CN103007614A - High-efficiency energy-saving belt filter press - Google Patents
High-efficiency energy-saving belt filter press Download PDFInfo
- Publication number
- CN103007614A CN103007614A CN2012105841945A CN201210584194A CN103007614A CN 103007614 A CN103007614 A CN 103007614A CN 2012105841945 A CN2012105841945 A CN 2012105841945A CN 201210584194 A CN201210584194 A CN 201210584194A CN 103007614 A CN103007614 A CN 103007614A
- Authority
- CN
- China
- Prior art keywords
- filter
- roller
- filter press
- pressing
- belt
- 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.)
- Pending
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Landscapes
- Filtration Of Liquid (AREA)
Abstract
The invention discloses a high-efficiency energy-saving belt filter press which comprises a frame, a filter press belt, a hopper and a motor, and is characterized in that a material equalizing regulation device is arranged at a discharging end of the frame; the filter press belt is a double-layer filter cloth belt; a four-stage press filtering mechanism is arranged on the discharged filter press belt at intervals; a vacuum suction filtration disc for vacuumizing by utilizing a vacuum pump is arranged below the filter press belt behind a mesh cage roller; a tail gas cleaning mesh-cleaning roller and a filter press belt gas ejector pipe are respectively arranged on the mesh cage roller and on a belt return part of the filter press belt. The machine is uniform in feeding, long in service life, stable in performance, good in dewatering effect and high in yield, and the filter belt is difficult to block; the slag adhered to the mesh cage roller and the filter press belt is subjected to air injection cleaning by utilizing the vacuum pump tail gas, and water and electric energy are saved; and the machine is suitable for squeezing and dewatering manioc waste, cassava residues, bean dregs and distillers grains and water-containing raw materials in the industries such as municipal sludge, chemical industry, oil refining, papermaking and sugar refining.
Description
Technical field
The present invention relates to a kind of separator, especially from the solid matter that contains liquid, squeeze out the filter press of liquid.
Background technology
Squeeze out liquid from the solid matter that contains liquid, the filter press that liquid is separated with solid matter is used more extensive, and kind and the structure type of existing filter press are also more.Existing common equipment with slag class, mud and the dehydration of poor class material has single band and dual-belt filter press, come filter cloth belt and plastic cement belt filter press minute are arranged by the material of driving-belt, their structure is basic identical all to be to adopt driving-belt and roller to the extruding of the raw material on the driving-belt, makes water break away from the material body.Be mainly used in manioc waste, cassava grain stillage, bean dregs and alcohol grain, and the industries such as municipal sludge, chemical industry, oil refining, papermaking and sugaring to moisture raw-material press dewatering.These belt filter presses generally have following shortcoming:
1, charging is inhomogeneous, and press dewatering produces weak effect;
2, strainer is easily stifled, is subjected to force intensity little, and service life is short;
3, the up and down pair roller power of squeezing is little, easily skids inefficiency;
4, transmission power is large, needs power source many;
5, the material of looking into of viscous cleans with a large amount of water on pair roller barrel and the strainer, wastes energy;
6, costs and poor dehydration results, speed is slow, and output is not high.
Summary of the invention
The purpose of this invention is to provide that a kind of charging is even, strainer is difficult for stifled and long service life, and stable performance, saving water resource, dehydrating effect is good and output is high high-efficiency energy-saving belt type filter press.
For reaching above-mentioned purpose, technical scheme of the present invention is:
A kind of high-efficiency energy-saving belt type filter press, it comprises other of machine, filter-pressing strap, hopper and motor, it is characterized in that:
On the discharging end of described frame, the homocline adjusting device is set;
Described filter-pressing strap adopts the double-layer filter cloth band;
On the filter-pressing strap after the blanking, be arranged at intervals with level Four press filtration mounting mechanism; Wherein, the first order is cylinder mould roll-in filter device, and second～level Four adds the pair roller filter-pressing device of strong power for band;
Below the filter-pressing strap behind described cylinder mould roller, be provided with the vacuum suction filter dish that utilizes vavuum pump to vacuumize, vavuum pump is communicated with by vacuum tube with the vacuum suction filter dish;
On described cylinder mould roller and filter-pressing strap rewind the place above, respectively be provided with the air jet pipe that the tail gas that utilizes vavuum pump is washed cylinder mould roller and filter-pressing strap.
Described homocline adjusting device comprises on the discharging end that is located at frame, and the filter-pressing strap that wraps on the carrying roller is made the filter-pressing strap tensioning governor motion that tensioning is regulated, and is located at the material-stirring shaft in the described hopper.
Described filter-pressing strap tensioning governor motion is mainly by screw rod and can be by to bolt rotary, drives the member that carrying roller two end axles bearing moves and forms.
Described cylinder mould roller is that the outer surface at steel rider tightly covers the described double-layer filter cloth band of last layer.
Described second～level Four adds the power of pair roller filter-pressing device of strong power for band, the transmission mechanism that is comprised of by gear, sprocket wheel and chain the drive roll of fourth stage pair roller is transported to secondary home roll and three grades of home rolls.
The high-efficiency energy-saving belt type filter press of above structure by the homocline adjusting device, is not subjected to what the impact of slag charge moisture content, make slag charge be assigned to equably filter-pressing strap above, and be subject to level Four press filtration mounting mechanism and evenly push, dehydration is fully raised the efficiency.Filter-pressing strap adopts the double-layer filter cloth band, this double-layer filter cloth band is the applicant/inventor's last patent, the patent No. is 201020529965.7, it is fixed to connect by press filtration strap and press filtration guipure and consists of, have pliability, increased the intensity of filter-pressing strap and suitable water permeable ability, strainer is difficult for running the limit when operation, stability is high, and also greatly prolong service life.Below the filter-pressing strap behind the cylinder mould roller, be provided with the vacuum suction filter dish that utilizes vavuum pump to vacuumize, strengthen water separation capability.On the cylinder mould roller and filter-pressing strap rewind the place above, respectively be provided with the air jet pipe that utilizes tail gas of vacuum gas pump to clean filter-pressing strap, to viscous on the cylinder mould roller and the slag charge of filter-pressing strap above rewinding carry out jet cleaning, changed the routine with large water gaging cleaning.And this gas is to fill waste gas---the tail gas that has utilized vavuum pump to discharge, thereby has saved the energy.By the transmission mechanism that gear, sprocket wheel and chain form, power is transported to the roll shaft of each pair roller filter-pressing device, effectively solved the problem that pair roller easily skids, improved the stability of operating efficiency and performance.
Description of drawings
Fig. 1 is structural representation of the present invention;
Fig. 2 is the structural representation of filter-pressing device among Fig. 1;
Fig. 3 is that the present invention is at the power transmission structure schematic diagram;
In the drawings, filter-pressing device 1, hopper 2, material-stirring shaft 3, hopper actuating unit 4, vacuum tube 5, vavuum pump 6, cylinder mould roller offgas duct 7, filter-pressing strap offgas duct 8, drive unit 9, driver output axle 10, drive roll 11, pair roller actuating unit 12, basis 13, filter-pressing strap tensioning governor motion 14, carrying roller 15, filter-pressing strap 16; Cylinder mould roller 17, vacuum suction filter dish 18, secondary pressure roller pressure-regulating device 19,20, three grades of pressure roller pressure-regulating devices 21 of secondary home roll, secondary runner 22, three grades of home rolls 23, three grades of runners 24, level Four top roll 25, unloader knife 27, catch tray 28, frame 29, transition roller 30, gear and sprocket wheel and chain drive transmission mechanism 31 and sprocket wheel and chain drive transmission mechanism 32.
The specific embodiment
Below in conjunction with accompanying drawing, the invention will be further described.
Shown in Figure 1, be structural representation of the present invention; As we know from the figure, the present invention includes filter-pressing device 1, hopper 2, vavuum pump 6, drive unit 9 and pair roller actuating unit 12.Wherein, hopper 2 is located at the rear end of filter-pressing device 1, i.e. discharging end; Be provided with material-stirring shaft 3 in the bottom of hopper 2, an end of material-stirring shaft 3 is by hopper actuating unit 4 input powers.Material-stirring shaft 3 stirs the slag charge that enters in the hopper 4 in rotation, and slag charge be assigned to equably filter-pressing strap above.Vavuum pump 6 by vacuum tube 5, cylinder mould roller offgas duct 7 and filter-pressing strap offgas duct 8 with in the vacuum suction filter dish 18 of vacuum pneumatic transmission below being located at filter-pressing strap 16; With waste gas---the tail gas that vavuum pump is discharged, the top and filter-pressing strap 16 of delivering to respectively cylinder mould roller 17 rewind the place above.Drive unit 9 mainly is made of motor and decelerator, and by drive roll 11 power is passed to pair roller actuating unit 12 by the driver output axle 10 of decelerator.
Shown in Figure 2, be the structural representation of filter-pressing device among Fig. 1; Can see in the drawings, the under-chassis of frame 29 is fixed on the basis 13.On the rear end of frame 29, be provided with from top to bottom hopper 2, filter-pressing strap 16, carrying roller 15 and filter-pressing strap tensioning governor motion 14.Wherein, carrying roller 15 is enclosed with filter-pressing strap 16, and the end opening of hopper 2 is facing to above the filter-pressing strap 16.Filter-pressing strap tensioning governor motion 14 is mainly by screw rod and can be by to bolt rotary, drives the member that carrying roller 15 two end axles bearings move and forms.When moving after carrying roller 15 bearings at both ends, make filter-pressing strap 16 tensionings, filter-pressing strap 16 promotes, and near the end opening of hopper 2, discharging is thin, on the contrary discharging is thick, i.e. and the thickness of discharging is adjustable.Filter-pressing strap tensioning governor motion 14 matches with the work of material-stirring shaft 3, can make suitable being assigned to equably on the filter-pressing strap 16 of slag charge in the hopper 2.Described homocline adjusting device comprises on the discharging end that is located at frame 29, the filter-pressing strap 16 that wraps on the carrying roller 15 is made the filter-pressing strap tensioning governor motion 14 that tensioning is regulated, and be located at material-stirring shaft 3 in the described hopper 2.Filter-pressing strap 16 is back-shaped setting, its trace is from the end opening of hopper 2, clockwise operation is sequentially through below the one-level squeezing cylinder mould roller 17, above the vacuum suction filter dish 18, between the pair roller of secondary home roll 20 and secondary runner 22, between the pair roller of three grades of home rolls 23 and three grades of runners 24, between 11 pairs of level Four top roll 25 and the drive rolls; Its backhaul is sequentially got back to the end opening of carrying roller 15 and hopper 2 through following, a transition roller 30 of two transition rollers 30, filter-pressing strap offgas duct 8 from below the drive roll 11.Wherein, trace at filter-pressing strap 16, slag charge bleed off pressure strainer 16 above, sequentially through below the one-level squeezing cylinder mould roller 17, above the vacuum suction filter dish 18, between the pair roller of secondary home roll 20 and secondary runner 22, between the pair roller of three grades of home rolls 23 and three grades of runners 24, between 11 pairs of level Four top roll 25 and the drive rolls, namely be the process of moisture slag charge sequentially being carried out one～level Four press dewatering.Vacuum tube 5 in Fig. 1 communicates with vacuum suction filter dish 18, and vacuum suction will be inhaled through the slag charge moisture content on the filter-pressing strap 16 above the vacuum suction filter dish 18 lower, and dehydration is discharged.On two～level Four pair roller, be provided with respectively secondary pressure roller pressure-regulating device 19, three grades of pressure roller pressure-regulating devices 21 and three grades of pressure roller pressure-regulating devices 21, every grade of squeezing all can be regulated squeeze pressure, according to parameters such as moisture content of material, inlet amounies, rationally regulate the squeeze pressure of belt speed and every one-level, can obtain best press dewatering effect.Filter-pressing strap adopts the double-layer filter cloth band, and this double-layer filter cloth band is the applicant/inventor's last patent, and the patent No. is 201020529965.7, and its performance is better than traditional filter-pressing strap, and details are seen its patent specification.Described double-deck belt structure is: being fixedly connected of press filtration strap and press filtration guipure opposite face consists of double-deck strainer.The double-layer filter cloth band can move in higher speed, but life-span of ductility strainer again.Be applied on the filter press of the present invention, can improve running speed and yield and stability.Described cylinder mould roller 17 is that the outer surface at steel rider tightly covers the described double-layer filter cloth band of last layer, it owing to coincideing of lines on cover and the zone face, has increased the squeezing area with both under durable prerequisite, namely increased slag charge pressure face and dynamics, can increase dehydration rate.So, cooperate with filter-pressing strap 16 with cylinder mould roller 17, as the first order squeezing to slag charge.Cylinder mould roller offgas duct 7 is set on cylinder mould roller 17, takes full advantage of the waste gas that vavuum pump is discharged, the slag charge of viscous on the cylinder mould roller 17 is carried out blowing-out wash, the water of deviating from can be discharged smoothly, be beneficial to the raising dehydration rate.In like manner, on the backhaul of filter-pressing strap 16, the slag charge of viscous is set on 8 pairs of filter-pressing straps 16 of filter-pressing strap offgas duct carries out blowing-out and wash, changed the mode of in the past giant shot blastinog, saved a large amount of waters and electric energy.Vavuum pump adopts roots blower, utilizes the vacuum of its generation that slag charge is inhaled dehydration, and the waste gas that reclaims its discharge carries out blowing-out to cylinder mould roller 17 and filter-pressing strap 16 and washes.Below one-level cylinder mould roller 17, secondary runner 22, three grades of runners 24 and drive roll 11, all be provided with catch tray 28, collect the moisture content that slag charge squeezes out and discharge.At the end of filter-pressing strap 16 traces, namely the front of drive roll 11 is provided with tilting unloader knife 27, will discharge with slag charge behind the filter-press dehydration.
Shown in Figure 3, that the present invention is at the power transmission structure schematic diagram, come together to see in conjunction with Fig. 1 and Fig. 2, drive unit 9 is passed to drive roll 11 by driver output axle 10 with power, the drive roll 11 again roller actuating unit 12 that forms of the gear by a side, sprocket wheel and chain flows to respectively secondary home roll 20 and three grades of home rolls 23, and makes each roller synchronous operation.Pair roller power is little up and down to have solved squeezing, the problem of easily skidding.Simultaneously, drive roll 11 is also passed to carrying roller 15 by filter-pressing strap 16 with power, the transmission mechanism 32 that forms by sprocket wheel and chain again on the extending shaft of carrying roller 15 1 ends is passed to the material-stirring shaft 3 in the hopper 2, material-stirring shaft 3 is rotated, mix the slag charge in the equal hopper 2, and be assigned to above the filter-pressing strap 16 under the hopper outlet.Filter-pressing strap 16 is in operation and constantly slag charge fortune is separated through the dehydration of level Four pressure roller.
Operation principle of the present invention is:
1, adjust, by the interval between the transition roller 30 of regulating cylinder mould roller 17 sides, and the squeeze pressure of adjusting secondary pressure roller pressure-regulating device 19, three grades of pressure roller pressure-regulating devices 21 and three grades of pressure roller pressure-regulating devices 21; Regulate filter-pressing strap tensioning governor motion 14, limit hopper 2 dischargings to the thickness above the filter-pressing strap 16;
2, charging and cloth start vavuum pump 6, drive unit 9, each roller, hopper 2 material-stirring shafts 3 and filter-pressing strap 16 operations.At discharging end charging, cloth.When real work, through the slag charge of vertical sieve screening---material (solidliquid mixture) is sifted out hopper and is fallen into continuously filter press hopper 2 by vertical, and stirs after the buffering through hopper material-stirring shaft 3, is distributed to uniformly above the filter-pressing strap 16;
3, press filtration, material are carried out preliminary press filtration through cylinder mould roller 17 after being distributed to above the filter-pressing strap 16, and most moisture is fallen in press filtration, forms compressible filter cake;
4, suction strainer is after 17 press filtrations of cylinder mould roller, in filter-pressing strap 16 and slag charge, contain certain moisture, pass through again the imbibition of vacuum suction filter dish 18, absorb most of moisture content, prevented that moisture content from being absorbed by slag charge again and enter the next stage pressed zone, impact squeezing effect improves dewatering efficiency;
5, squeezing in pressed zone, is provided with between the pair roller of secondary home roll 20 and secondary runner 22, three grades of squeezings between the pair roller of three grades of home rolls 23 and three grades of runners 24.Every grade of squeezing all can be regulated squeeze pressure, during use, according to parameters such as moisture content of material, inlet amounies, rationally regulates the squeeze pressure of belt speed and every one-level, can obtain best press dewatering effect.The moisture of the discharges such as press filtration district, suction strainer district, pressed zone is all collected through the catch tray that the bottom is provided with, prevent from directly falling into the strainer back side of bottom, effectively avoided the repeatedly absorption of moisture, add the cleaning action of filtering band cleaning unit, guaranteed the cleaning of strainer and the press filtration effect of complete machine;
6, clean, the waste gas that utilizes vavuum pump 6 to discharge, by cylinder mould roller offgas duct 7 and filter-pressing strap offgas duct 8, respectively tail gas is guided to above the backhaul of top and filter-pressing strap 16 of cylinder mould roller 17, the slag charge of viscous on cylinder mould roller 17 and the filter-pressing strap 16 is carried out blowing-out to be washed, change the mode of in the past giant shot blastinog, saved a large amount of waters and electric energy;
7, discharge, at the end of filter-pressing strap 16 traces, namely the front of drive roll 11 is provided with tilting unloader knife 27, will discharge with slag charge behind the filter-press dehydration.So far whole press dewatering process is all finished.
Claims (6)
1. high-efficiency energy-saving belt type filter press, it comprises other of machine, filter-pressing strap, hopper and motor, it is characterized in that:
On the discharging end of described frame (29), the homocline adjusting device is set;
Described filter-pressing strap (16) adopts the double-layer filter cloth band;
On the filter-pressing strap after the blanking (16), be arranged at intervals with level Four press filtration mounting mechanism; Wherein, the first order is cylinder mould roller (17) filter-pressing device, and second～level Four adds the pair roller filter-pressing device of strong power for band;
Below the filter-pressing strap (16) behind described cylinder mould roller (17), be provided with the vacuum suction filter dish (18) that utilizes vavuum pump (6) to vacuumize, vavuum pump (6) is communicated with by vacuum tube (5) with vacuum suction filter dish (18);
On described cylinder mould roller (17) and filter-pressing strap (16) rewind the place above, respectively be provided with the air jet pipe (7,8) that the tail gas that utilizes vavuum pump (6) cleans cylinder mould roller (17) and filter-pressing strap (16).
2. high-efficiency energy-saving belt type filter press according to claim 1 is characterized in that:
Described homocline adjusting device comprises on the discharging end that is located at frame (29), and the filter-pressing strap (16) that wraps on the carrying roller (15) is made the filter-pressing strap tensioning governor motion (14) that tensioning is regulated, and is located at the material-stirring shaft (3) in the described hopper (2).
3. high-efficiency energy-saving belt type filter press according to claim 1 and 2 is characterized in that:
Described filter-pressing strap tensioning governor motion (14) is mainly by screw rod and can be by to bolt rotary, drives the member that carrying roller two end axles bearing moves and forms.
4. high-efficiency energy-saving belt type filter press according to claim 1 is characterized in that:
Described cylinder mould roller (17) is that the outer surface at steel rider tightly covers the described double-layer filter cloth band of last layer.
5. high-efficiency energy-saving belt type filter press according to claim 1 is characterized in that:
Described second～level Four adds the power of pair roller filter-pressing device of strong power for band, the transmission mechanism (12) that is comprised of by gear, sprocket wheel and chain the drive roll (11) of fourth stage pair roller is transported to secondary home roll (20) and three grades of home rolls (23).
6. high-efficiency energy-saving belt type filter press according to claim 1 is characterized in that:
Being fixedly connected of press filtration strap and press filtration guipure opposite face consists of double-deck strainer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012105841945A CN103007614A (en) | 2012-12-30 | 2012-12-30 | High-efficiency energy-saving belt filter press |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012105841945A CN103007614A (en) | 2012-12-30 | 2012-12-30 | High-efficiency energy-saving belt filter press |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103007614A true CN103007614A (en) | 2013-04-03 |
Family
ID=47957054
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012105841945A Pending CN103007614A (en) | 2012-12-30 | 2012-12-30 | High-efficiency energy-saving belt filter press |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103007614A (en) |
Cited By (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103285648A (en) * | 2013-06-25 | 2013-09-11 | 湖州核宏机械有限公司 | Filter belt tensioning control device of vacuum filter |
| CN103342753A (en) * | 2013-07-26 | 2013-10-09 | 陆汉克 | Production method of cassava starch |
| CN103611354A (en) * | 2013-11-29 | 2014-03-05 | 广西大学 | Multistage filtering squeezer for cassava residues |
| CN103623632A (en) * | 2013-11-29 | 2014-03-12 | 广西大学 | Three-wheel rolling filter press for cassava residue |
| CN103623634A (en) * | 2013-11-29 | 2014-03-12 | 广西大学 | Belt type manioc waste pressure filter |
| CN103623633A (en) * | 2013-11-29 | 2014-03-12 | 广西大学 | Barbell type manioc waste belt pressure filter with mud carding device |
| CN103877774A (en) * | 2014-03-27 | 2014-06-25 | 宜兴市意达铜业有限公司 | Filtration fabric recycling utilization device for copper alloy production line |
| CN104275818A (en) * | 2013-07-01 | 2015-01-14 | 北京瑞仕邦科技有限公司 | Circulating belt type squeezing device |
| CN104418478A (en) * | 2013-09-10 | 2015-03-18 | 中国科学院大连化学物理研究所 | Method for processing sludge employing biocide-coupled quick lime |
| CN104707388A (en) * | 2013-12-12 | 2015-06-17 | 北京瑞仕邦科技有限公司 | Circulation belt-type squeezing device |
| CN104922962A (en) * | 2015-06-10 | 2015-09-23 | 北京中矿环保科技股份有限公司 | Filter press with single filter belt |
| US20160264894A1 (en) * | 2015-03-09 | 2016-09-15 | Mitsubishi Heavy Industries, Ltd. | Pyrolyzed coal finisher, coal upgrade plant, and method for manufacturing deactivated pyrolyzed coal |
| CN105999813A (en) * | 2016-07-14 | 2016-10-12 | 四特酒有限责任公司 | Waste distillage water separation, treatment and delivery device |
| CN107721124A (en) * | 2017-12-10 | 2018-02-23 | 泰兴市洁源环保工程有限公司 | A kind of belt mud dewatering equipment structure |
| CN108126399A (en) * | 2017-12-20 | 2018-06-08 | 中冶宝钢技术服务有限公司 | The heavy mud dehydration device of metallurgy |
| US10151530B2 (en) | 2015-03-09 | 2018-12-11 | Mitsubishi Heavy Industries Engineering, Ltd. | Coal upgrade plant and method for manufacturing upgraded coal |
| US10188980B2 (en) | 2015-03-09 | 2019-01-29 | Mitsubishi Heavy Industries Engineering, Ltd. | Coal upgrade plant and method for manufacturing upgraded coal |
| US10221070B2 (en) | 2015-03-09 | 2019-03-05 | Mitsubishi Heavy Industries Engineering, Ltd. | Coal upgrade plant and method for manufacturing upgraded coal |
| CN110215755A (en) * | 2019-05-15 | 2019-09-10 | 湖州核工惠能环保过滤科技有限公司 | A kind of vacuum change chamber belt filter press |
| US10703976B2 (en) | 2015-03-09 | 2020-07-07 | Mitsubishi Heavy Industries Engineering, Ltd. | Pyrolyzed coal quencher, coal upgrade plant, and method for cooling pyrolyzed coal |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2132967A (en) * | 1982-09-27 | 1984-07-18 | Enviro Clear Co Inc | Aircushion support and fluid film air bearing for use in horizontal belt vacuum filters |
| CN2429242Y (en) * | 2000-04-30 | 2001-05-09 | 核工业华东烟台机械厂 | Continuous vacuum belt press filtering apparatus |
| CN201578913U (en) * | 2010-01-18 | 2010-09-15 | 广西武鸣丰克机械有限公司 | Belt-type filter press |
| CN201791417U (en) * | 2010-09-15 | 2011-04-13 | 陆汉克 | Double-layered filter fabric belt of belt filter press |
| US20110132832A1 (en) * | 2009-12-07 | 2011-06-09 | Flsmidth A/S | Horizontal belt vacuum filter with overhead fluid removal |
| CN203170095U (en) * | 2012-12-30 | 2013-09-04 | 陆汉克 | High-efficiency energy-saving belt type filter press |
-
2012
- 2012-12-30 CN CN2012105841945A patent/CN103007614A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2132967A (en) * | 1982-09-27 | 1984-07-18 | Enviro Clear Co Inc | Aircushion support and fluid film air bearing for use in horizontal belt vacuum filters |
| CN2429242Y (en) * | 2000-04-30 | 2001-05-09 | 核工业华东烟台机械厂 | Continuous vacuum belt press filtering apparatus |
| US20110132832A1 (en) * | 2009-12-07 | 2011-06-09 | Flsmidth A/S | Horizontal belt vacuum filter with overhead fluid removal |
| CN201578913U (en) * | 2010-01-18 | 2010-09-15 | 广西武鸣丰克机械有限公司 | Belt-type filter press |
| CN201791417U (en) * | 2010-09-15 | 2011-04-13 | 陆汉克 | Double-layered filter fabric belt of belt filter press |
| CN203170095U (en) * | 2012-12-30 | 2013-09-04 | 陆汉克 | High-efficiency energy-saving belt type filter press |
Cited By (24)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103285648A (en) * | 2013-06-25 | 2013-09-11 | 湖州核宏机械有限公司 | Filter belt tensioning control device of vacuum filter |
| CN103285648B (en) * | 2013-06-25 | 2015-01-14 | 湖州核宏机械有限公司 | Filter belt tensioning control device of vacuum filter |
| CN104275818B (en) * | 2013-07-01 | 2016-01-06 | 北京瑞仕邦科技有限公司 | A kind of circulating belt pressing device |
| CN104275818A (en) * | 2013-07-01 | 2015-01-14 | 北京瑞仕邦科技有限公司 | Circulating belt type squeezing device |
| CN103342753A (en) * | 2013-07-26 | 2013-10-09 | 陆汉克 | Production method of cassava starch |
| CN104418478A (en) * | 2013-09-10 | 2015-03-18 | 中国科学院大连化学物理研究所 | Method for processing sludge employing biocide-coupled quick lime |
| CN104418478B (en) * | 2013-09-10 | 2017-03-29 | 中国科学院大连化学物理研究所 | A kind of method that biocide coupling quick lime processes sludge |
| CN103611354A (en) * | 2013-11-29 | 2014-03-05 | 广西大学 | Multistage filtering squeezer for cassava residues |
| CN103623632A (en) * | 2013-11-29 | 2014-03-12 | 广西大学 | Three-wheel rolling filter press for cassava residue |
| CN103623634A (en) * | 2013-11-29 | 2014-03-12 | 广西大学 | Belt type manioc waste pressure filter |
| CN103623633A (en) * | 2013-11-29 | 2014-03-12 | 广西大学 | Barbell type manioc waste belt pressure filter with mud carding device |
| CN104707388A (en) * | 2013-12-12 | 2015-06-17 | 北京瑞仕邦科技有限公司 | Circulation belt-type squeezing device |
| CN103877774A (en) * | 2014-03-27 | 2014-06-25 | 宜兴市意达铜业有限公司 | Filtration fabric recycling utilization device for copper alloy production line |
| US20160264894A1 (en) * | 2015-03-09 | 2016-09-15 | Mitsubishi Heavy Industries, Ltd. | Pyrolyzed coal finisher, coal upgrade plant, and method for manufacturing deactivated pyrolyzed coal |
| US10151530B2 (en) | 2015-03-09 | 2018-12-11 | Mitsubishi Heavy Industries Engineering, Ltd. | Coal upgrade plant and method for manufacturing upgraded coal |
| US10188980B2 (en) | 2015-03-09 | 2019-01-29 | Mitsubishi Heavy Industries Engineering, Ltd. | Coal upgrade plant and method for manufacturing upgraded coal |
| US10221070B2 (en) | 2015-03-09 | 2019-03-05 | Mitsubishi Heavy Industries Engineering, Ltd. | Coal upgrade plant and method for manufacturing upgraded coal |
| US10703976B2 (en) | 2015-03-09 | 2020-07-07 | Mitsubishi Heavy Industries Engineering, Ltd. | Pyrolyzed coal quencher, coal upgrade plant, and method for cooling pyrolyzed coal |
| CN104922962A (en) * | 2015-06-10 | 2015-09-23 | 北京中矿环保科技股份有限公司 | Filter press with single filter belt |
| CN105999813A (en) * | 2016-07-14 | 2016-10-12 | 四特酒有限责任公司 | Waste distillage water separation, treatment and delivery device |
| CN105999813B (en) * | 2016-07-14 | 2018-07-20 | 四特酒有限责任公司 | Grains waste water separating treatment conveying device |
| CN107721124A (en) * | 2017-12-10 | 2018-02-23 | 泰兴市洁源环保工程有限公司 | A kind of belt mud dewatering equipment structure |
| CN108126399A (en) * | 2017-12-20 | 2018-06-08 | 中冶宝钢技术服务有限公司 | The heavy mud dehydration device of metallurgy |
| CN110215755A (en) * | 2019-05-15 | 2019-09-10 | 湖州核工惠能环保过滤科技有限公司 | A kind of vacuum change chamber belt filter press |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103007614A (en) | High-efficiency energy-saving belt filter press | |
| CN100355481C (en) | Belt type filter press | |
| CN203060942U (en) | Roller screen type solid-liquid separator | |
| CN105922617A (en) | High-moisture forage grass and straw dewatering device | |
| CN201260913Y (en) | Pressure filter | |
| CN215480481U (en) | A centrifugal filter-pressing dewatering device of mud for sewage treatment plant | |
| CN203170095U (en) | High-efficiency energy-saving belt type filter press | |
| CN103623633A (en) | Barbell type manioc waste belt pressure filter with mud carding device | |
| CN206337139U (en) | A kind of novel high-pressure belt type sludge deep dehydrator | |
| CN204434441U (en) | Movable type sludge dewatering unit | |
| CN117065416A (en) | Plate-and-frame filter press for treating epoxy resin wastewater and filter cake cutting method | |
| CN103358581B (en) | Squeezing machine | |
| CN104524846B (en) | Wedge shape supercharging sawtooth groove double dewatering squeezes belt filter press | |
| CN206896968U (en) | large belt filter press | |
| CN2171401Y (en) | Belt filter press | |
| JP6466366B2 (en) | Sludge dewatering device and cleaning method thereof | |
| CN211876543U (en) | Raw material dehydration device | |
| CN201512467U (en) | Sludge dewatering device | |
| CN212072562U (en) | Squeezing granulator | |
| CN100404099C (en) | High-efficient strong filter press | |
| CN209756172U (en) | Water surface cleaning ship with dewatering function | |
| CN201926254U (en) | Dehydration equipment for starch residue | |
| CN206896969U (en) | Large belt filter press press filtration processing system | |
| CN202456332U (en) | Drying press for cassava dreg | |
| CN209322692U (en) | A kind of activated sludge dehydration 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 | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20130403 |