CN201809212U - Magnetic cyclone clarifier - Google Patents
Magnetic cyclone clarifier Download PDFInfo
- Publication number
- CN201809212U CN201809212U CN2010205174346U CN201020517434U CN201809212U CN 201809212 U CN201809212 U CN 201809212U CN 2010205174346 U CN2010205174346 U CN 2010205174346U CN 201020517434 U CN201020517434 U CN 201020517434U CN 201809212 U CN201809212 U CN 201809212U
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- China
- Prior art keywords
- magnetic rotation
- magnetic
- swash plate
- cyclone reaction
- cyclone
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Abstract
The utility model provides a magnetic cyclone clarifier, which is a wastewater purification treatment device integrating processes such as chemical magnetic coagulation, cohesion, cyclone reaction settlement, tilted plate clarification and the like. The magnetic cyclone clarifier comprises a chemical feeding device, a water inlet pipe, a permanent magnetic flocculator, a cyclone reaction settling zone, a guide channel, a tilted plate clarifying zone, an overflow channel, a water outlet channel and a water outlet pipe. After chemicals are fed in wastewater, the wastewater flows into the cyclone reaction settling zone through the pipe type permanent magnetic flocculator, magnetic oxidation substances and nonmagnetic oxidation substances are flocculated or gathered under the action of chemical magnetism to form large grains, the large grains are settled rapidly under the action of cyclone, and formed small grains are purified by the tilted plate clarifying zone. The magnetic cyclone clarifier is simple in structure, convenient in operation, small in occupied floor area and high in treatment efficiency.
Description
Technical field
The utility model relates to a kind of magnetic rotation stream settler, relates in particular to a kind of integrated equipment that integrates multinomial technology such as precipitation, clarification that is used for to water treatment, sewage disposal, oily(waste)water processing, turbid circulating water purifying treatment.
Background technology
At present, in the water supply and drainage treatment technology, technology such as coagulating sedimentation commonly used, clarification separations, these known technologies mostly are the blocking technology, and its shortcoming is that floor space is big, and investment is big, and complex operation, management are inconvenient, and the working cost height, environment is poor, efficient is low etc.So developing the precipitation technology that a kind of volume is little, easy and simple to handle, processing efficiency is high again integrated technology replaces this conventional elements processing is problem demanding prompt solution.
Summary of the invention
The purpose of this utility model is to provide a kind of integrated purification of waste water treatment facility of diversification technology that integrates technologies such as medicine magnetic-coagulation, cohesion, cyclone reaction precipitation, swash plate clarification, replaces the conventional elements treatment technology.
Magnetic rotation stream settler described in the utility model comprises, chemicals dosing plant, water inlet pipe, permanent magnetism flocculator, cyclone reaction settling region, swash plate settling section, overflow groove, effluent trough, rising pipe, it is characterized in that, described cyclone sediment district includes whirl cylinder, wherein said water inlet pipe is connected with described whirl cylinder, and the water inlet pipe that connects whirl cylinder is provided with tubular type permanent magnetism flocculator and chemical feed pipe, and chemical feed pipe is connected with chemicals dosing plant, and described chemicals dosing plant is joined in addition; Described chemical feed pipe be arranged at water inlet pipe by an end of the mouth of pipe, tubular type permanent magnetism flocculator is arranged on the water inlet pipe between whirl cylinder and the chemical feed pipe; The composite waste of described permanent magnetism flocculator after to dosing done magnetic treatment, forms the macrobead floss of ferromegnetism and nonferromagnetic; The cyclone reaction settling region is arranged at the center of entire equipment, it includes water-in, whirl cylinder, first sludge bucket, center upflow tube, mud discharging mouth, wherein centre, cyclone reaction settling region is the center upflow tube, periphery is a whirl cylinder, cone-shaped body that is connected with the whirl cylinder bottom or truncated cone body are first sludge bucket, the first sludge bucket lower end connects first mud discharging mouth, is connected with first shore pipe; The swash plate settling section is arranged at cyclone reaction settling region periphery, it is connected by diversion trench with the cyclone reaction settling region, the swash plate settling section comprises swash plate district, clear water zone, buffer zone, second sludge bucket, second mud discharging mouth, wherein clear water zone is positioned at top, swash plate district, buffer zone is between the swash plate district and second sludge bucket, there is second mud discharging mouth second sludge bucket lower end, is connected with second shore pipe; Overflow groove is arranged at swash plate settling section top, overflow groove communicates with effluent trough, behind the long-pending Qing Dynasty of clear water zone water, spill in the overflow groove, enter effluent trough by overflow groove, have water outlet in the effluent trough, be connected, the clear water that comes out from overflow groove with rising pipe, by effluent trough, water outlet, rising pipe, be recovered then.
Above-mentioned magnetic rotation stream settler can be that rectangle, circle or other are convenient to the shape implemented arbitrarily.
First sludge bucket and second sludge bucket of above-mentioned magnetic rotation stream settler can be taper, truncated cone shape or other structure that can realize.
The permanent magnetism flocculator of above-mentioned magnetic rotation stream settler can be tubular type or other structure that can realize.
Adopt the advantage of the technical program to be: described magnetic rotation stream settler integrates multinomial technology such as medicine magnetic-coagulation, cyclone reaction precipitation, swash plate clarification, multibuchet spoil disposal, and is simple in structure, easy to operate, floor space is little, processing efficiency is high.
Description of drawings
Fig. 1 is a magnetic rotation stream settler equipment synoptic diagram of the present utility model.
Embodiment
In order better to understand the purpose of this utility model, structure and function, below in conjunction with the do detailed description of accompanying drawing to an embodiment of magnetic rotation stream settler of the present utility model:
Magnetic rotation stream settler as shown in Figure 1 comprises chemicals dosing plant 18, water inlet pipe 1, chemical feed pipe 2, permanent magnetism flocculator 3, cyclone reaction settling region, swash plate settling section, overflow groove 13, effluent trough 14, rising pipe 17.Water inlet pipe 1 is connected with whirl cylinder 5, and on the water inlet pipe 1 that connects whirl cylinder 5, chemical feed pipe 2 and permanent magnetism flocculator 3 are set, composite waste after 3 pairs of dosings of described permanent magnetism flocculator is done magnetic treatment, effect by medicine magnetic makes ferromagnetic oxide matter and nonmagnetic oxide matter produce flocculation or gathering, forms larger particles.The cyclone reaction settling region is arranged at the center of whole magnetic rotation stream settler, and it includes water-in 4, whirl cylinder 5, first sludge bucket 6, center upflow tube 7, first mud discharging mouth 8.Wherein, centre, cyclone reaction settling region is a center upflow tube 7, and periphery is a whirl cylinder 5, and the whirl cylinder bottom is first sludge bucket 6, and described first sludge bucket 6 lower ends form first mud discharging mouth 8, are connected with first shore pipe.The swash plate settling section is a rectangle form pool, is positioned at cyclone reaction settling region periphery, and it is connected by diversion trench 9 with the cyclone reaction settling region, and the swash plate settling section comprises buffer zone 10, swash plate district 11, clear water zone 12, second sludge bucket 15, second mud discharging mouth 16.Wherein, clear water zone 12 is positioned at 11 tops, swash plate district, and buffer zone 10 is positioned at the top of 11 belows, swash plate district and second sludge bucket 15, and there is second mud discharging mouth 16 second sludge bucket, 15 lower ends, are connected with second shore pipe.Overflow groove 13 is arranged at swash plate settling section top, overflow groove 13 communicates with effluent trough 14, behind clear water zone 12 long-pending Qing Dynasty water, spill in the overflow groove 13, enter effluent trough 14 by overflow groove 13, have water outlet in the effluent trough 14, be connected, the clear water that comes out from overflow groove 13 with rising pipe 17, by effluent trough 14, rising pipe 17, be recovered then.
Here, magnetic rotation stream settler can be rectangle, circle or other structure formation of being convenient to implement; First sludge bucket and second sludge bucket of magnetic rotation stream settler can be taper, truncated cone shape or other Any shape that can realize; The permanent magnetism flocculator of magnetic rotation stream settler can be tubular type or other any structure that can realize.
During concrete operations, waste water after the dosing passes through permanent magnetism flocculator 3 through water inlet pipe 1, under the effect of medicine magnetic, ferromagnetic oxide matter in the waste water and nonmagnetic oxide matter produce flocculation, be gathered into big particulate matter, enter whirl cylinder 5 via water-in 4 then, be subjected to the effect of centrifugal force and gravity, the macrobead thing is settled down to rapidly in first sludge bucket 6, and discharges by first shore pipe.The waste water that contains the fine particle suspended substance is discharged by center upflow tube 7, enter the swash plate settling section via diversion trench 9 then, the clear water that obtains after handling through swash plate district 11 enters clear water zone 12, enters effluent trough 14 by overflow groove 13, discharge through rising pipe 17, be recovered then.Be settled down to second sludge bucket 15 by the throw out after 11 processing of swash plate district, discharge through second mud discharging mouth 16.
The above only is a preferred implementation of the present utility model; should be pointed out that for the person of ordinary skill of the art, under the prerequisite that does not break away from the utility model principle; can also make some modification and improvement, these also should be considered as belonging to protection domain of the present utility model.
Claims (11)
1. settler is flowed in a magnetic rotation, it comprises water inlet pipe (1), cyclone reaction settling region, diversion trench (9), swash plate settling section, overflow groove (13), effluent trough (14), rising pipe (17), it is characterized in that wherein said water inlet pipe (1) is connected with described cyclone reaction settling region; Described cyclone reaction settling region is arranged at this magnetic rotation stream settler central position; Described swash plate settling section is arranged at described cyclone reaction settling region periphery, and is connected by diversion trench (9) with described cyclone reaction settling region; Described overflow groove (13) is arranged at the top of described swash plate settling section; Described effluent trough (14) one ends are connected with described overflow groove (13), and the other end is connected in the described rising pipe (17) of stating.
2. magnetic rotation stream settler as claimed in claim 1 is characterized in that described cyclone reaction district includes whirl cylinder (5), and wherein said water inlet pipe (1) is connected with described whirl cylinder (5).
3. magnetic rotation stream settler as claimed in claim 1 or 2 is characterized in that also include chemicals dosing plant (18) and chemical feed pipe (2), described chemicals dosing plant (18) is connected with chemical feed pipe (2), and chemical feed pipe (2) is arranged on the described water inlet pipe (1).
4. magnetic rotation as claimed in claim 1 or 2 stream settler is characterized in that, also includes permanent magnetism flocculator (3), and described permanent magnetism flocculator (3) is arranged on the water inlet pipe (10) between chemical feed pipe (2) and the whirl cylinder (5).
5. magnetic rotation stream settler as claimed in claim 1, it is characterized in that, described cyclone reaction zone center position is center upflow tube (7), periphery is the cyclone reaction settling region, the bottom is first sludge bucket (6), described first sludge bucket (6) lower end forms first mud discharging mouth (8), is connected with first shore pipe.
6. magnetic rotation stream settler as claimed in claim 1 is characterized in that described swash plate settling section comprises clear water zone (12), swash plate district (11), buffer zone (10), second sludge bucket (15), second mud discharging mouth (16) from top to bottom successively.
7. as claim 1 or 6 described magnetic rotation stream settlers, it is characterized in that described swash plate settling section is a rectangle.
8. as claim 1 or 6 described magnetic rotation stream settlers, it is characterized in that described swash plate settling section is circular.
9. as claim 1 or 5 described magnetic rotation stream settlers, it is characterized in that described cyclone reaction settling region is a circular configuration.
10. magnetic rotation stream settler as claimed in claim 1 is characterized in that described first sludge bucket (6) and second sludge bucket (15) are taper.
11. magnetic rotation stream settler as claimed in claim 1 is characterized in that described first sludge bucket (6) and second sludge bucket (15) are truncated cone shape.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010205174346U CN201809212U (en) | 2010-09-01 | 2010-09-01 | Magnetic cyclone clarifier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010205174346U CN201809212U (en) | 2010-09-01 | 2010-09-01 | Magnetic cyclone clarifier |
Publications (1)
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CN201809212U true CN201809212U (en) | 2011-04-27 |
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CN2010205174346U Expired - Lifetime CN201809212U (en) | 2010-09-01 | 2010-09-01 | Magnetic cyclone clarifier |
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Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102372353A (en) * | 2011-08-03 | 2012-03-14 | 东华大学 | Spiral-flow type crystal phosphorous removal reactor |
CN102755768A (en) * | 2012-07-30 | 2012-10-31 | 葛洲坝集团第一工程有限公司 | Sludge treatment device used at pressure type pumping and drainage outlet |
CN102874910A (en) * | 2012-10-15 | 2013-01-16 | 华东理工大学 | Coagulation-precipitation integrated treatment method and device |
CN104402087A (en) * | 2014-11-28 | 2015-03-11 | 中冶东方工程技术有限公司 | Magnetic cyclone filtering device |
CN105668740A (en) * | 2016-03-17 | 2016-06-15 | 绵阳科勤环保科技有限公司 | Integrated sand washing waste water reuse device |
CN106219858A (en) * | 2016-08-02 | 2016-12-14 | 山东科技大学 | Portable magnetic wrench of a force system settler |
CN107032463A (en) * | 2017-04-25 | 2017-08-11 | 煤科集团杭州环保研究院有限公司 | A kind of municipal treatment device for overflow sewage and method |
CN110342608A (en) * | 2019-05-27 | 2019-10-18 | 安徽理工大学 | A kind of compound concentration and settlement device of cyclone classification formula |
CN115054949A (en) * | 2022-05-26 | 2022-09-16 | 肖丹丹 | Filtration and separation device for environment-friendly manufacturing industrial sewage |
-
2010
- 2010-09-01 CN CN2010205174346U patent/CN201809212U/en not_active Expired - Lifetime
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102372353A (en) * | 2011-08-03 | 2012-03-14 | 东华大学 | Spiral-flow type crystal phosphorous removal reactor |
CN102755768B (en) * | 2012-07-30 | 2015-06-17 | 葛洲坝集团第一工程有限公司 | Sludge treatment device used at pressure type pumping and drainage outlet |
CN102755768A (en) * | 2012-07-30 | 2012-10-31 | 葛洲坝集团第一工程有限公司 | Sludge treatment device used at pressure type pumping and drainage outlet |
CN102874910A (en) * | 2012-10-15 | 2013-01-16 | 华东理工大学 | Coagulation-precipitation integrated treatment method and device |
CN102874910B (en) * | 2012-10-15 | 2014-05-07 | 华东理工大学 | Coagulation-precipitation integrated treatment method and device |
CN104402087B (en) * | 2014-11-28 | 2016-05-04 | 中冶东方工程技术有限公司 | A kind of magnetic eddy filter |
CN104402087A (en) * | 2014-11-28 | 2015-03-11 | 中冶东方工程技术有限公司 | Magnetic cyclone filtering device |
CN105668740A (en) * | 2016-03-17 | 2016-06-15 | 绵阳科勤环保科技有限公司 | Integrated sand washing waste water reuse device |
CN106219858A (en) * | 2016-08-02 | 2016-12-14 | 山东科技大学 | Portable magnetic wrench of a force system settler |
CN107032463A (en) * | 2017-04-25 | 2017-08-11 | 煤科集团杭州环保研究院有限公司 | A kind of municipal treatment device for overflow sewage and method |
CN107032463B (en) * | 2017-04-25 | 2019-05-10 | 煤科集团杭州环保研究院有限公司 | A kind of municipal administration treatment device for overflow sewage and method |
CN110342608A (en) * | 2019-05-27 | 2019-10-18 | 安徽理工大学 | A kind of compound concentration and settlement device of cyclone classification formula |
CN110342608B (en) * | 2019-05-27 | 2022-03-08 | 安徽理工大学 | Cyclone grading type composite concentration sedimentation device |
CN115054949A (en) * | 2022-05-26 | 2022-09-16 | 肖丹丹 | Filtration and separation device for environment-friendly manufacturing industrial sewage |
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Granted publication date: 20110427 |
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CX01 | Expiry of patent term |