CN201482299U - Multifunctional combined type belt press filter - Google Patents
Multifunctional combined type belt press filter Download PDFInfo
- Publication number
- CN201482299U CN201482299U CN2009201463679U CN200920146367U CN201482299U CN 201482299 U CN201482299 U CN 201482299U CN 2009201463679 U CN2009201463679 U CN 2009201463679U CN 200920146367 U CN200920146367 U CN 200920146367U CN 201482299 U CN201482299 U CN 201482299U
- Authority
- CN
- China
- Prior art keywords
- dewater unit
- flocculation
- enrichment facility
- filter press
- flocculation plant
- 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
Images
Landscapes
- Treatment Of Sludge (AREA)
Abstract
The utility model relates to a sludge treatment system device of a water treatment system in the field of environmental protection, which is applicable to sludge treatment of the multifunctional combined type belt press filter. The device comprises a flocculation device, a concentration device, a wideband distribution device and a dewatering device and integrates functions of flocculation, concentration, and dewatering. The press filter solves the defects of insufficient mixing and flocculation, mass of sludge contained in the filter liquor, uniform material distribution and the like. When the slurry concentration is less than 1%, the flocculation device, the concentration device and the dewatering device are combined, and when the slurry concentration is larger than 1%, the flocculation device, the wideband material distribution device and the dewatering device are combined.
Description
Technical field
The utility model relates in the water treatment system of a kind of environmental protection field, is applicable to the multifunction combined belt filter press of Treatment of Sludge.
Background technology
In the sludge treatment device in the water treatment system of environmental protection field, belt filter press is the equipment that extensively adopts.Belt dehydration equipment form is a lot of at present, but owing to various use reasons, all has in the mud separation process, and it is insufficient to mix, flocculate, and has influenced the belt filter press result of use, has increased the expense of Treatment of Sludge virtually.
The utility model content
The technical problems to be solved in the utility model provides a kind of Collecting flocculation, concentrates, cloth and dewatering in the multifunction combined belt filter press of one, solves defective such as to mix, flocculation is insufficient, still contains a large amount of mud in the filtrate, and cloth is inhomogeneous.
In order to address the above problem, the utility model provides a kind of multifunction combined belt filter press of being made up of flocculation plant, enrichment facility, broadband distribution device, dewater unit.Concentration of hydraulic mixture adopted flocculation plant, enrichment facility, dewater unit combination less than 1% o'clock, and concentration adopted flocculation plant, broadband distribution device, dewater unit combination greater than 1% o'clock, and flocculation plant is installed in dewater unit top left end; Enrichment facility is installed in the middle of the dewater unit top; The broadband distribution device is installed in the middle of the dewater unit top.
Flocculation plant is the device that flocculation tube and the mixer that is installed in flocculation tube top are formed; The mixer of described flocculation plant is a spiral hoisting type mixer.
Enrichment facility is the left end that enrichment facility drive motors reductor is installed in enrichment facility, and its right side is installed 1~3 and concentrated the net tube, and the bottom righthand side of enrichment facility is installed the device that 1~3 little distributing device is formed.
The broadband distribution device is the device that distributing trough and the material distribution cartridge that is installed in distributing trough top are formed.
Dewater unit is the left side, upper end that the gravity dehydration district is positioned at dewater unit, and the gravity dehydration district installs on the right side strainer cleaning device successively, goes up deviation correcting device, dewater unit drive motors reductor; Drive roll is installed in the right-hand member of dewater unit, the right side forms the stripping area between the drive roll, the S shape zone in left side, stripping area is S extrusion dehydration district, left side, S extrusion dehydration district is a wedge shape drying zone of going up strainer and lower filter belt formation, slewing rollers are installed in the left end of dehydration equipment, following deviation correcting device is installed in the right side, bottom of dewater unit, and the lower filter belt cleaning device is installed in down the device that the deviation correcting device left group becomes.
Description of drawings
Below in conjunction with the drawings and specific embodiments the utility model is described in further detail.
Fig. 1 is the schematic diagram of first kind of embodiment of the multifunction combined belt filter press of the utility model.
Fig. 2 is the schematic diagram of second kind of embodiment of the multifunction combined belt filter press of the utility model.
The specific embodiment
The utility model working condition is such:
As shown in Figure 1, enter flocculation plant 23 through the former low concentration mud after the dosing by mud mouth 20, mud flocculation in flocculation tube 2 is quickened the reaction of mud and medicament by mixer 1 stirring of spiral hoisting type, form bigger flocculation group, flow automatically to then in the enrichment facility 4.Drive stainless steel by enrichment facility drive motors reductor 3 and concentrate 5 rotations of net tube, mud concentrates in concentrating net tube 5, and the mud after concentrating is evenly distributed on the strainer 19 by supporting little distributing device 7.Dewater unit drive motors reductor 10 drives drive roll 11 and rotates, and strainer 19 is gone up in drive roll 11 drives and lower filter belt 16 moves.Mud drives by gravity dehydration district 6 at last strainer 19, pressure maintaining valve provides the slewing rollers 18 of constant pressure, turn to and fall on the lower filter belt 16, push in advance at wedge shape drying zone 17 then, at last at S extrusion dehydration district 13 extrusion dehydrations, and the formation mud cake, mud cake finally 12 is isolated dewater unit 25 in the stripping area.Last strainer 19 is adjusted the position of strainer by the last deviation correcting device 9 of fluid valve control.8 pairs of last strainer cleaning devices are gone up strainer 19 and are cleaned.Lower filter belt 16 is adjusted the position of strainer by the following deviation correcting device 14 of fluid valve control.15 pairs of lower filter belts 16 of lower filter belt cleaning device clean.
The former low concentration mud through after the dosing that shows as Fig. 2 enters flocculation plant 23 by mud mouth 20, mud flocculation in flocculation tube 2, mixer 1 by the spiral hoisting type stirs the reaction of quickening mud and medicament, form bigger flocculation group, flow automatically to broadband distribution device 24 then, coagulation in material distribution cartridge 21 is evenly distributed to strainer 19 by distributing trough 22 again.Dewater unit drive motors reductor 10 drives drive roll 11 and rotates, and strainer 19 is gone up in drive roll 11 drives and lower filter belt 16 moves.Mud drives by gravity dehydration district 6 at last strainer 19, pressure maintaining valve provides the slewing rollers 18 of constant pressure, turn to and fall on the lower filter belt 16, push in advance at wedge shape drying zone 17 then, at last at S extrusion dehydration district 13 extrusion dehydrations, and the formation mud cake, mud cake finally 12 is isolated dewater unit 25 in the stripping area.Last strainer 19 is adjusted the position of strainer by the last deviation correcting device 9 of fluid valve control.8 pairs of last strainer cleaning devices are gone up strainer 19 and are cleaned.Lower filter belt 16 is adjusted the position of strainer by the following deviation correcting device 14 of fluid valve control.15 pairs of lower filter belts 16 of lower filter belt cleaning device clean.
Claims (5)
1. multifunction combined belt filter press, by flocculation plant, enrichment facility, the broadband distribution device, dewater unit constitutes, concentration of hydraulic mixture adopted flocculation plant, enrichment facility, dewater unit to make up less than 1% o'clock, concentration adopted flocculation plant, broadband distribution device, dewater unit combination greater than 1% o'clock, and it is characterized in that: described flocculation plant (23) is installed in dewater unit (25) top left end, and enrichment facility (4) is installed in the middle of dewater unit (25) top; Broadband distribution device (24) is installed in the middle of dewater unit (25) top.
2. according to the described multifunction combined belt filter press of claim 1, it is characterized in that: described flocculation plant (23) is the device that flocculation tube (2) and the mixer (1) that is installed in flocculation tube (2) top are formed; The mixer (1) of described flocculation plant (23) is a spiral hoisting type mixer.
3. according to the described multifunction combined belt filter press of claim 1, it is characterized in that: described enrichment facility (4) is the left end that enrichment facility drive motors reductor (3) is installed in enrichment facility, its right side is installed 1~3 and is concentrated net tube (5), and the bottom righthand side of enrichment facility is installed the device that 1~3 little distributing device (7) is formed.
4. according to the described multifunction combined belt filter press of claim 1, it is characterized in that: described broadband distribution device (24) is the device that distributing trough (22) and the material distribution cartridge (21) that is installed in distributing trough (22) top are formed.
5. according to the described multifunction combined belt filter press of claim 1, it is characterized in that: described dewater unit (25) is the left side, upper end that gravity dehydration district (6) is positioned at dewater unit (25), gravity dehydration district (6) installs strainer cleaning device (8) in the right side successively, last deviation correcting device (9), dewater unit drive motors reductor (10), drive roll (11) is installed in the right-hand member of dewater unit (25), the right side forms stripping area (12) between the drive roll (11), the S shape zone in left side, stripping area (12) is S extrusion dehydration district (13), left side, S extrusion dehydration district (13) is a wedge shape drying zone (17) of going up strainer (19) and lower filter belt (16) formation, slewing rollers (18) are installed in the left end of dewater unit (25), following deviation correcting device (14) is installed in the right side, bottom of dewater unit (25), and lower filter belt cleaning device (15) is installed in down the device that deviation correcting device (14) left side is formed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2009201463679U CN201482299U (en) | 2009-03-18 | 2009-03-18 | Multifunctional combined type belt press filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2009201463679U CN201482299U (en) | 2009-03-18 | 2009-03-18 | Multifunctional combined type belt press filter |
Publications (1)
Publication Number | Publication Date |
---|---|
CN201482299U true CN201482299U (en) | 2010-05-26 |
Family
ID=42421193
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2009201463679U Expired - Fee Related CN201482299U (en) | 2009-03-18 | 2009-03-18 | Multifunctional combined type belt press filter |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN201482299U (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102849914A (en) * | 2011-06-29 | 2013-01-02 | 南通奥贝尔工程技术有限公司 | Belt type press filtering-concentrating-dehydrating integrated machine |
CN103830950A (en) * | 2012-11-20 | 2014-06-04 | 江苏普利斯环保科技有限公司 | Belt-type sludge thickening and dewatering all-in-one machine |
CN104487235A (en) * | 2012-07-24 | 2015-04-01 | 北欧机械制造鲁道夫巴德尔有限及两合公司 | Chain link, support chain, and support device |
CN105060676A (en) * | 2015-08-25 | 2015-11-18 | 浙江华章科技有限公司 | Intelligent control continuous concentration and deep dewatering integrated machine |
CN106237694A (en) * | 2016-08-31 | 2016-12-21 | 沈阳禹华环保有限公司 | Belt filter press concentration one sludge filter press |
CN110539513A (en) * | 2019-09-29 | 2019-12-06 | 东宸环保装备制造有限公司 | A high-efficient full-automatic mineral separator for saw mud |
CN112452037A (en) * | 2020-11-13 | 2021-03-09 | 王琳 | Belt filter press for sludge dewatering with backwash function |
-
2009
- 2009-03-18 CN CN2009201463679U patent/CN201482299U/en not_active Expired - Fee Related
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102849914A (en) * | 2011-06-29 | 2013-01-02 | 南通奥贝尔工程技术有限公司 | Belt type press filtering-concentrating-dehydrating integrated machine |
CN104487235A (en) * | 2012-07-24 | 2015-04-01 | 北欧机械制造鲁道夫巴德尔有限及两合公司 | Chain link, support chain, and support device |
CN104487235B (en) * | 2012-07-24 | 2017-03-08 | 北欧机械制造鲁道夫巴德尔有限及两合公司 | Chain link, supporting chain and supporting arrangement |
US10376893B2 (en) | 2012-07-24 | 2019-08-13 | Nordischer Maschinebau RUD. Baader GMBH + Co., KG | Chain link, support chain, and support device |
CN103830950A (en) * | 2012-11-20 | 2014-06-04 | 江苏普利斯环保科技有限公司 | Belt-type sludge thickening and dewatering all-in-one machine |
CN105060676A (en) * | 2015-08-25 | 2015-11-18 | 浙江华章科技有限公司 | Intelligent control continuous concentration and deep dewatering integrated machine |
CN105060676B (en) * | 2015-08-25 | 2017-10-20 | 浙江华章科技有限公司 | A kind of intelligence control continuous concentration deep dehydration all-in-one |
CN106237694A (en) * | 2016-08-31 | 2016-12-21 | 沈阳禹华环保有限公司 | Belt filter press concentration one sludge filter press |
CN110539513A (en) * | 2019-09-29 | 2019-12-06 | 东宸环保装备制造有限公司 | A high-efficient full-automatic mineral separator for saw mud |
CN110539513B (en) * | 2019-09-29 | 2021-05-11 | 东宸环保装备制造有限公司 | A high-efficient full-automatic mineral separator for saw mud |
CN112452037A (en) * | 2020-11-13 | 2021-03-09 | 王琳 | Belt filter press for sludge dewatering with backwash function |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN201482299U (en) | Multifunctional combined type belt press filter | |
US4105558A (en) | Apparatus for draining of muddy liquids | |
CN201358206Y (en) | Integral equipment for sludge thickening and dehydrating | |
CN201713368U (en) | Concentration, flocculation and dewatering integrated machine | |
CN206736066U (en) | A kind of combined type deep dehydration system for sludge | |
CN105645731B (en) | The secondary concentration kettle and its method for sludge treatment of thickened sludge | |
CN206736067U (en) | A kind of Integral sludge deep dehydration system | |
CN209333318U (en) | Drum concentration two filtering bands formula dewaterer | |
CN204325027U (en) | Quick sewage disposal device | |
CN110282853A (en) | The purification device and its purification method of integrated sewage materializing strategy and sludge dewatering | |
CN203370393U (en) | Chemical dosing device for strengthening dehydration effect of pressurized filter by using aluminium polychlorid filter aid | |
CN203845883U (en) | Textile wastewater coagulation inclined pipe combined settling pond | |
CN204974463U (en) | Purify device of sizing material | |
CN201799149U (en) | Belt sewage filter | |
CN204675980U (en) | A kind of sludge dehydration device | |
CN208049469U (en) | It is a kind of to prevent from running the ion fiber filter device expected | |
CN205368336U (en) | Natural pond sediment natural pond liquid separator | |
CN115385539A (en) | Sludge step-by-step separation system | |
CN112851069B (en) | Belt type concentration and dehydration integrated machine and working method | |
CN204700030U (en) | A kind of containing cyanogen waste residue total system | |
CN210885461U (en) | Mixed reaction device | |
CN210237324U (en) | Bean product wastewater pretreatment device | |
CN208747910U (en) | Sludge dewatering treatment device | |
CN113830952A (en) | Phosphorite mine water treatment system and treatment method | |
CN207970583U (en) | A kind of pig farm equipment for separating liquid from solid reducing obstruction |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
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: 20100526 Termination date: 20180318 |
|
CF01 | Termination of patent right due to non-payment of annual fee |