CN205115110U - Filter is suppressed to electroosmosis high pressure - Google Patents
Filter is suppressed to electroosmosis high pressure Download PDFInfo
- Publication number
- CN205115110U CN205115110U CN201520942937.0U CN201520942937U CN205115110U CN 205115110 U CN205115110 U CN 205115110U CN 201520942937 U CN201520942937 U CN 201520942937U CN 205115110 U CN205115110 U CN 205115110U
- Authority
- CN
- China
- Prior art keywords
- end rail
- cross beam
- mould
- high voltage
- moved cross
- 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.)
- Active
Links
- 238000005370 electroosmosis Methods 0.000 title abstract 4
- 239000000463 material Substances 0.000 claims abstract description 26
- 238000000034 method Methods 0.000 claims abstract description 13
- 238000007599 discharging Methods 0.000 claims description 15
- 239000004744 fabric Substances 0.000 claims description 8
- 229910001220 stainless steel Inorganic materials 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 3
- 230000018044 dehydration Effects 0.000 abstract description 15
- 238000006297 dehydration reaction Methods 0.000 abstract description 15
- 230000000694 effects Effects 0.000 abstract description 8
- 238000005265 energy consumption Methods 0.000 abstract 1
- 239000005416 organic matter Substances 0.000 abstract 1
- 238000001914 filtration Methods 0.000 description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 239000010802 sludge Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000001962 electrophoresis Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model relates to a filter -pressing technical field, concretely relates to filter is suppressed to electroosmosis high pressure, including entablature, portable beam, bottom end rail on, mould, well mould, lower mould, drive device and electroosmosis equipment, the utility model discloses an above structure, suppress this mechanical dewatering mode of the mode of straining to the high pressure and electroosmosis dehydration mode combines effectively, the mass dryness fraction of dehydration back material has been improved widely, especially, to biochemical mud, the mud that organic matter content is high, dewatering effect is showing more, furthermore, the mould is gone up in its activity and well mould can reciprocate, feed, filter -pressing and the process of unloading are simple and convenient, utilize the drive power of oil pressure unit and the weight of portable beam and last mould self to carry out filter -pressing and pressurize, save energy consumption 30% -50%.
Description
Technical field
The utility model relates to pressure filtering technique field, is specifically related to a kind of osmosis High Voltage pressure filter.
Background technology
Pressure filter is a kind of industrial equipments conventional in environmental technology field, and the sewage of doping mud is separated into drier material and compares clean water after pressure filter.Volume of material greatly reduces, and convenient by bury or the form such as burning processes, water then owing to being separated various solid state component, or is directly recycled, or is further processed rear recycling, and directly discharges.
But, by the water ratio of the material after pressure filter mechanical dehydration of the prior art or higher, especially for chemical sludge and the very high mud of organic content, moisture in this mud is difficult to be disposed by the mode of mechanical expression, if the moisture in these mud is not removed the cost that can increase post-processed and burn, workload and the cost of later stage harmless treatment can be increased.
Utility model content
The purpose of this utility model is for weak point of the prior art, a kind of osmosis High Voltage pressure filter is provided, effectively this mechanical dehydration mode of High Voltage press filtration mode and electroosmotic dewatering mode is combined, greatly increase the mass dryness fraction of the rear material of dehydration, especially for biochemical sludge, mud that organic content is high, dehydrating effect is more remarkable, and have efficiency high, structure is simple, cost is low, and highly little, be convenient to install, low power consumption and other advantages.
For achieving the above object, the utility model is achieved through the following technical solutions:
A kind of osmosis High Voltage pressure filter, comprise top end rail, moved cross beam, bottom end rail, patrix, middle mould, counterdie and driving arrangement, described top end rail is fixedly connected with the column of bottom end rail by multiple vertical setting; Described moved cross beam and middle mould are installed on described column, and are provided with pilot hole, and described pilot hole matches with described column, and described moved cross beam and middle mould can be moved up and down along described column, and described moved cross beam is placed in the top of described mould;
Described driving arrangement comprises upper cylinder and lower oil cylinder; Described upper cylinder is fixed on described top end rail, drives described moved cross beam to move up and down; Described lower oil cylinder is fixed on described bottom end rail, drives described middle mould to move up and down;
Described middle mould is provided with the die cavity being communicated with upper and lower two ends, and described patrix is fixed on the lower end of described moved cross beam, and described counterdie is fixed on the upper end of described bottom end rail, and described upper die and lower die can be placed in described die cavity, makes described die cavity form enclosed housing; The upper end of the lower end and/or described counterdie that are individually fixed in described patrix is provided with filter cloth; The lower end of described patrix and/or the upper end of described counterdie are provided with multiple for the through hole through drainage;
Also comprise osmosis equipment, described osmosis equipment comprises battery lead plate and pulse dc power, described battery lead plate comprises negative plate and positive plate, described positive plate is located at the lower end of described upper film, the upper end of described lower film is located at by described negative plate, described positive plate and negative plate are in the inner side of filter cloth respectively, and described positive plate and negative plate are respectively equipped with terminal stud.
The material of described battery lead plate is 316 model stainless steels after titanizing process, and its thickness is not less than 0.8mm.
Described positive plate and cathode plate surface are respectively equipped with perforate, and the size and number of described perforate is corresponding with the drainage through hole of the lower end of described upper film and the lower end of described lower film respectively.
Described terminal stud adopts silver-plated 316L stainless steel plate, is welded on described battery lead plate.
The position alignment parallel to each other of described negative plate and positive plate.
Described upper die and lower die and die cavity are cylindrical, and the sidewall of described patrix and described counterdie is provided with sealing-ring.
Described upper cylinder is fixed on the middle part of described top end rail, acts on the upper end center of described moved cross beam; Described lower oil cylinder is multiple, is individually fixed in the edge of described bottom end rail, acts on the edge of described middle mould.
Also comprise limiting device, comprise slide bar and multiplely detect the infrared detector that described moved cross beam and described middle mould move up and down position respectively; Described slide bar two ends are individually fixed in described top end rail and bottom end rail, are arranged in the side of described moved cross beam and mould; Described infrared detector is slidably installed on slide rail, also comprises operating device, is connected with described limiting device and driving arrangement.
Also comprise discharging platform, described counterdie is fixed on described discharging platform, and described discharging platform is by guide rails assembling in described bottom end rail, and described guide rail extends from the side and protrudes from described bottom end rail, and described discharging platform is provided with flip horizontal mechanism.
Also comprise the topping up case that hydraulic efficiency oil is provided to described upper cylinder and lower oil cylinder, be fixed on described top end rail, also comprise automatic draining mechanism, be communicated with described through hole.
The utility model is by above structure, effectively this mechanical dehydration mode of High Voltage press filtration mode and electroosmotic dewatering mode are combined, greatly increase the mass dryness fraction of the rear material of dehydration, " free water " and " Bound moisture " in mud is separated simultaneously from mud, achieve high-level efficiency dehydration, because osmosis can make the most difficult separated " Bound moisture " in material to be thoroughly separated, thus the material mass dryness fraction after dehydration is improved greatly, and the later material self that dewaters also has certain waste heat, more can take away a part of moisture content, particularly for biochemical sludge, the mud that organic content is high, dehydrating effect is more remarkable, device height is little, be convenient to install, cost is low.
Accompanying drawing explanation
Fig. 1 is the front elevational schematic of a kind of example of the present utility model.
Fig. 2 is the enlarged diagram at A place in Fig. 1.
Wherein: top end rail 1, moved cross beam 2, bottom end rail 3, discharging platform 31, patrix 4, middle mould 5, die cavity 51, counterdie 6, upper cylinder 71, lower oil cylinder 72, sealing-ring 73, column 74, guide rail 75, topping up case 76, filter cloth 77, through hole 78, slide bar 81, infrared detector 82, operating device 9, negative plate 91, positive plate 92.
Embodiment
The utility model is described in further detail with the following Examples.
As shown in Figure 1, a kind of osmosis High Voltage pressure filter, comprises top end rail 1, moved cross beam 2, bottom end rail 3, patrix 4, middle mould 5, counterdie 6, osmosis equipment and driving arrangement;
Described top end rail 1 is fixedly connected with the column 74 of bottom end rail 3 by multiple vertical setting; Described moved cross beam 2 and middle mould 5 are installed on described column 74, and are provided with pilot hole, and described pilot hole matches with described column 74, and described moved cross beam 2 and middle mould 5 can be moved up and down along described column, and described moved cross beam 2 is placed in the top of described mould 5;
Described driving arrangement comprises upper cylinder 71 and lower oil cylinder 72; Described upper cylinder 71 is fixed on described top end rail 1, drives described moved cross beam 2 to move up and down, and the operating pressure of described upper cylinder 71 is 25Mpa-30Mpa; Described lower oil cylinder 72 is fixed on described bottom end rail 3, drives described middle mould 5 to move up and down;
Described middle mould 5 is provided with the die cavity 51 being communicated with upper and lower two ends, described patrix 4 is fixed on the lower end of described moved cross beam 2, described counterdie 6 is fixed on the upper end of described bottom end rail 3, and described patrix 4 and counterdie 6 can be placed in described die cavity 51, makes described die cavity 51 form enclosed housing; As depicted in figs. 1 and 2, the upper end of the lower end and/or described counterdie 6 that are individually fixed in described patrix 4 is provided with filter cloth 77; As depicted in figs. 1 and 2, the lower end of described patrix 4 and/or the upper end of described counterdie 6 are provided with multiple for the through hole 78 through drainage.
Also comprise osmosis equipment, described osmosis equipment comprises battery lead plate and pulse dc power, described battery lead plate comprises negative plate 91 and positive plate 92, described positive plate is located at the lower end of described upper film 4, the upper end of described lower film 6 is located at by described negative plate, described positive plate 92 and negative plate 91 are in the inner side of filter cloth respectively, and described positive plate 92 and negative plate 91 are respectively equipped with terminal stud.
The material of described battery lead plate is 316 model stainless steels after titanizing process, and its thickness is not less than 0.8mm.
Described positive plate and cathode plate surface are respectively equipped with perforate, and the size and number of described perforate is corresponding with the drainage through hole of the lower end of described upper film and the lower end of described lower film respectively, ensure drainage effect.
Described terminal stud adopts silver-plated 316L stainless steel plate, improves its conductive capability, is welded on described battery lead plate.
The position alignment parallel to each other of described negative plate 92 and positive plate 91, makes electroosmotic dewatering effect better.
Working process:
Fill process: described lower oil cylinder 72 drives described middle mould 5 to decline, described counterdie 6 is made to be placed in described die cavity 51, described upper cylinder 71 drives described moved cross beam 2 to rise, and makes described patrix 4 depart from described die cavity 51, is filled in described die cavity 51 by material from described die cavity 51 upper end;
Pressure-filtering process: described patrix 4 declines, the weight of the power utilizing described upper cylinder 72 to provide and described patrix 4 and moved cross beam 2 self, extrude described material, suppress with height and press filtration is carried out to described material, mechanical dehydration is carried out to material, simultaneously, positive pole and the negative pole of pulse dc power is connected respectively on described positive plate 92 and described negative plate 91, pulse direct current is led to the material in film chamber 51, carry out electroosmotic dewatering, electroosmotic dewatering technology is the opinion of managing according to " electrophoresis ", to make in film chamber 51 the water molecules formed in filter cake carry out displacement, mechanical dehydration and electroosmotic dewatering are combined, the water molecules of the material in whole film chamber 51 is evenly distributed, substantially increase the speed of dehydration, greatly reduce the water ratio of material simultaneously, particularly for biochemical sludge, mud that organic content is high, dehydrating effect is more remarkable,
And, electroosmotic dewatering passes into electric current under the state of moisture existence, equipment arranges several insulation layer and ensures as safety and deodorization around alive part, in dehydration, sludge odor burst size is very little, in dehydration filter residue, water ratio reduces, foul smell alleviates, so the body refuse foul smell of osmosis is lighter; After dehydration, filtrate directly can be back to Sewage treatment systems, guarantees that non-secondary pollution hidden danger exists;
Described filter cloth 77 makes the moisture in described material depart from from described material, and is discharged by described through hole 78.
Discharge process: described patrix 4 and described moved cross beam 2 rise, makes the described material after press filtration depart from described die cavity 51 from lower end, then by described material removal.
As shown in Figure 1, described patrix 4, counterdie 4 and die cavity 51 is cylindrical.Tooling cost is little, and in pressure-filtering process, makes described material without pressure dead angle.
As depicted in figs. 1 and 2, the sidewall of described patrix 4 and described counterdie 6 is provided with sealing-ring 73.In pressure-filtering process, make described die cavity 51 keep sealed state, improve press filtration effect.
As shown in Figure 1, described upper cylinder 71 is fixed on the middle part of described top end rail 1, acts on the upper end center of described moved cross beam 2; Described lower oil cylinder 72 is multiple, is individually fixed in the edge of described bottom end rail 3, acts on the edge of described middle mould 5.
As shown in Figure 1, also comprise limiting device, comprise slide bar 81 and multiplely detect the infrared detector 82 that described moved cross beam 2 and described middle mould 5 move up and down position respectively; Described slide bar 81 two ends are individually fixed in described top end rail 1 and bottom end rail 3, are arranged in the side of described moved cross beam 2 and mould 5; Described infrared detector 82 is slidably installed on described slide rail 81.
Described infrared detector 82 detects described moved cross beam 2 and middle mould 5 upper and lower end face, thus determines the position of described moved cross beam 2 and middle mould 5, accurately to control translational speed and the braking of described moved cross beam 2 and middle mould 5.
As shown in Figure 1, also comprise operating device 9, be connected with described limiting device and driving arrangement.The pressure of described upper cylinder 71 and lower oil cylinder 72, driving velocity and dwell time is controlled respectively by described operating device 9, by receiving the position of described moved cross beam 2 that described infrared detector 82 detects and middle mould 5, thus accurately control described moved cross beam 2 and middle mould 5 stroke, quick travel district and turnover zone at a slow speed.
As shown in Figure 1, also comprise discharging platform 31, described counterdie 6 is fixed on described discharging platform 31, and described discharging platform 31 is installed on described bottom end rail 3 by guide rail 75, and described guide rail 75 extends from the side and protrudes from described bottom end rail 3.After completing press filtration, described discharging platform 31 is skidded off by guide rail 75, then by the material removal after press filtration on described counterdie 6, make discharge process convenient, improve discharge rate.
Described discharging platform 31 is provided with flip horizontal mechanism.After skidding off described discharging platform 31, overturn described counterdie 6, make its lower surface down, be convenient to clear up material, in Figure of description, do not provide structure iron.
As shown in Figure 1, also comprise the topping up case 76 that hydraulic efficiency oil is provided to described upper cylinder 71 and lower oil cylinder 72, be fixed on described top end rail 1.
Also comprise automatic draining mechanism, be communicated with described through hole 78, in Figure of description, do not provide structure iron.Automatic clearance drainage, raises the efficiency.
Finally should be noted that; the restriction of above embodiment only for illustration of the technical solution of the utility model but not to the utility model protection domain; although be explained in detail the utility model with reference to preferred embodiment; those of ordinary skill in the art is to be understood that; can modify to the technical solution of the utility model or equivalent replacement, and not depart from essence and the scope of technical solutions of the utility model.
Claims (10)
1. an osmosis High Voltage pressure filter, comprises top end rail, moved cross beam, bottom end rail, patrix, middle mould, counterdie and driving arrangement, and described top end rail is fixedly connected with the column of bottom end rail by multiple vertical setting; Described moved cross beam and middle mould are installed on described column, and are provided with pilot hole, and described pilot hole matches with described column, and described moved cross beam and middle mould can be moved up and down along described column, and described moved cross beam is placed in the top of described mould;
Described driving arrangement comprises upper cylinder and lower oil cylinder; Described upper cylinder is fixed on described top end rail, drives described moved cross beam to move up and down; Described lower oil cylinder is fixed on described bottom end rail, drives described middle mould to move up and down;
Described middle mould is provided with the die cavity being communicated with upper and lower two ends, and described patrix is fixed on the lower end of described moved cross beam, and described counterdie is fixed on the upper end of described bottom end rail, and described upper die and lower die can be placed in described die cavity, makes described die cavity form enclosed housing; The upper end of the lower end and/or described counterdie that are individually fixed in described patrix is provided with filter cloth; The lower end of described patrix and/or the upper end of described counterdie are provided with multiple for the through hole through drainage;
It is characterized in that: also comprise osmosis equipment, described osmosis equipment comprises battery lead plate and pulse dc power, described battery lead plate comprises negative plate and positive plate, described positive plate is located at the lower end of described patrix, the upper end of described counterdie is located at by described negative plate, described positive plate and negative plate are in the inner side of filter cloth respectively, and described positive plate and negative plate are respectively equipped with terminal stud.
2. a kind of osmosis High Voltage pressure filter according to claim 1, is characterized in that: the material of described battery lead plate is 316 model stainless steels after titanizing process, and its thickness is not less than 0.8mm.
3. a kind of osmosis High Voltage pressure filter according to claim 1, it is characterized in that: described positive plate and cathode plate surface are respectively equipped with perforate, the size and number of described perforate is corresponding with the drainage through hole of the lower end of described upper film and the lower end of described lower film respectively.
4. a kind of osmosis High Voltage pressure filter according to claim 1, is characterised in that: described terminal stud adopts silver-plated 316L stainless steel plate, is welded on described battery lead plate.
5. a kind of osmosis High Voltage pressure filter according to claim 1, is characterized in that: the position alignment parallel to each other of described negative plate and positive plate.
6. a kind of osmosis High Voltage pressure filter according to claim 1, is characterized in that: described upper die and lower die and die cavity are cylindrical, and the sidewall of described patrix and described counterdie is provided with sealing-ring.
7. a kind of osmosis High Voltage pressure filter according to claim 1, is characterized in that: described upper cylinder is fixed on the middle part of described top end rail, acts on the upper end center of described moved cross beam; Described lower oil cylinder is multiple, is individually fixed in the edge of described bottom end rail, acts on the edge of described middle mould.
8. a kind of osmosis High Voltage pressure filter according to claim 1, is characterized in that: also comprise limiting device, comprises slide bar and multiplely detects the infrared detector that described moved cross beam and described middle mould move up and down position respectively; Described slide bar two ends are individually fixed in described top end rail and bottom end rail, are arranged in the side of described moved cross beam and mould; Described infrared detector is slidably installed on slide rail, also comprises operating device, is connected with described limiting device and driving arrangement.
9. a kind of osmosis High Voltage pressure filter according to claim 1, it is characterized in that: also comprise discharging platform, described counterdie is fixed on described discharging platform, described discharging platform by guide rails assembling in described bottom end rail, described guide rail extends from the side and protrudes from described bottom end rail, and described discharging platform is provided with flip horizontal mechanism.
10. a kind of osmosis High Voltage pressure filter according to claim 1, is characterized in that: also comprise the topping up case providing hydraulic efficiency oil to described upper cylinder and lower oil cylinder, be fixed on described top end rail, also comprise automatic draining mechanism, be communicated with described through hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520942937.0U CN205115110U (en) | 2015-11-23 | 2015-11-23 | Filter is suppressed to electroosmosis high pressure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520942937.0U CN205115110U (en) | 2015-11-23 | 2015-11-23 | Filter is suppressed to electroosmosis high pressure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205115110U true CN205115110U (en) | 2016-03-30 |
Family
ID=55570734
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520942937.0U Active CN205115110U (en) | 2015-11-23 | 2015-11-23 | Filter is suppressed to electroosmosis high pressure |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205115110U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105859103A (en) * | 2016-06-21 | 2016-08-17 | 饶宾期 | Sewage sludge dehydrating device based on electroosmosis and mechanical pressure filtration coupling |
| CN105923977A (en) * | 2016-06-21 | 2016-09-07 | 饶宾期 | Electroosmosis and pressure filtration coupled sewage sludge dehydrating device |
| CN106396303A (en) * | 2016-06-21 | 2017-02-15 | 饶宾期 | A sewage and sludge dehydrating device coupling electroosmosis and mechanical pressure filtration |
| CN108314281A (en) * | 2018-01-22 | 2018-07-24 | 浙江工业大学 | A kind of high-voltage pulse electrode system of electrolysis processing deeply dehydrating sludge |
| CN110422956A (en) * | 2019-07-15 | 2019-11-08 | 湖南大学 | A kind of shield slurry dehydration device |
| CN114702223A (en) * | 2022-06-02 | 2022-07-05 | 山东祥龙新材料股份有限公司 | Sludge dewatering treatment device |
-
2015
- 2015-11-23 CN CN201520942937.0U patent/CN205115110U/en active Active
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105859103A (en) * | 2016-06-21 | 2016-08-17 | 饶宾期 | Sewage sludge dehydrating device based on electroosmosis and mechanical pressure filtration coupling |
| CN105923977A (en) * | 2016-06-21 | 2016-09-07 | 饶宾期 | Electroosmosis and pressure filtration coupled sewage sludge dehydrating device |
| CN106396303A (en) * | 2016-06-21 | 2017-02-15 | 饶宾期 | A sewage and sludge dehydrating device coupling electroosmosis and mechanical pressure filtration |
| CN105859103B (en) * | 2016-06-21 | 2018-08-17 | 中国计量大学 | The sewage sludge dehydration device coupled with mechanism filter-pressing based on electro-osmosis |
| CN106396303B (en) * | 2016-06-21 | 2019-03-26 | 中国计量大学 | The sewage sludge dehydration device that electro-osmosis is coupled with mechanism filter-pressing |
| CN105923977B (en) * | 2016-06-21 | 2019-03-26 | 中国计量大学 | The sewage sludge dehydration device of electro-osmosis filters pressing coupling |
| CN108314281A (en) * | 2018-01-22 | 2018-07-24 | 浙江工业大学 | A kind of high-voltage pulse electrode system of electrolysis processing deeply dehydrating sludge |
| CN110422956A (en) * | 2019-07-15 | 2019-11-08 | 湖南大学 | A kind of shield slurry dehydration device |
| CN114702223A (en) * | 2022-06-02 | 2022-07-05 | 山东祥龙新材料股份有限公司 | Sludge dewatering treatment device |
| CN114702223B (en) * | 2022-06-02 | 2022-08-09 | 山东祥龙新材料股份有限公司 | Sludge dewatering treatment device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205115110U (en) | Filter is suppressed to electroosmosis high pressure | |
| CN108101340A (en) | Mechanical expression carries the high mass dryness fraction dewatering of economic benefits and social benefits sewage sludge with air-flow | |
| CN104326641B (en) | Electroosmosis plate-frame sludge compressor and sludge treatment method | |
| CN104944646B (en) | Wastewater advanced treatment method coupling membrane and electricity | |
| CN1948193A (en) | Electric field synergistic mud dewatering method and its device | |
| CN107555754B (en) | Energy-saving electroosmosis sludge high-dryness dehydration method | |
| CN107686223A (en) | Electrochemistry deep dehydration device for sludge and deep dehydration method for sludge | |
| CN112607995B (en) | Continuous dewatering system of mud | |
| CN107381997B (en) | Electroosmosis filter pressing and sludge dewatering cooperated method | |
| CN104058567B (en) | A kind of electrodialysis oxidation style barrier film sheet frame sludge dewatering equipment | |
| CN102690039A (en) | Sludge dewatering device capable of implementing quick opening and closing | |
| CN107382023B (en) | Energy-saving electroosmosis sludge high-dryness dewatering system | |
| CN107381996B (en) | Electroosmosis filter-pressing cooperated sludge dewatering device | |
| CN204939237U (en) | A kind of Electroosmosis sludge dewatering equipment | |
| CN203123645U (en) | Deep dewatering and molding integrated device for sludge | |
| CN205152036U (en) | Sludge thickener and drier combination | |
| CN218011389U (en) | Material extrusion dewatering system | |
| CN203212368U (en) | Electrochemical waste water treatment device | |
| CN110395871A (en) | It is separated by solid-liquid separation Treatment of Sludge filtering equipment | |
| CN103058486A (en) | Electrolytic squeezing device applied to dehydrator or deoiling machine | |
| CN102115302A (en) | Electrolytic filtering/squeezing integrated sludge dewatering machine | |
| CN203890209U (en) | Solar multidimensional electrode and microwave catalysis sludge power generation device | |
| CN207362023U (en) | A kind of electrochemistry deep dehydration device for sludge | |
| CN201534386U (en) | Press filtration dehydrator of domestic garbage | |
| CN210085229U (en) | Cathode and pressing belt integrated sludge electroosmosis belt type filter pressing device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20181119 Address after: 362200 No. 4 Kaiyuan Road, Jingbian Village, Cizao Town, Jinjiang City, Quanzhou City, Fujian Province Patentee after: Quanzhou Chuanglu Machinery Industry and Trade Co.,Ltd. Address before: 528000 Workshop of Zinanaobian Industrial Zone, Nanzhuang Town, Chancheng District, Foshan City, Guangdong Province Patentee before: FOSHAN JINKAIDI FILTRATION EQUIPMENT Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| CP03 | Change of name, title or address |
Address after: No. 20 Jinhe Avenue, Xiamei Town, Nan'an City, Quanzhou City, Fujian Province Patentee after: Fujian Chuangli Machinery Co.,Ltd. Country or region after: China Address before: No. 4 Kaiyuan Road, Jingbian Village, Cizao Town, Jinjiang City, Quanzhou City, Fujian Province Patentee before: Quanzhou Chuanglu Machinery Industry and Trade Co.,Ltd. Country or region before: China |
|
| CP03 | Change of name, title or address |