CN202346852U - Full-automatic integrated backwash water purifying equipment - Google Patents
Full-automatic integrated backwash water purifying equipment Download PDFInfo
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- CN202346852U CN202346852U CN2011204742572U CN201120474257U CN202346852U CN 202346852 U CN202346852 U CN 202346852U CN 2011204742572 U CN2011204742572 U CN 2011204742572U CN 201120474257 U CN201120474257 U CN 201120474257U CN 202346852 U CN202346852 U CN 202346852U
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- recoil
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- pipe
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Abstract
The utility model discloses full-automatic integrated backwash water purifying equipment, which comprises a flocculation reaction area arranged in the middle of an equipment main body, sedimentators arranged on the left and right of the upper part of the equipment, and filters and filtered water tanks, which are arranged on the left and right of the lower part of the equipment. More than one stage of reaction area is arranged in the flocculation reaction area, clapboards are arranged between the reaction areas and provided with overflowing holes, and each stage of reaction area is provided with 3 to 4 layers of grids. Compared with the prior art, the full-automatic integrated backwash water purifying equipment has the advantages that 1, inclined tube sedimentation components are parallelly arranged on the left and right of the upper part of the equipment, water is distributed uniformly, a sedimentation effect is good, and the quality of effluent is stable; 2, gas-water separation components are arranged, a problem that water entraining gas enters a gravity valveless filter is effectively solved, the backwash water amount is greatly reduced and the cleaning is thorough; and 3, equipment integrates grid flocculation reaction, high-efficiency inclined tube sedimentation, gravity valveless automatic backwash filtration and other processes, pipeline arrangement of the whole system is simplified, and operation management intensity and equipment investment are greatly reduced.
Description
Technical field
The utility model relates to a kind of integrated full-automatic recoil water purifying plant.
Background technology
Along with increasing of industrial enterprise, environmental disruption, the surface water pollution mouth becomes seriously, and the regional undressed surface water of industry can not be as tap water and process water; And the water purifier that a few days ago uses all is generally to be the integral type water purifier eighties of last century research and development or that improve a little, mainly contains simple water technology and combines.Drinking water standard has improved in country now; Simultaneously, water purifier of the prior art have that low, the personal water loss of level of automation is big, recoil not thoroughly, the water treatment effect is limited, system pipeline is complicated, bulky, be inconvenient to transport, installation period length and safeguard shortcoming such as inconvenience.Therefore, be necessary to do further improvement and perfect.
The utility model content
The purpose of the utility model aims to provide a kind of simple and reasonable, easy for installation and short construction period, easy and simple to handle, floor space is few, shock-resistant ability is strong integrated full-automatic recoil water purifying plant, to overcome weak point of the prior art.
A kind of integrated full-automatic recoil water purifying plant by this purpose design; Comprise the flocculation reaction district that is arranged at equipment body middle part, be arranged at the settling vessel of its upper side left and right sides and be arranged at the strainer and the filtered water tank of the left and right sides, bottom; Its constitutional features is that said flocculation reaction district is provided with the above reaction zone of one-level; Between each reaction zone dividing plate is set, flowing hole is set on the dividing plate, every order reaction district also is provided with 3-4 layer grid.
Said settling vessel is provided with tube settling assembly precipitable or clarification sewage, and the bottom of settling vessel is provided with bucket and spoil disposal assembly; The water intake end of settling vessel is provided with water distribution zone, and top is provided with water collecting dike, and the water outlet on the settling vessel links to each other with strainer inhalant region pipe through distributing trough, U-shaped pipeline.
Said strainer is a gravity type boat davit valveless water filter device, is disposed with distributing trough, U-shaped pipe, gas-water separation, siphon recoil tube, filter plate assembly and silica sand on the gravity type boat davit valveless water filter device; Distributing trough and U-shaped pipe are positioned at the outside of settling vessel, and are connected with the tube settling assembly; The siphon recoil tube is positioned on the sidewall of equipment body; The siphon recoil tube is provided with the one water route circulation of the common formation of back flushing waterways, water sealed tank and spoil disposal ditch; The spoil disposal ditch links to each other with flocculation reaction shore pipe and sludge from sedimentation tank pipe, and the gas-water separation assembly is arranged on the filter top feed-water end.
Said gas-water separation assembly comprises water separator inner core and water separator urceolus; Wherein the water inlet from the U-shaped pipe is getting into apart from urceolus top 1/2 place's tangential swirl in the cavity of water separator urceolus and water separator inner core formation; The water separator inner diameter of steel flue is identical with back flushing water shoot diameter; Water separator urceolus top is an enclosed construction, and vapor pipe is set, and exhaust outlet is connected in the distributing trough and water seal 50-100mm; The outer tube bottom of water separator is provided with reflector cloth water assembly, and its diameter is than the big 200-300mm of water separator urceolus.
The water-in of said U-shaped pipe links to each other with the settling tank distributing trough; The water outlet of U-shaped pipe links to each other with the gas-water separation assembly; Pipe and outer tube in this U-shaped pipe comprises, current get into from interior pipe, flow to downwards apart from main body base plate 100-150mm place (or being lower than base plate); In the cavity that pipe and outer tube are formed in getting on the current direction, flow into the gas-water separation assembly then.
The water separator inner core links to each other on the water-in of said siphon recoil tube and the gas-water separation assembly; The water outlet of siphon recoil tube links to each other with water sealed tank and back flushing waterways; The siphon recoil tube is made up of pipe in the siphon recoil and siphon recoil outer tube, and current get in the cavity of interior pipe and outer tube composition, upwards flow to apart from the main body top along the 1200-1500mm place; Pipe in current direction gets into down flows into water sealed tank then.
The top of said siphon recoil tube is provided with the automatic siphon recoil and destroys the assembly of recoil, and the assembly of automatic siphon recoil and destruction recoil comprises normally closed solenoid valve and normally open solenoid valve, and normally closed solenoid valve is communicated with the supporting assembly that vacuumizes; Normally open solenoid valve and atmosphere are formed complete control unit with supporting PLC control.
Said siphon recoil tube is provided with automatic liquid level control unit; Automatically the liquid level control unit comprises electromagnetism liquidometer and bypass pipe fitting; The electromagnetism liquidometer is arranged in the by-pass line; By-pass line links to each other with upper end pipe and lower end pipe respectively, lower end pipe installation site 100mm below edge, pipe top in the siphon recoil.By-pass line respectively meets DN15 pipe except that upper and lower ends, and all the other are sealing.The electromagnetism liquid level is counted the stainless steel product.
Said tube settling assembly comprises more than one inclined tube; The diameter of inclined tube is 30mm-50mm, and length is 1000-1200mm, and the material of inclined tube is a PP honeycomb product.
But said equipment body is the body structure of closed or semi-enclosed pressurized, and main equipment is T-shaped, and the plane is a rectangle, width 2500-3200mm; Equipment body is provided with more than one manhole; Also be provided with cat ladder and platform on the equipment body, the material of equipment body, cat ladder and platform is carbon steel product or stainless steel product.
The utility model compared with prior art has the following advantages:
1, technologies such as flocculation reaction, high-efficiency pipe chute deposition, gravity type boat davit valveless water filter and automatic recoil is organically combined; Have that the anti impulsion load ability washes hair by force, in a state of excitement that loss is few, full-automatic back washing, failure rate advantage low, stable and easy and simple to handle,
2, through optimized design of structure, its upper side left and right sides is parallel to be provided with the tube settling assembly, and water distribution is more even, and sedimentation effect is good, stable effluent quality.
3, through optimized design of structure, adopt 4 major parts up and down, each several part is independent, and be implemented in plant and produce, the automobile transportation, field assembly shortens construction period greatly, enhances productivity.
4, the gas-water separation assembly is set, effectively solves the problem of gravity type boat davit valveless water filter device water inlet gas enclosure, reduce the backwash water amount significantly, clean more thorough.
5, through optimization design, supporting SV of siphon downtake and fluid level controller realize that back-purge system PLC controls automatically.
6, it is big effectively to solve the legacy equipment floor space, can reduce setting up of backwash pump, need not extract the clear water of clean water basin simultaneously and make backwash water, can energy-conserving and environment-protective to reach, improve deposition efficiency, reduce the purpose of whole height; And simplify the pipeline configuration of total system, alleviated operational administrative intensity and facility investment widely.
7, can be used for removing that suspended substance promptly reduces turbidity in the water; Materials such as part that can be removed ferrimanganic and colloid also; Delivery turbidity reaches the Drinking Water turbidity index of national regulation, and the process water that is widely used in cities and towns and industrial and mining enterprises is handled, and also can be used for Industrial Wastewater Treatment; And can supporting as required dosing and sterilization equipment and/or PLC system.
Description of drawings
Fig. 1 is embodiment master's TV structure synoptic diagram of the utility model.
Fig. 2 is along A-A direction sectional structure synoptic diagram among Fig. 1.
Fig. 3 is the plan structure synoptic diagram of Fig. 1.
Fig. 4 is the main TV structure synoptic diagram after cat ladder and platform and the equipment body assembling.
Fig. 5 is the left TV structure synoptic diagram of Fig. 4.
Fig. 6 is the main TV structure synoptic diagram of gas-water separation assembly.
Fig. 7 is the main TV structure synoptic diagram of U-shaped pipe assembly.
Fig. 8 is the main TV structure synoptic diagram of siphon recoil tube.
Fig. 9 is the main TV structure synoptic diagram of liquid level control unit.
Among the figure: 1 is equipment body, and 1.1 is manhole, and 1.2 is the spoil disposal ditch, and 1.3 is water sealed tank, and 1.4 are the back flushing waterways, and 2 is the tube settling assembly; 3 is effluent weir, and 4 is settling vessel, 5 water distribution zone, and 6 are the flocculation reaction district, and 7 is grid, and 8 is the sludge from sedimentation tank pipe; 9 is the gas-water separation assembly, and 9.1 is venting port and water seal part, and 9.2 is vapor pipe, and 9.3 is the water separator urceolus, and 9.4 is reflector cloth wet part, and 9.5 is the water separator inner core; 10 is water outlet, and 11 is filtered water tank, and 12 is strainer, and 13 is silica sand, and 14 is filter plate assembly; 15 is distributing trough, and 16 is the U-shaped pipe, and 16.1 is inner core, and 16.2 is urceolus, and 17 are the siphon recoil tube; 17.1 be normally closed solenoid valve, 17.2 is normally open solenoid valve, 17.3 is the liquid level control unit, and 17.31 is last pipe, and 17.32 is lower communicating tube; 17.33 be the electromagnetism liquidometer, 17.34 is common pipe, 17.4 are siphon recoil outer tube, and 17.5 are pipe in the siphon recoil, and 17.6 is the backwashing strength adjustable plate; 18 is dividing plate, and 19 is water inlet pipe, and 20 is the reaction zone shore pipe, and 21 is cat ladder, and 22 is the passageway platform.
Embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is further described.
Referring to Fig. 1-Fig. 9, this integrated full-automatic recoil water purifying plant comprises the flocculation reaction district 6 that is arranged at equipment body 1 middle part, is arranged at the settling vessel 4 of its upper side left and right sides and is arranged at the strainer 12 of the left and right sides, bottom.Flocculation reaction district 6 is provided with the above reaction zone of one-level, and each reaction interval is provided with dividing plate 18, on the dividing plate 18 flowing hole is set, and every order reaction district also is provided with 3-4 layer grid 7.Settling vessel 4 is provided with tube settling assembly 2 precipitable or clarification sewage, and the bottom is provided with bucket and spoil disposal assembly, and water intake end is provided with water distribution zone 5, and top is provided with water collecting dike, and water outlet links to each other with valveless water filter device 12 inhalant region pipes through distributing trough 15, U-shaped pipe 16 roads; Strainer 12 adopts gravity type boat davit valveless water filter device 12, is provided with distributing trough 15, U-shaped pipe 16, gas-water separation, siphon recoil tube 17, filter plate assembly 14 and silica sand 13.Distributing trough 15 and U-shaped pipe 16 are positioned at the outside of settling vessel 4, and are connected with tube settling assembly 2.The siphon downtake is positioned at strainer 12 outsides, is connected with strainer 12 assemblies.The gas-water separation assembly is arranged on the filter chamber top feed-water end.Siphon recoil tube 17 is provided with back flushing waterways 1.4, water sealed tank 1.3 and the 1.2 common formation one water route circulations of spoil disposal ditch; Spoil disposal ditch 1.2 links to each other with flocculation reaction shore pipe 20 and sludge from sedimentation tank pipe 8, and gas-water separation assembly 9 is arranged on the strainer 12 top feed-water ends.
Principle of work of the utility model and technical characteristic:
Be provided with tube settling assembly 2 in the settling vessel 4, hydraulics is significantly improved, and current processing layer stream mode, particles settling not disturbed by current and settling stability is better, the sedimentation distance shortens and the settling time is shorter.Select inclined tube caliber and spacing about about 30-50mm for use, increased desilting area, make the settling vessel 4 with homalographic increase aquifer yield, plant efficiency is greatly enhanced, and equipment volume significantly reduces and saved investment.Tube settler is after 4 operation for some time, and a large amount of sludgd depositions must regularly be discharged settling vessel 4 bottom bucket mud in the bucket of bottom.Sludge discharging period is relevant with raw water quality and institute's with medicament, specifically can regulate according to the day-to-day operation situation.Raw water turbidity is when 2000ppm is following generally speaking, and settling vessel 4 delivery turbidities can be less than 15ppm.
Gravity type boat davit valveless water filter device to settling vessel 4 water outlets carry out depth type filtration and handle, adopt advanced power fully automatic operation mode.Filtering process: the clear water after deposition or clarification; Get into the siphon upcast through distributing trough 15 and U-shaped pipe; Be assigned to equably in the filter material layer by the water distribution plate washer in the top cover, water filters through filtering layer from top to bottom again, and filter back water is collected the back by slight drag water distribution assembly and got into the clear water zone storage; When water level rose to rising pipe, filter back water flowed out through water leg.The backwash flow process: the filter tank operation is relatively cleaner at the beginning; Filtering layer surface particles impurity increases gradually along with the passing of working time, and the syringe pipe loss also increases thereupon, and water level will slowly raise along the siphon upcast; When water level rises to certain altitude; When arriving the backwash start-up point, vacuumize assembly through supporting vacuum pump or water-jet and extract the air in the U trap out, make it form the siphon backwash.
When just put into operation in the filter tank, filter material layer is cleaning, but after running to the regular hour, owing to increasing gradually of solid particle polluter in the filter material layer; Therefore the syringe pipe loss also increases thereupon, and water level just slowly raises along the siphon upcast, after the syringe pipe loss increases to a certain degree, makes the water level in the siphon upcast be elevated to the liquid level switch position; Liquid level switch floats, and PLC obtains starting backwashing procedures behind the signal, and extraction valve is opened in control; The open vacuum pump is bled, and makes U trap form vacuum, and the water in the siphon upcast is just crossed the pipe top in a large number; Fall along the siphon downtake, at this moment, just begun backwash process.
Flushing is through 5min, and extraction valve and vacuum pump are closed in PLC control, open intake valve, and siphon promptly is destroyed, and flushing process finishes, and filters to begin again.This structure can reduce setting up of backwash pump in traditional water purifying plant; Reduced energy consumption; Need not extract simultaneously the clear water of clean water basin and make backwash water; Reduced personal water loss, the pipeline configuration of system integration designs simplification total system has alleviated operational administrative intensity and facility investment widely.Through setting up gas-water separation assembly 9, it is not thorough to have solved the recoil that gravity type boat davit valveless water filter device water inlet gas enclosure brings, the shortcoming that personal water loss is bigger.Back flushing is to carry out automatically according to the chocking-up degree of filtering layer, realizes the PLC ctc, has reduced the error of manual operation, can be implemented in operation under the operatorless state.And have following characteristics 1, detect the syringe pipe loss with liquid level switch; 2, the suction of vacuum pump is bigger, can form siphon in the short period of time; 3, direct switch electromagnetic valve of PLC and vacuum pump can form backwash or stop.
Claims (10)
1. integrated full-automatic recoil water purifying plant; Comprise the flocculation reaction district (6) that is arranged at equipment body (1) middle part, be arranged at the settling vessel (4) of its upper side left and right sides and be arranged at the strainer (12) and the filtered water tank (11) of the left and right sides, bottom; It is characterized in that said flocculation reaction district (6) is provided with the above reaction zone of one-level; Dividing plate (18) is set between each reaction zone, and dividing plate is provided with flowing hole on (18), and every order reaction district also is provided with 3-4 layer grid (7).
2. integrated full-automatic recoil water purifying plant according to claim 1 is characterized in that said settling vessel is provided with tube settling assembly (2) precipitable or clarification sewage, and the bottom of settling vessel is provided with bucket and spoil disposal assembly (8); The water intake end of settling vessel is provided with water distribution zone (5), and top is provided with water collecting dike (3), and the water outlet on the settling vessel (10) links to each other with strainer (12) inhalant region pipe through distributing trough (15), U-shaped pipeline (16).
3. integrated full-automatic recoil water purifying plant according to claim 2; It is characterized in that said strainer (12) is a gravity type boat davit valveless water filter device, is disposed with distributing trough (15), U-shaped pipe (16), gas-water separation (9), siphon recoil tube (17), filter plate assembly (14) and silica sand (13) on the gravity type boat davit valveless water filter device; Distributing trough (15) and U-shaped pipe (16) are positioned at the outside of settling vessel, and are connected with the tube settling assembly; Siphon recoil tube (17) is positioned on the sidewall of equipment body (1); Siphon recoil tube (17) is provided with back flushing waterways (1.4), water sealed tank (1.3) and spoil disposal ditch (1.2) and constitutes water route circulation jointly; Spoil disposal ditch (1.2) links to each other with flocculation reaction shore pipe (20) and sludge from sedimentation tank pipe (8), and gas-water separation assembly (9) is arranged on the feed-water end of strainer (12) top.
4. integrated full-automatic recoil water purifying plant according to claim 3; It is characterized in that said gas-water separation assembly (9) comprises water separator inner core (9.5), water separator urceolus (9.3), venting port and water seal part (9.1); The diameter of water separator inner core (9.5) is identical with the diameter of back flushing water shoot; Water separator urceolus (9.3) top is an enclosed construction; And be provided with vapor pipe (9.2), water separator urceolus (9.3) bottom is provided with reflector cloth wet part (9.4), and the diameter of reflector cloth wet part (9.4) is than the big 200-300mm of water separator urceolus (9.3).
5. according to claim 3 or 4 described integrated full-automatic recoil water purifying plants; The water-in that it is characterized in that said U-shaped pipe (16) links to each other with settling tank distributing trough (15); The water outlet of U-shaped pipe (16) links to each other with gas-water separation assembly (9), and this U-shaped pipe (16) comprises interior pipe (16.1) and outer tube (16.2).
6. integrated full-automatic recoil water purifying plant according to claim 5; The water-in that it is characterized in that said siphon recoil tube (17) links to each other with the last water separator inner core (9.5) of gas-water separation assembly (9); The water outlet of siphon recoil tube (17) links to each other with water sealed tank (1.3) and back flushing waterways (1.4), and the siphon recoil tube is made up of pipe (17.5) and siphon recoil outer tube (17.4) in the siphon recoil.
7. integrated full-automatic recoil water purifying plant according to claim 6; The top that it is characterized in that said siphon recoil tube (17) is provided with the automatic siphon recoil and destroys the assembly that recoils; The assembly of automatic siphon recoil and destruction recoil comprises normally closed solenoid valve (17.1) and normally open solenoid valve (17.2), and normally closed solenoid valve (17.1) is communicated with the supporting assembly that vacuumizes; Normally open solenoid valve (17.2) and atmosphere are formed complete control unit with supporting PLC control.
8. integrated full-automatic recoil water purifying plant according to claim 7; It is characterized in that said siphon recoil tube (17) is provided with automatic liquid level control unit; Automatically the liquid level control unit comprises electromagnetism liquidometer (17.33) and bypass pipe fitting (17.34); Electromagnetism liquidometer (17.33) is arranged in the by-pass line (17.34), and by-pass line (17.34) links to each other with upper end pipe (17.31) and lower end pipe (17.32) respectively.
9. integrated full-automatic recoil water purifying plant according to claim 8 is characterized in that said tube settling assembly (2) comprises more than one inclined tube; The diameter of inclined tube is 30mm-50mm, and length is 1000-1200mm, and the material of inclined tube is a PP honeycomb product.
10. integrated full-automatic recoil water purifying plant according to claim 9, it is characterized in that said equipment body (1) but be the body structure of closed or semi-enclosed pressurized, main equipment is T-shaped, the plane is a rectangle, width 2500-3200mm; Equipment body is provided with more than one manhole (1.1); Also be provided with cat ladder (21) and platform (22) on the equipment body, the material of equipment body, cat ladder and platform is carbon steel product or stainless steel product.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204742572U CN202346852U (en) | 2011-11-24 | 2011-11-24 | Full-automatic integrated backwash water purifying equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204742572U CN202346852U (en) | 2011-11-24 | 2011-11-24 | Full-automatic integrated backwash water purifying equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202346852U true CN202346852U (en) | 2012-07-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204742572U Expired - Lifetime CN202346852U (en) | 2011-11-24 | 2011-11-24 | Full-automatic integrated backwash water purifying equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202346852U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103332806A (en) * | 2013-06-24 | 2013-10-02 | 宜兴市全洲水工设备厂 | Automatic water processing system |
| CN105110507A (en) * | 2015-09-01 | 2015-12-02 | 中冶建筑研究总院有限公司 | Self-cleaning-floatation-filtration treatment facility |
| CN106348496A (en) * | 2016-11-15 | 2017-01-25 | 济南山源电力设备有限公司 | Integrated water purifier |
| CN111908656A (en) * | 2020-07-23 | 2020-11-10 | 南方泵业智水（杭州）科技有限公司 | Integrated water purification equipment and water purification process thereof |
| CN115477410A (en) * | 2021-06-15 | 2022-12-16 | 青岛鑫源环保集团有限公司 | Integrated water purifying equipment |
-
2011
- 2011-11-24 CN CN2011204742572U patent/CN202346852U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103332806A (en) * | 2013-06-24 | 2013-10-02 | 宜兴市全洲水工设备厂 | Automatic water processing system |
| CN105110507A (en) * | 2015-09-01 | 2015-12-02 | 中冶建筑研究总院有限公司 | Self-cleaning-floatation-filtration treatment facility |
| CN106348496A (en) * | 2016-11-15 | 2017-01-25 | 济南山源电力设备有限公司 | Integrated water purifier |
| CN111908656A (en) * | 2020-07-23 | 2020-11-10 | 南方泵业智水（杭州）科技有限公司 | Integrated water purification equipment and water purification process thereof |
| CN115477410A (en) * | 2021-06-15 | 2022-12-16 | 青岛鑫源环保集团有限公司 | Integrated water purifying equipment |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 528000 Yangmei West District, Cangjiang Industrial Park, Gaoming District, Foshan City, Guangdong Province Patentee after: Guangdong xintailong Environmental Protection Group Co., Ltd Address before: 528000 Yangmei West District, Cangjiang Industrial Park, Gaoming District, Foshan City, Guangdong Province Patentee before: FOSHAN XINTAILONG ENVIRONMENTAL PROTECTION EQUIPMENT MANUFACTURING Co.,Ltd. |
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| CP01 | Change in the name or title of a patent holder | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120725 |
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| CX01 | Expiry of patent term |