CN202740880U - Floating bed filter - Google Patents

Floating bed filter Download PDF

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Publication number
CN202740880U
CN202740880U CN 201220349166 CN201220349166U CN202740880U CN 202740880 U CN202740880 U CN 202740880U CN 201220349166 CN201220349166 CN 201220349166 CN 201220349166 U CN201220349166 U CN 201220349166U CN 202740880 U CN202740880 U CN 202740880U
Authority
CN
China
Prior art keywords
floating bed
bed filter
floating
center
cleaning device
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
Application number
CN 201220349166
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Chinese (zh)
Inventor
刘广西
冯友龙
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
YANTAI SUNNY HEXING ENVIRONMENT PROTECTION EQUIPMENT CO Ltd
Original Assignee
YANTAI SUNNY HEXING ENVIRONMENT PROTECTION EQUIPMENT CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by YANTAI SUNNY HEXING ENVIRONMENT PROTECTION EQUIPMENT CO Ltd filed Critical YANTAI SUNNY HEXING ENVIRONMENT PROTECTION EQUIPMENT CO Ltd
Priority to CN 201220349166 priority Critical patent/CN202740880U/en
Application granted granted Critical
Publication of CN202740880U publication Critical patent/CN202740880U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a floating bed filter relating to the field of reclaimed water fine micro-processing. The utility model aims at solving the difficult problem of reclaimed water fine micro-processing and providing the floating bed filter reliable in performance, low in energy consumption and low in operation and maintenance costs. A casing body is positioned at the outer end of the floating bed filter, a material distributing device is positioned at the top end of the inner part of the casing body, and a washing device is positioned on the upper part in the casing body. The floating bed filter is characterized in that a fine micro-filtering device is arranged in the casing body; the fine micro-filtering device comprises a center clarifier and an annular floating net; the center clarifier is fixed at the center of the top end in the casing body; and the annular floating net is distributed on the washing device in an annular shape. By utilizing the floating bed filter, the use ratio of domestic and industrial water can be greatly improved. The floating bed filter is not provided with a drive part and is low in energy consumption and low in operation and maintenance costs.

Description

A kind of floating bed filter
Technical field
The utility model relates to a kind of floating bed filter, relates to the trickle process field of middle crystal.
Background technology
China is one of country of the in the world serious scarcity of water resource, and it is extremely uneven to distribute, and the water yield is in world's middle and lower reaches level per capita, and the random emission problem of sewage has further polluted near water source simultaneously.The thin filtering technique of middle crystal can make municipal sewage, mine ore dressing wastewater reuse, greatly improves the utilization rate of life and water for industrial use, can effectively solve sewage discharge pollution and water resource and lack a dual difficult problem of bringing.
Common filter plant can only be controlled at middle water solid content 300-500ppm (ppm is the abbreviation of English parts per million, represents 1,000,000/(several)), and traditional microfilter device cost and operation expense are very high, can't large-scale promotion.
The utility model content
The difficult problem of the trickle processing of crystal during the purpose of this utility model is to solve.A kind of dependable performance is provided, and energy consumption is low, the floating bed filter that operation expense is low.
The technical scheme that the utility model solves the problems of the technologies described above is as follows:
A kind of floating bed filter, comprise housing, distribution device, cleaning device, housing is positioned at the outer end of floating bed filter, distribution device is positioned at the top of enclosure interior, cleaning device is positioned at the top of housing, it is characterized in that: described enclosure interior is provided with meticulous microfilter device, and described meticulous microfilter device comprises center clarifier, the floating net of annular, described center clarifier is fixed on the center on enclosure interior top, and the floating net of described annular is distributed on the cleaning device ringwise.
The beneficial effects of the utility model are: the difficult problem of the trickle processing of crystal during the utility model solves, can greatly improve the utilization rate of life and water for industrial use, and there is not driver part, energy consumption is low, and operation expense is low.
Further, described cleaning device is water flushing device or gas flushing device.
Further, described cleaning device comprises flushing line and spray equipment.
The beneficial effect of above-mentioned further improvement project is: more effective meticulous microfilter device is cleaned.Spray equipment is for device provides wide-angle vaporific backwash hydraulic pressure, makes the floating bed Rapid Expansion and the flocculation particle of the floating bed that broken through is washed.
Further, need to add filter medium in the process of work, described filter medium is low density polyethylene (LDPE) particle or granules of polystyrene.
The beneficial effect of above-mentioned further improvement project is: form floating bed in the process of work, very effectively capture the fine particle that rises with material in the clarifier, thereby form fine filtering.
Further, described distribution device, cleaning device, meticulous microfilter device are fixed on cell body with hang and support.
The beneficial effect of above-mentioned further improvement project is: convenient maintenance to equipment.
Further, the floating net material of described annular is 304 or the 316L screen cloth.
Description of drawings
Fig. 1 is front view of the present utility model;
Fig. 2 is top view of the present utility model;
Fig. 3 is process chart of the present utility model.
In the accompanying drawing, the list of parts of label representative is as follows:
1, housing, 2, distribution device, 3, cleaning device, 4, meticulous microfilter device, 5, cell body, 6, cell body supports, 7, crane span structure, 8, guardrail, 9, overflow passage, 10, discharge pipelines, 11, charge pipe, 12, degree of depth material distribution cartridge, 13, flushing line, 14, spray equipment, 15, center clarifier, 16, floating bed, 17, the floating net of annular, 18, flocculant pipe, 19, overflow water, 20, backwashing water.
The specific embodiment
Below in conjunction with accompanying drawing principle of the present utility model and feature are described, institute gives an actual example and only is used for explaining the utility model, is not be used to limiting scope of the present utility model.
In the present embodiment, the floating bed filter comprises housing 1; Distribution device 2; Cleaning device 3; Meticulous microfilter device 4.The housing 1 of telling comprises slurries cell body 5, cell body support 6, crane span structure 7, guardrail 8, overflow passage 9, discharge pipelines 10.Distribution device 2 comprises 12 of charge pipes 11, flocculant pipeline 18, degree of depth material distribution cartridge; Cleaning device 3 comprises flushing line 13 and spray equipment 14.Meticulous microfilter device 4 comprises center clarifier 15, the floating net 17 of annular.Cell body 5 is fixed on the cell body support 6, and the first half of cell body 5 is cylinder, and Lower Half is cone.The bottom that cell body 5 tops are equipped with crane span structure 7, guardrail 8 and cell body 5 is equipped with discharge duct 10, and the top center of cell body 5 is hung with degree of depth material distribution cartridge 12.Charge pipe 11, flocculant pipe 18 are positioned at the upper end of cell body 5, charge pipe 11 is linked degree of depth material distribution cartridge interior 12, flocculant pipe 18 is connected in degree of depth material distribution cartridge 12 and the charge pipe 11, and the center of degree of depth material distribution cartridge 12 is fixed with center clarifier 15, and the top of cell body 5 inner side edges is equipped with overflow pipe 9.Under overflow pipe 9, the floating net 17 of annular is installed between deep material distribution cartridge 12 and the cell body 5, the floating net 17 of annular is to have cleaning device 3, and cleaning device 3 comprises flushing line 13 and spray equipment 14, and spray equipment 14 is installed on the flushing line 13.
Distribution device 2 adds degree of depth material distribution cartridge 12 with original slurry by charge pipe 11, and flocculant pipe 18 is simultaneously to charge pipe 11 and the 12 interior interpolations of degree of depth distribution barrel, so that flocculant can fully mix with slurries and flocculate.Degree of depth material distribution cartridge 12 is peeled off fed slurry and supernatant liquid, and material is directly added cell body 5 middle and lower parts, reserves enough rising spaces.
In the meticulous microfilter device 4, center clarifier 15 is fixed on degree of depth material distribution cartridge 12 centers by crane span structure, and low density polyethylene (LDPE) or granules of polystyrene utilize the floating net 17 of Dual-layer annular, and are distributed on wherein; After slurries after the flocculation enter material distribution cartridge; rely on the self gravitation effect and with the interaction of center clarifier 15; larger particles is sedimentation downwards rapidly; along with liquid level constantly raises; slurries with fine particle upwards push low-density particles, form floating bed 16, and clarified solution is upwards raised by intergranular slit smoothly; particle is blocked in the floating bed bottom, and the part particle can be filled in the middle of the floating bed.
Cleaning device 3 is positioned at about 150-200mm place, floating bed below, utilize 14 pairs of floating beds of spray equipment 16 to carry out vaporific backwash, under hydraulic pressure or gas pressure, floating bed 16 expansions, broken through the flocculant particle of floating bed 16 by the floating bed 16 downward sedimentations of expansion, thereby reach the regeneration of floating bed 16, recover its water penetration.
In operating process, in case floating bed 16 is broken or degree of depth material distribution cartridge 12 in certain altitude to occur poor with cell body 5 interior solution level, the floating bed of this moment 16 is stopped up by fine particle, should be immediately floating bed 16 be cleaned in the feed situation not interrupting; General available overflow water directly washes, and makes floating bed 16 Rapid Expansion that low-density particles forms and the flocculation particle of the floating bed 16 that broken through is washed; Can regularly wash by field condition in the practical application; To again recover the water penetration of floating bed 16 after the flushing and repeat said process, and can reach rapidly high clarity, and, even be lower than 20ppm generally at 50ppm once, recycled water can reuse or use as him.
Filter medium can be low density polyethylene (LDPE) or granules of polystyrene, and shape generally is diameter 5mm toroidal.
The above only is preferred embodiment of the present utility model, and is in order to limit the utility model, not all within spirit of the present utility model and principle, any modification of doing, is equal to replacement, improvement etc., all should be included within the protection domain of the present utility model.

Claims (6)

1. floating bed filter, comprise housing, distribution device, cleaning device, distribution device is positioned at the top of enclosure interior, cleaning device is positioned at the top of housing, it is characterized in that: described enclosure interior is provided with meticulous microfilter device, described meticulous microfilter device comprises center clarifier, the floating net of annular, and described center clarifier is fixed on the center on enclosure interior top, and the floating net of described annular is distributed on the cleaning device ringwise.
2. floating bed filter according to claim 1, it is characterized in that: described cleaning device is water flushing device or gas flushing device.
3. floating bed filter according to claim 1 and 2, it is characterized in that: described cleaning device comprises flushing line and spray equipment, and spray equipment is installed on the flushing pipe.
4. floating bed filter according to claim 1 is characterized in that: need to add filter medium in the process of work, described filter medium is low density polyethylene (LDPE) particle or granules of polystyrene.
5. floating bed filter according to claim 1, it is characterized in that: described distribution device, cleaning device, meticulous microfilter device are fixed on the housing with hang.
6. floating bed filter according to claim 1 is characterized in that: the floating net of described annular is 304 or the 316L screen cloth.
CN 201220349166 2012-07-18 2012-07-18 Floating bed filter Expired - Fee Related CN202740880U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220349166 CN202740880U (en) 2012-07-18 2012-07-18 Floating bed filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220349166 CN202740880U (en) 2012-07-18 2012-07-18 Floating bed filter

Publications (1)

Publication Number Publication Date
CN202740880U true CN202740880U (en) 2013-02-20

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220349166 Expired - Fee Related CN202740880U (en) 2012-07-18 2012-07-18 Floating bed filter

Country Status (1)

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CN (1) CN202740880U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102772930A (en) * 2012-07-18 2012-11-14 烟台桑尼核星环保设备有限公司 Reclaimed water fine micro-filtration device
CN112023313A (en) * 2020-08-11 2020-12-04 沈文月 Fire control long-range water supply is with filtering anti-blocking device
CN112023505A (en) * 2020-08-11 2020-12-04 孙悦 Cleaning device for wastewater treatment pool for rare earth oxide production and implementation method thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102772930A (en) * 2012-07-18 2012-11-14 烟台桑尼核星环保设备有限公司 Reclaimed water fine micro-filtration device
CN102772930B (en) * 2012-07-18 2015-03-04 烟台桑尼核星环保设备有限公司 Reclaimed water fine micro-filtration device
CN112023313A (en) * 2020-08-11 2020-12-04 沈文月 Fire control long-range water supply is with filtering anti-blocking device
CN112023505A (en) * 2020-08-11 2020-12-04 孙悦 Cleaning device for wastewater treatment pool for rare earth oxide production and implementation method thereof

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C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130220

Termination date: 20150718

EXPY Termination of patent right or utility model