 238000000746 purification Methods 0.000 claims description 18
- 229910000831 Steel Inorganic materials 0.000 claims description 8
- 239000010959 steel Substances 0.000 claims description 8
- 239000000706 filtrate Substances 0.000 claims description 6
- 238000007689 inspection Methods 0.000 claims description 3
- 230000002787 reinforcement Effects 0.000 claims description 2
- 239000010865 sewage Substances 0.000 abstract description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 abstract 1
- 229910052801 chlorine Inorganic materials 0.000 abstract 1
- 239000000460 chlorine Substances 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 7
- 238000010586 diagram Methods 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 239000003295 industrial effluent Substances 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 239000003599 detergent Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical group [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 230000000274 adsorptive effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 230000019771 cognition Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- -1 electric power Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Abstract
The invention discloses a high-efficiency double-decker parallel type wastewater purifier, relating to the field of sewage treatment. The high-efficiency double-decker parallel type wastewater purifier comprises a shell, wherein an upper-layer purifying device and a lower-layer purifying device are arranged in the shell; each of the upper-layer purifying device and the lower-layer purifying device comprises a conical top plate, an water inlet pipe arranged in the center of the conical top plate, a backflushing gas distribution pipe system arranged below the conical top plate, a porous filter board below the backflushing gas distribution pipe system, a filter material arranged on the porous filter board, a water collecting pipe system below the porous filter board, and an escape pipe; the water inlet pipe of the lower-layer purifying device penetrates through the porous filter board of the upper-layer purifying device and extends out of the shell. The high-efficiency double-decker parallel type wastewater purifier is mainly used for removing organic matters, chromaticity and residual chlorine in water from a water supply and drainage system. The high-efficiency double-decker parallel type wastewater purifier has the characteristics that the purifier is high in handling amount, simple to operate, unlikely to have a fault and the like, can realize fully-automatic control in combination with an electric valve and a PLC (Programmable Logic Controller) and can be widely adopted in various industries.
Description
Technical field
The present invention is used for the larger industry of the reuse quantity of circulating water such as electric power, iron and steel, municipal administration, printing and dyeing, relates to sewage treatment area, particularly relates to the parallel purification of waste water device of double bunk.
Background technology
Along with population constantly increases and economic develop rapidly, water consumption and water displacement increase year by year, and limited water resources is constantly polluted, and the imbalance between supply and demand of water resources is further sharp-pointed.Based on above-mentioned cognition, current industrial effluent reusing is subject to the attention of relevant department day by day, as the second water source newly developed, the reuse of municipal effluent and trade effluent has the advantages that the water yield is large, stable, do not need long distance water diversion, be a kind of reliable water resources.As compared to the method for sea water desaltination with other mining new source of waters such as remote water transfer, industrial effluent reusing less investment, duration short, instant effect, more real easy.The reuse of trade effluent, effectively can keep the running balance of water resources, realize the benign cycle of water, prevent the pollution of the environment, and ensures that industrial development is to the needs of water.Industrial effluent reusing will bring significant economic benefit, environmental benefit and social benefit.
In the industry production process that electric power, iron and steel water consumption are larger, solid particulate can be scattered in system along with the circulation of steam, under certain temperature, pressure and pH value condition, become dissolved impurity.And control the content contributing to reducing solubilised state metal ion as the solid impurity of the main source of dissolved impurity.A considerable amount of iron ion deposits in systems in which and can form underdeposit corrosion, and iron, silicon sequence of ion also can form deposition at steam turbine and the medium/low pressure section of boiler tubing.
It is large that common filter has floor space, and filter effect restricts by various factors, reliable undesirable, realizes full-automatic difficulty, easily produces filtrate caking, the halfway phenomenon of backwash.
Summary of the invention
The present invention is directed to the deficiencies in the prior art, provide that a kind of floor space is little, treatment capacity is large, filtration efficiency is high, effectively prevent that filtrate from luming, the parallel purification of waste water device of backwash halfway high-efficiency double-layer bed.
For realizing the object of the invention, provide following technical scheme: the parallel purification of waste water device of a kind of high-efficiency double-layer bed, comprise housing, it is characterized in that in housing, being provided with upper and lower two-layer refining plant, levels refining plant includes taper top board, be opened in the water inlet pipe at taper top board center, be arranged at the backwash gas distribution piping below taper top board, porous filter plate below backwash gas distribution piping, be arranged at the filtrate on porous filter plate, catchment piping and blow-down pipe below porous filter plate, the water inlet pipe of described lower floor refining plant stretches out outside housing through the porous filter plate of upper strata refining plant.
As preferably, the taper top board lower surface of upper strata refining plant is provided with some and supports steel pipes, supports that steel pipe bottom is provided with reinforcement gusset.
As preferably, the backwash gas distribution piping of upper strata refining plant comprise supervisor, be responsible for the ring pipe be connected and the some arms be distributed on ring pipe.
As preferably, the backwash gas distribution piping of lower floor's refining plant comprises supervisor, is connected with supervisor and vertically disposed two arms, be responsible for the arm being connected also horizontal-extending.
As preferably, the piping that catchments of upper strata refining plant comprise supervisor and with the octagon circulating line be responsible for use 8 arms of being connected and 8 tube stubs and be spliced into, described circulating line offers gully-hole.
As preferably, the piping that catchments of lower floor's refining plant comprise supervisor, be responsible for two the inc circulating lines be connected, described circulating line offers gully-hole.
As preferably, porous filter plate is circular orifice, is provided with strainer head in hole.
As preferably, housing is separately provided with inspection manhole, long waist visor and discharge opening.
Beneficial effect of the present invention: the present invention adopts the double-deck clean-up bed of right circular cylinder shape cleaner cylindrical shell, parallel-connected operation.Single cover cleaner diameter can reach more than 10 meters, detergent power reach hundreds of cube per hour more than, have superpower detergent power, floor space and construction investment only have the half of general strainer.Mix motorized valve and PLC can carry out full automatic control, all on-the-spot feedback signals are connected with watch-keeping cubicle PLC, can remote online operation supervise and control by HMI, carry out technical parameter setting, realize fault alarm display, system reserves Ethernet interface, by network communication function, can realize data transmission.High-efficiency double-layer bed parallel purification of waste water device is compared with traditional pretreatment unit, and total facility investment expense reduces, floor space is little, the better effects if of purification, shorten the clarification time, decrease operating performance; Long service life, by the hierarchical control suspended substance particle diameter of one-level filtration bed with multi filtration layer, its purification precision is high, and purification there will not be short flow phenomenon, has corrosion-resistant, wear-resisting, heatproof, the life-span is long, adsorptive power is strong, can realize water, gas mixing backwash.Be mainly used in removing Organic substance in water, colourity and chlorine residue in feedwater, disintegrating system in waste pipe.It is large that this invention has treatment capacity, simple to operate, not the feature such as easy break-down, mixes motorized valve and PLC can carry out full automatic control, can extensively adopt in industry-by-industry.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Fig. 2 is the backwash gas distribution piping schematic diagram of the upper strata refining plant of Fig. 1.
Fig. 3 is the backwash gas distribution piping schematic diagram of lower floor's refining plant of Fig. 1.
Fig. 4 is the piping schematic diagram that catchments of the upper strata refining plant of Fig. 1.
Fig. 5 is the piping schematic diagram that catchments of lower floor's refining plant of Fig. 1.
Fig. 6 is the porous filter plate schematic diagram of Fig. 1.
Embodiment
Embodiment 1: the parallel purification of waste water device of a kind of high-efficiency double-layer bed, comprise housing 1, upper and lower two-layer refining plant is provided with in housing 1, levels refining plant includes taper top board 1.1, be opened in the water inlet pipe 1.2 at taper top board 1.1 center, be arranged at the backwash gas distribution piping 1.3 below taper top board 1.1, porous filter plate 1.4 below backwash gas distribution piping 1.3, be arranged at the filtrate 1.5 on porous filter plate 1.4, catchment piping 1.6 and blow-down pipe 1.7 below porous filter plate 1.4, the porous filter plate 1.4 that the water inlet pipe 1.2 of described lower floor refining plant passes upper strata refining plant stretches out outside housing 1.Taper top board 1.1 lower surface of upper strata refining plant is provided with 6 and supports steel pipe 1.8, supports that steel pipe 1.8 bottom is provided with and strengthens gusset 1.9.The backwash gas distribution piping 1.3 of upper strata refining plant comprises supervisor 1.3.1, the ring pipe 1.3.2 be connected with supervisor 1.3.1 and the 3 arm 1.3.3 be distributed on ring pipe 1.3.2.The backwash gas distribution piping 1.3 of lower floor's refining plant comprises supervisor 1.3.1, is connected with supervisor 1.3.1 and vertically disposed two arm 1.3.3, with the arm 1.3.3 being responsible for 1.3.1 and being connected also horizontal-extending.The octagon circulating line 2 that the piping 1.6 that catchments of upper strata refining plant comprises supervisor 1.6.1 and use 8 arm 1.6.2 and 8 tube stub 1.6.3 of being connected with supervisor 1.6.1 is spliced into, described circulating line 2 offers gully-hole 1.6.4.The piping 1.6 that catchments of lower floor's refining plant comprises two the inc circulating lines 2 be responsible for 1.6.1, be connected with supervisor 1.6.1, and described circulating line 2 offers gully-hole 1.6.4.Porous filter plate 1.4 is circular orifice, is provided with strainer head 3 in hole.Housing 1 is separately provided with inspection manhole, long waist visor and discharge opening.
Waste water enters upper strata refining plant and lower floor's refining plant respectively by upper strata refining plant water inlet pipe 1.2, lower floor's refining plant water inlet pipe 1.2, after conical plate 1.1 top water eliminator refraction water distribution, purified by filtrate 1.5, water purification is collected by the piping 1.6 that catchments of levels refining plant respectively, discharge outside housing 1 through the piping 1.6 that catchments respectively again, be promoted to after collecting and use water spot reuse; Backwash process controls backwash lift pump by PLC, and backwash water is controlled to enter through the piping 1.6 that catchments by motorized valve, and carry out air bump rinse operation through levels refining plant from the bottom to top, backwash water discharges housing through water inlet pipe, enters leading portion water collecting basin and continues purifying treatment; Backwash water inlet provides pressurized air by air bump rinse operation source of the gas (roots blower etc.) simultaneously, and air is by the even gas distribution of backwash gas distribution piping 1.3.
Claims (8)
1. the parallel purification of waste water device of high-efficiency double-layer bed, comprise housing, it is characterized in that in housing, being provided with upper and lower two-layer refining plant, levels refining plant includes taper top board, is opened in the water inlet pipe at taper top board center, is arranged at the backwash gas distribution piping below taper top board, catchment piping and blow-down pipe below the porous filter plate below backwash gas distribution piping, the filtrate be arranged on porous filter plate, porous filter plate, and the water inlet pipe of described lower floor refining plant stretches out outside housing through the porous filter plate of upper strata refining plant.
2. the parallel purification of waste water device of a kind of high-efficiency double-layer bed according to claim 1, is characterized in that the taper top board lower surface of upper strata refining plant is provided with some and supports steel pipe, supports that steel pipe bottom is provided with reinforcement gusset.
3. the parallel purification of waste water device of a kind of high-efficiency double-layer bed according to claim 1, is characterized in that the backwash gas distribution piping of upper strata refining plant comprises supervisor, the ring pipe be connected with supervisor and the some arms be distributed on ring pipe.
4. the described parallel purification of waste water device of a kind of high-efficiency double-layer bed according to claim 1, it is characterized in that the backwash gas distribution piping of lower floor's refining plant comprise supervisor, be connected with supervisor and vertically disposed two arms, be responsible for the arm being connected also horizontal-extending.
5. the parallel purification of waste water device of a kind of high-efficiency double-layer bed according to claim 1, it is characterized in that the piping that catchments of upper strata refining plant comprise supervisor and with the octagon circulating line be responsible for use 8 arms of being connected and 8 tube stubs and be spliced into, described circulating line offers gully-hole.
6. the parallel purification of waste water device of a kind of high-efficiency double-layer bed according to claim 1, is characterized in that two inc circulating lines that the piping that catchments of lower floor's refining plant comprises supervisor, is connected with supervisor described circulating line offering gully-hole.
7. the parallel purification of waste water device of a kind of high-efficiency double-layer bed according to claim 1, is characterized in that porous filter plate is circular orifice, is provided with strainer head in hole.
8. the parallel purification of waste water device of a kind of high-efficiency double-layer bed according to claim 1, is characterized in that housing being separately provided with inspection manhole, long waist visor and discharge opening.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510367991.1A CN105036233B (en) | 2015-06-30 | 2015-06-30 | A kind of parallel purification of waste water device of high-efficiency double-layer bed |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510367991.1A CN105036233B (en) | 2015-06-30 | 2015-06-30 | A kind of parallel purification of waste water device of high-efficiency double-layer bed |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105036233A true CN105036233A (en) | 2015-11-11 |
| CN105036233B CN105036233B (en) | 2017-07-04 |
Family
ID=54443285
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510367991.1A Active CN105036233B (en) | 2015-06-30 | 2015-06-30 | A kind of parallel purification of waste water device of high-efficiency double-layer bed |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105036233B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109331527A (en) * | 2018-12-06 | 2019-02-15 | 烟台核信环保设备有限公司 | A kind of tower vacuum filter |
| CN109621538A (en) * | 2018-12-06 | 2019-04-16 | 烟台核信环保设备有限公司 | A kind of tower electro-osmosis vacuum filter |
| CN111035983A (en) * | 2020-01-06 | 2020-04-21 | 同济大学 | A filter device for removing impurities in biological diatomite mixed solution |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103657169A (en) * | 2013-12-04 | 2014-03-26 | 南京中电环保股份有限公司 | Tubular fiber bundle filtering method and apparatus |
| CN204778926U (en) * | 2015-06-30 | 2015-11-18 | 江苏德立环保工程股份有限公司 | Useless water purifier of high -efficient bunk beds parallel |
-
2015
- 2015-06-30 CN CN201510367991.1A patent/CN105036233B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103657169A (en) * | 2013-12-04 | 2014-03-26 | 南京中电环保股份有限公司 | Tubular fiber bundle filtering method and apparatus |
| CN204778926U (en) * | 2015-06-30 | 2015-11-18 | 江苏德立环保工程股份有限公司 | Useless water purifier of high -efficient bunk beds parallel |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109331527A (en) * | 2018-12-06 | 2019-02-15 | 烟台核信环保设备有限公司 | A kind of tower vacuum filter |
| CN109621538A (en) * | 2018-12-06 | 2019-04-16 | 烟台核信环保设备有限公司 | A kind of tower electro-osmosis vacuum filter |
| CN109621538B (en) * | 2018-12-06 | 2024-07-26 | 烟台核信环保设备有限公司 | A tower type electroosmosis vacuum filter |
| CN111035983A (en) * | 2020-01-06 | 2020-04-21 | 同济大学 | A filter device for removing impurities in biological diatomite mixed solution |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105036233B (en) | 2017-07-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104671499B (en) | Smelt composite wastewater advanced treatment separate-recycling method | |
| CN103922506B (en) | Integrated complete equipment for water quality purification treatment | |
| CN101712516B (en) | Device and method for deeply treating mine water for underground coal mine | |
| CN204752397U (en) | Papermaking advanced waste treatment system | |
| CN203890150U (en) | Water-saving water purification device | |
| CN204918252U (en) | Processing system who contains detergent waste water | |
| CN105036233A (en) | High-efficiency double-decker parallel type wastewater purifier | |
| CN204778926U (en) | Useless water purifier of high -efficient bunk beds parallel | |
| CN202246180U (en) | Nanofiltration integrated device for advanced treatment of leachate | |
| CN201880410U (en) | Water distributor for multi-stage high-efficiency fiber filter | |
| CN203768136U (en) | Scale-inhibition and corrosion-inhibition treatment system for gas drainage pump circulating water | |
| CN202390268U (en) | In-situ reuse treatment system for downhole directional drilling machine medium circulation water | |
| CN107376480A (en) | Filter element filtering device for strong brine wastewater | |
| CN102847351A (en) | Novel quartz sand filter | |
| CN207119193U (en) | Filter element filtering device for strong brine wastewater | |
| CN213924384U (en) | System for preparing demineralized water through high-efficiency treatment of mixed surface water | |
| CN201400615Y (en) | Treatment system of wastewater from circulating water | |
| CN215592773U (en) | Integrated rural water supply treatment device | |
| KR101543548B1 (en) | Filtering apparatus and the use of total phosphorus filtering method | |
| CN207845311U (en) | A kind of cutting wastewater processing system | |
| CN102642938A (en) | High-turbidity tower-shaped water purifier | |
| CN208087361U (en) | A kind of Water Treatment equipment | |
| CN207918650U (en) | A kind of wash water cyclic utilization system | |
| CN206915805U (en) | One kind contains golden waste water recycling device system | |
| CN211712846U (en) | Tea treatment product water supply system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB02 | Change of applicant information |
Address after: 214242 Jiangsu city of Wuxi province Xu Yixing City Industrial Zone Applicant after: JIANGSU DELI ENVIRONMENTAL PROTECTION ENGINEERING LIMITED BY SHARE LTD. Address before: 214242 Jiangsu city of Wuxi province Xu Yixing City Industrial Zone Applicant before: Jiangsu De Li Ingegneria Ambientale SRL |
|
| CB02 | Change of applicant information | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200603 Address after: 214242 Jiangsu city of Wuxi province Xu Yixing City Industrial Zone Patentee after: Jiangsu Huatai Ecological Environmental Protection Technology Co.,Ltd. Address before: 214242 Jiangsu city of Wuxi province Xu Yixing City Industrial Zone Patentee before: JIANGSU DELI ENVIRONMENTAL PROTECTION ENGINEERING LIMITED BY SHARE Ltd. |
|
| TR01 | Transfer of patent right |