CN207462809U - A kind of DC electric field combination vertical pressurization is high to contain interior water dehydration device - Google Patents
A kind of DC electric field combination vertical pressurization is high to contain interior water dehydration device Download PDFInfo
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- CN207462809U CN207462809U CN201721299200.7U CN201721299200U CN207462809U CN 207462809 U CN207462809 U CN 207462809U CN 201721299200 U CN201721299200 U CN 201721299200U CN 207462809 U CN207462809 U CN 207462809U
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- electric field
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Abstract
It is high containing interior water dehydration device the utility model discloses a kind of pressurization of DC electric field combination vertical, device includes press filtration component, DC electric field component and pressing mechanism, anode system is provided on the upside of the press filtration component, downside is provided with cathod system, the positive and negative anodes difference jointed anode system and cathod system of DC power supply, form DC electric field component, press filtration component is made to form the DC electric field environment for realizing electro-osmosis up and down, pressing mechanism applies Vertical Square to press filtration component and upwards pressure, by controlling its moulding pressure, pressing speed and pressing time and the conduction time of DC electric field component, it realizes and three-dimensional dehydration is carried out under mechanism filter-pressing and/or electro-osmosis filter pressing.
Description
Technical field
It is high containing interior water dehydration device the utility model is related to a kind of pressurization of DC electric field combination vertical.
Background technology
Water material in height, such as bacteria residue are dehydrated usually using the mode of press filtration, and existing filter-press dehydration operation is deposited
In following shortcoming:
The simple mechanical pressure by weight is dehydrated, and compression system is huge and not easy to control, is needed in construction especially
It takes care, while equipment investment cost is big;
Since equipment is huge, situations such as if there is failure or damage, it is not easy to repair;
Draining is uneven in pressure-filtering process, and efficiency is low, and the water content for be easy to causeing the filter cake after press filtration is uneven, is not conducive to
It is follow-up to use.
Former simple mechanical press filtration, since filter cake thickness is smaller, therefore whole efficiency is lower.
Utility model content
The utility model is to solve the above-mentioned problems, it is proposed that a kind of DC electric field combination vertical pressurization is high to be dehydrated containing interior water
Device, the utility model are combined electro-osmosis with box weight, can carry out adaptability according to material water ratio and physical characteristic
It adjusts, realizes dehydration, so as to optimize press filtration environment, improve overall efficiency, it is energy saving.
To achieve these goals, the utility model adopts the following technical solution:
A kind of pressurization of DC electric field combination vertical is high containing interior water dehydration device, including press filtration component, DC electric field component and
Pressing mechanism, the press filtration component upside are provided with anode system, and downside is provided with cathod system, the positive and negative anodes point of DC power supply
Other jointed anode system and cathod system form DC electric field component, and press filtration component is made to form the direct current for realizing electro-osmosis up and down
Electric field environment;
The anode system includes multiple anode stubs in array distribution, and anode stub, which extends downwardly, is uniformly arranged in press filtration
In the press filtration space of component, the cathod system includes multiple filtration net, is arranged in press filtration space;
The pressing mechanism applies Vertical Square to press filtration component and upwards pressure, by controlling its moulding pressure, pressurization speed
It degree and pressing time and the conduction time of DC electric field component, realizes and is carried out under mechanism filter-pressing and/or electro-osmosis filter pressing
Solid dehydration.
Further, the press filtration component includes conveyer belt and several press filtration baskets, and the press filtration basket is waited to take off to carry
Water material, and run on a moving belt, when press filtration basket stops at the lower end of pressing mechanism, press filtration basket provides press filtration space.
Further, the dehydration device further includes rack, and the pressing mechanism and DC electric field component are arranged at machine
On frame, and conveyer belt is fixed in rack, is replaced with transporting press filtration basket.
Further, the lower end of the dehydration device is additionally provided with shedding mechanism, with discharging press filtration basket.
Further, anode stub contact with cathode filter screen is bolted, and the bolt outer sheath is equipped with
Insulation sleeve plays insulating effect.
Further, the cathode filter screen is connected on insulating base, utilizes insulating base and fixed anode system
It insulate between rack.
Further, the cathode filter screen filtration mesh number is determined according to the characteristic of different material.
Further, the anode stub and cathode filter screen are uniformly distributed, and intersected with each other, are uniformly set on cathode filter screen
Multiple water outlets are equipped with, filter cake is made to form three-dimensional dehydration in pressure-filtering process, forms cellular structure.
Further, the current switching time of the DC electric field component or/and duration are according to material water ratio and physics
Characteristic is adjusted.
Method of work based on above device feeds to press filtration component, and then pressing mechanism starts to push material to centainly
Degree, DC power supply adjust moulding pressure, pressing speed and pressurization of the pressing mechanism in the vertical direction that press filtration component applies
Time and the conduction time of DC electric field component, in press filtration component after the completion of material press filtration, pressing mechanism raising is unloaded
Material after the completion of discharging, replaces press filtration component, carries out electro-osmosis pressure-filtering process again.
When carrying out press filtration, the mechanism filter-pressing and electro-osmotic pressure that are applied according to the type and water content of material, pressing mechanism
Filter is used in combination or is used alone.
Compared with prior art, the beneficial effects of the utility model are:
(1) the utility model is combined box weight with electro-osmosis technology, and anode and cathod system are in material pressure process
In can be powered simultaneously, and conduction time can be adjusted, moulding pressure can be adjusted, and pressing time can be adjusted, thus this
Utility model can change filter-pressing process at any time according to different materials;
(2) anode system is made of multiple anode stubs, and cathod system is made of multiple sintering filter screens.And the two Cheng Jun
Even arrangement, for material in pressure-filtering process, draining is uniform, and anode stub and cathode filter screen are uniformly distributed, and intersected with each other, and filter cake exists
Three-dimensional dehydration is formed in pressure-filtering process, i.e., filter cake surrounding is dehydrated by cathode filter screen, helps to improve filter cake Homogeneous Aqueous
Rate improves dehydration efficiency, improves overall equipment efficiency.comprehensive efficiency of equipment;
(3) it can be equipped with multiple press filtration baskets simultaneously, carry out press filtration or charging, do not delay operating mode, improve material efficiency of press filtering;
(4) press-area is dehydrated by being sintered filter screen, forms three-dimensional dehydration, i.e. cellular structure is dehydrated.It is significantly excellent
Change squeezing environment, improve dehydration efficiency, it is energy saving.
Description of the drawings
The accompanying drawings which form a part of this application are used for providing further understanding of the present application, and the application's shows
Meaning property embodiment and its explanation do not form the improper restriction to the application for explaining the application.
Fig. 1 is the utility model structure diagram;
Fig. 2 is the structure bottom view of the utility model;
Fig. 3 is the cathod system schematic diagram of the utility model;
Fig. 4 is that the anode system of the utility model and cathod system arrange schematic diagram;
Wherein:1st, compression system, 2, anode system, 3, electro-osmosis press filtration basket, 4, running gear, 5, rack, 6, discharging system
System, 7, cathod system, 8, cathode filtration core, 9, anode carbon steel rod, 10, cathode sintering filter screen.
Specific embodiment:
The utility model is described in further detail with embodiment below in conjunction with the accompanying drawings.
It is noted that following detailed description is all illustrative, it is intended to provide further instruction to the application.It is unless another
It indicates, all technical and scientific terms used herein has usual with the application person of an ordinary skill in the technical field
The identical meanings of understanding.
It should be noted that term used herein above is merely to describe specific embodiment, and be not intended to restricted root
According to the illustrative embodiments of the application.As used herein, unless the context clearly indicates otherwise, otherwise singulative
It is also intended to include plural form, additionally, it should be understood that, when in the present specification using term "comprising" and/or " packet
Include " when, indicate existing characteristics, step, operation, device, component and/or combination thereof.
In the utility model, term as " on ", " under ", "left", "right", "front", "rear", " vertical ", " level ",
The orientation or position relationship of the instructions such as " side ", " bottom " are based on orientation shown in the drawings or position relationship, only to facilitate chatting
State each component of the utility model or component structure relationship and determining relative, not refer in particular in the utility model either component or
Element, it is impossible to be construed as a limitation of the present invention.
In the utility model, term such as " affixed ", " connected ", " connection " should be interpreted broadly, and expression can be fixed
It connects or is integrally connected or is detachably connected;It can be directly connected, the indirect phase of intermediary can also be passed through
Even.Related scientific research or technical staff for this field can determine above-mentioned term in the utility model as the case may be
Concrete meaning, it is impossible to be construed as a limitation of the present invention.
As background technology is introduced, the not high deficiency of dehydrating effect exists in the prior art, in order to solve as above
Technical problem, present applicant proposes a kind of electro-osmosis technologies and the box weight dehydration device of machinery.
In a kind of typical embodiment of the application, as shown in Figure 1, being illustrated for carrying out wet bacteria slag dehydration.
A kind of press perpendicular DC electric field bacteria residue desiccation apparatus is provided, it include compression system, anode system, cathod system, press filtration basket,
Running gear, discharge system, rack.The compression system pressurizes for hydraulic control oil cylinder and pressure release, and anode system is by carbon steel
Plate pressing plate and carbon stick composition, cathod system are made of sintering filter screen, and running gear is made of guide rail, oil cylinder, discharge system
It is made of oil cylinder, lower push plate.The carbon steel plate pressing plate and sintering that DC electric field positive and negative anodes are respectively turned in the utility model filter
Wet bacteria slag is directly clamped between net, press-area is dehydrated by being sintered filter screen, forms three-dimensional dehydration, i.e., cellular structure takes off
Water.Optimization squeezing environment significantly improves dehydration efficiency, energy saving.
As shown in Fig. 2, a kind of bacteria residue dehydration device combined based on electro-osmosis with box weight, including compression system, sun
Electrode systems, cathod system, press filtration basket, running gear, discharge system, rack, DC power supply.It is characterized in that:The anode
System is arranged on the top of press filtration basket, and the cathod system is arranged on the lower part of press filtration basket, the DC power supply positive and negative anodes
It is powered and connects with anode system and cathod system respectively, apopore is equipped on the cathod system;The anode system
It is connect with hydraulic system;Multiple anode stubs are provided on the anode system, the anode stub extends downwardly uniform arrangement
In in press filtration basket, anode stub is connected with the anode of DC power supply, and cathod system is connected with the cathode of DC power supply.Its Anodic with
What cathode contacts were connected with, connection bolt sleeve is played insulating effect in inside using nylon jacket.Cathode is sintered filter screen
It is connected on nylon bottom plate, is insulated using nylon bottom plate and anode rack.
Box weight is combined with electro-osmosis technology.Anode and cathod system can be powered simultaneously in material pressure process,
And conduction time can be adjusted, and moulding pressure can be adjusted, and pressing time can be adjusted.It can be according to different materials, at any time
Change filter-pressing process.Such as first mechanism filter-pressing, then it is powered again.Or the mechanism filter-pressing again that is first powered.Or mechanism filter-pressing and energization
Interval carries out.
Cathod system is made of sintering filter screen, as shown in figure 3, sintering filter screen is formed with 5 layers of filter layer, filters mesh number
It can be customized according to the characteristic of different material.Sintering filter screen is uniformly distributed in bottom base panel, and separated with rack with insulation board.
Sintering filter screen is made by stainless steel material, and in the high material of moisture content, usage time can lengthen, and convenient for safeguarding.It crosses
Filter screen bottom is threadedly coupled with bottom plate, easy to disassemble, convenient for cleaning.Bottom plate is insulated using nylon sheet.Accomplish that equipment was run
Ensure personnel safety in journey.
As shown in Figure 1, two press filtration baskets of configuration.Such first press filtration basket is in material pressure-filtering process, second press filtration
Basket can feed.After first press filtration basket discharging, second press filtration basket is run to pressing position by running gear, is carried out
Pressurization press filtration.First press filtration basket can feed.Do not delay opportunity in this way, improve material efficiency of press filtering.
Anode system is made of multiple anode stubs, and cathod system is made of multiple sintering filter screens.And the two is into uniform
Arrangement.As shown in figure 4, material, in pressure-filtering process, draining is uniform.Anode stub and cathode filter screen are uniformly distributed, and hand over each other
Fork.Filter cake forms three-dimensional dehydration in pressure-filtering process, i.e., filter cake surrounding is dehydrated by cathode filter screen.Filter cake is improved uniformly to contain
Water rate improves dehydration efficiency, improves overall equipment efficiency.comprehensive efficiency of equipment.
Specific workflow is:It is fed first to first press filtration basket, then compression system starts to push material to centainly
Degree.DC power supply is opened, and carries out electro-osmosis for a period of time, closes DC power supply.Compression system pushes material to centainly again
Degree carries out electro-osmosis for a period of time, closes DC power supply.This process can be adjusted according to material water ratio and physical characteristic
Section.Compression system is run by HYDRAULIC CONTROL SYSTEM first, and operating pressure and the speed of service can be adjusted.Secondly DC power supply is powered
Time can be adjusted.It can obtain a more satisfactory state by many experiments in this way.When i.e. compression system is run
Between, conduction time, pressure size can be adjusted respectively.So as in the case where material water ratio obtains desired value, control respectively
Each parameter.So as to optimize press filtration environment significantly, overall efficiency is improved, it is energy saving.Simultaneously in pressure-filtering process, second press filtration
Basket can feed.Improve equipment whole efficiency.
In first press filtration basket after the completion of material press filtration, compression system raising.Discharge system carries out discharging.Discharging is completed
Afterwards, running gear is run, and second press filtration basket is made to run to below compression system.Carry out electro-osmosis pressure-filtering process.Then it repeats
Above procedure completes equipment overall operation.Wherein material is shifted onto press filtration basket top by discharge system for push plate under lower oil cylinder pushing.
The compression system and discharge system and running gear of the utility model use existing device, and such as machinery adds
Pressure device, discharging robot and conveyer belt etc..Details are not described herein again.
Wet bacteria slag is replaced with unclassified stores, such as High water cut briquette by the another embodiment of the utility model, according to
Material water ratio and physical characteristic are configured moulding pressure, the speed of service and DC power supply conduction time and duration.
The foregoing is merely the preferred embodiments of the application, are not limited to the application, for the skill of this field
For art personnel, the application can have various modifications and variations.It is all within spirit herein and principle, made any repair
Change, equivalent replacement, improvement etc., should be included within the protection domain of the application.
It is above-mentioned although specific embodiments of the present invention are described with reference to the accompanying drawings, but not to this practicality newly
The limitation of type protection domain, those skilled in the art should understand that, on the basis of the technical solution of the utility model, ability
Field technique personnel do not need to make the creative labor the various modifications or changes that can be made still in the protection model of the utility model
Within enclosing.
Claims (10)
1. a kind of DC electric field combination vertical pressurization is high containing interior water dehydration device, it is characterized in that:Including press filtration component, DC electric field
Component and pressing mechanism, the press filtration component upside are provided with anode system, and downside is provided with cathod system, and DC power supply is just
Cathode distinguishes jointed anode system and cathod system, forms DC electric field component, and press filtration component is made to be formed up and down and realizes electro-osmosis
DC electric field environment;
The anode system includes multiple anode stubs in array distribution, and anode stub, which extends downwardly, is uniformly arranged in press filtration component
Press filtration space in, the cathod system include multiple filtration net, be arranged in press filtration space;
The pressing mechanism to press filtration component apply Vertical Square upward pressure, by control its moulding pressure, pressing speed with
Pressing time and the conduction time of DC electric field component are realized and solid are carried out under mechanism filter-pressing and/or electro-osmosis filter pressing
Dehydration.
2. a kind of DC electric field combination vertical pressurization as described in claim 1 is high containing interior water dehydration device, it is characterized in that:It is described
Press filtration component includes conveyer belt and several press filtration baskets, and the press filtration basket is transported on a moving belt to carry material to be drained off
Row, when press filtration basket stops at the lower end of pressing mechanism, press filtration basket provides press filtration space.
3. a kind of DC electric field combination vertical pressurization as described in claim 1 is high containing interior water dehydration device, it is characterized in that:It is described
Dehydration device further includes rack, and the pressing mechanism and DC electric field component are arranged in rack, and biography is fixed in rack
Band is sent, is replaced with transporting press filtration basket.
4. a kind of DC electric field combination vertical pressurization as claimed in claim 3 is high containing interior water dehydration device, it is characterized in that:It is described
The lower end of dehydration device is additionally provided with shedding mechanism, with discharging press filtration basket.
5. a kind of DC electric field combination vertical pressurization as described in claim 1 is high containing interior water dehydration device, it is characterized in that:It is described
Anode stub contact with cathode filter screen is bolted, and the bolt outer sheath is equipped with insulation sleeve, plays insulating effect.
6. a kind of DC electric field combination vertical pressurization as described in claim 1 is high containing interior water dehydration device, it is characterized in that:It is described
Cathode filter screen is connected on insulating base, using insulating between the rack of insulating base and fixed anode system.
7. a kind of DC electric field combination vertical pressurization as described in claim 1 is high containing interior water dehydration device, it is characterized in that:It is described
Cathode filter screen filtration mesh number is determined according to the characteristic of different material.
8. a kind of DC electric field combination vertical pressurization as described in claim 1 is high containing interior water dehydration device, it is characterized in that:It is described
Anode stub and cathode filter screen are uniformly distributed, and intersected with each other, and multiple water outlets are evenly arranged on cathode filter screen, make filter cake
Three-dimensional dehydration is formed in pressure-filtering process, forms cellular structure.
9. a kind of DC electric field combination vertical pressurization as described in claim 1 is high containing interior water dehydration device, it is characterized in that:It is described
The current switching time of DC electric field component or/and duration are adjusted according to material water ratio and physical characteristic.
10. a kind of DC electric field combination vertical pressurization as described in claim 1 is high containing interior water dehydration device, it is characterized in that:Add
The mechanism filter-pressing and electro-osmosis press filtration that press mechanism applies are used in combination or are used alone.
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CN107551656A (en) * | 2017-10-10 | 2018-01-09 | 山东百川同创能源有限公司 | A kind of DC electric field combination vertical pressurization height contains interior water dehydration device and method |
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CN107551656A (en) * | 2017-10-10 | 2018-01-09 | 山东百川同创能源有限公司 | A kind of DC electric field combination vertical pressurization height contains interior water dehydration device and method |
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