CN103752057A - Vertical full-automatic microwave drying filter press - Google Patents

Vertical full-automatic microwave drying filter press Download PDF

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Publication number
CN103752057A
CN103752057A CN201410040212.2A CN201410040212A CN103752057A CN 103752057 A CN103752057 A CN 103752057A CN 201410040212 A CN201410040212 A CN 201410040212A CN 103752057 A CN103752057 A CN 103752057A
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filter
frame
plate
microwave
filtrate
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CN201410040212.2A
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CN103752057B (en
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陈爱民
陈长林
左敦稳
缪宏
华宝同
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Jiangsu New Hongda Group Co Ltd
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Jiangsu New Hongda Group Co Ltd
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Abstract

The invention relates to a vertical full-automatic microwave drying filter press which comprises a rack (2) and a plurality of filter pressing frame sets (5) arranged on the rack (2). The vertical full-automatic microwave drying filter press is characterized in that each filter pressing frame set (5) mainly comprises a filter frame plate (14), a filtrate frame (15), a diaphragm (11) and a hoarding (22); each filter frame plate (14) is arranged on the corresponding hoarding (22); each filtrate frame (15) is fixed on the corresponding filter frame plate (14); a filter plate grille (16) for supporting filter cloth (7) is mounted in each filtrate frame (15); in each filtrate frame (15), the lower part of the filter plate grille (16) is provided with an ultrasonic oscillating plate (17) and a microwave heater (20); one side of each microwave heater (20) is provided with a corresponding microwave controller (19); each microwave controller (19) is controlled by a temperature sensor (18) arranged on the corresponding diaphragm (11). The vertical full-automatic microwave drying filter press can greatly improve drying efficiency and shorten drying time consumption.

Description

Vertical type full automatic microwave drying filter press
Technical field
The present invention relates to a kind of solid-liquid separating equipment, especially a kind of vertical type blotter press, is specifically a kind ofly applied in the vertical type full automatic microwave drying filter press in Separation of Solid and Liquid pressure-filtering process by microwave drying technology.
Background technology
As everyone knows, filter press is take solid/liquid separation as object equipment, is widely used in the industries such as mine, oil, chemical industry, building materials, pharmacy, and brings into play the effect of wanting emphatically.According to the difference of material characteristic, current adoptable filter plant mainly contains horizontal belt filter, rotary drum vacuum filter, vane type filtration machine, vacuum type pressing filter, vertical type blotter press, horizontal pressure filter etc.Wherein vertical type blotter press is little because having floor space, and washing usefulness is high, and material filtering is effective, becomes the advantages such as cake speed is fast, and filter cake moisture is low, and disposal ability is large, and be used widely under large pressure reduction.
The filtration cakes torrefaction of the vertical type blotter press of domestic application is completed by compressed air at present, the air entering by distributing pipe has been full of filter chamber, mention barrier film, make the water of compaction on barrier film discharge filter press, by the air-flow of filter cake, reduce moisture and realize the dry of filter cake to optimum degree, but there is a lot of deficiencies in this filtration cakes torrefaction method, dry required time is long, dry not thorough, consumes energy high, efficiency is low, economical not.
And that heating using microwave has penetration is strong, the advantage that speed is fast and temperature is adjustable, but according to the knowledge of the applicant, have not yet to see the relevant report that organically combines, adopts microwave to heat filter cake both.
Summary of the invention
The object of the invention is mostly to adopt when filter cake is heated for existing vertical type blotter press compressed air to carry out, utilize circulation of air to realize drying purpose and have the problems such as speed is slow, filter cake internal moisture content is large, thus design a kind of by microwave heating technique and pressure filtering technique organically combine give full play to heating using microwave speed soon, the vertical type full automatic microwave drying filter press of high conformity.
Technical scheme of the present invention is:
A kind of vertical type full automatic microwave drying filter press, it comprises frame 2 and is arranged on the multiple press filtration frame groups 5 in frame 2, it is characterized in that described press filtration frame group 5 is mainly by filter frame plate 14, filtrate frame 15, barrier film 11 and coaming plate 22 form, described barrier film 11, the press filtration frame group 5 that coaming plate 22 is adjacent with bottom surrounds a filter chamber 10, described coaming plate 22 is provided with the feed pipe interface 13 that supplies filtrate and cleaning solution to enter filter chamber 10, between described barrier film 11 and filter frame plate 14, be provided with water under high pressure import 21, thereby water under high pressure from water under high pressure import 21 enter backward presses against diaphragm 11 liquid in filtrate in filter chamber 10 is extruded and is realized press filtration function, described filter frame plate 14 is arranged on coaming plate 22, and filtrate frame 15 is fixed on filter frame plate 14, and the filter plate grid 16 of supporting filter cloth 7 is installed in filtrate frame 15, in filtrate frame 15, the bottom of filter plate grid 16 is provided with supersonic oscillations plate 17 and microwave applicator 20, one side of each microwave applicator 20 is all fitted with corresponding microwave controller 19, and microwave controller 19 is controlled by the temperature sensor 18 being arranged on barrier film 11.
Four microwave applicators 20 of uniformly-spaced arranging are at least installed in described each press filtration frame group 5.
Described coaming plate 22 and the contact-making surface of barrier film and and the contact-making surface of the filtrate frame 15 of adjacent press filtration frame group 5 between sealing ring 23 is all installed.
The temperature of described microwave applicator 20 is adjustable, by the temperature of temperature sensor 18 on-line measurement filter cakes, realizes On-line Control.
Each filter frame of the present invention has filtration cakes torrefaction device, and described filtration cakes torrefaction device consists of microwave applicator 20, microwave controller 19, temperature sensor 18.Described microwave applicator 20 is at a distance of certain built-in being arranged in filtrate frame 15 in interval, on its side, is furnished with microwave controller 19, on it, be placed with filter plate grid 16, 7 of filter clothes are placed on filter plate grid 16, temperature sensor 18 is housed on diaphragm of rubber 11, filtration cakes torrefaction stage charging aperture 13 and floss hole are all closed and are formed airtight chamber 10, microwave carries out heat drying to filter cake, because the water in filter cake is subject to thermal evaporation, barrier film is lifted, the water under high pressure of secondary extrusion is got rid of from water under high pressure interface 21, microwave can be absorbed while penetrating filter cake inside, its energy is instantaneous to be transferred heat energy to and filter cake (comprising nexine filter cake and contained moisture thereof) entirety is heated up.Now, nexine water vapour pressure rises sharply, under the driving of this pressure, steam is got rid of to filter cake top layer, and first drying layer forms at filter cake internal layer, then expansion from inside to outside, realize the dry of filter cake, filtration cakes torrefaction device, according to the composition difference of filter cake, can be selected different power by microwave controller, temperature measurer (temperature sensor) is the temperature in on-line measurement filter chamber constantly, thereby realizes the On-line Control to dry operating temperature.
Beneficial effect of the present invention:
1. first the drying layer in vertical type full automatic microwave drying filter press filter cake dry run of the present invention forms at filter cake internal layer, then expansion from inside to outside, the moisture drying of filter cake is thorough, and dry cleansing is pollution-free, filter cake shortens whole drying time greatly, has improved operating efficiency.
2. vertical type full automatic microwave drying filter press of the present invention heating using microwave is instantaneous heating, therefore without thermal inertia, and easy operating, microwave drying technology easily-controlled operation, can realize continuous fully-automatic production.
3. vertical type full automatic microwave drying filter press of the present invention is according to the difference of filter cake composition, and heating using microwave can select different capacity to be dried, and realizes power adjustable, by temperature sensor and micro-.
4. microwave controller of the present invention can On-line Control baking temperature, therefore can avoid the waste of the energy.
5. the invention has been carried out organic combination by traditional filter press and microwave technology, can greatly improve drying efficiency, through evidence on year-on-year basis, can shorten more than 2/3rds drying time, be conducive to increase substantially production efficiency, shortened process is consuming time, simultaneously due to thoroughly dry, for improving end product quality successful.
Accompanying drawing explanation
Fig. 1 is the overall structure schematic diagram of vertical type blotter press of the present invention.
Fig. 2 is the structural representation of microwave drying filter frame group of the present invention unit.
Fig. 3 is the structural representation of facing of filter cloth cycling mechanism of the present invention.
Fig. 4 is the left TV structure schematic diagram of filter cloth cycling mechanism of the present invention.
Fig. 5 is the structural representation of filter cloth correction device of the present invention.
Fig. 6 is the structure chart of filter cloth cleaning device of the present invention.
In figure: 1-filter cloth cleaning device, 2-frame, 3-discharge tube, 4-slag bucket, 5-filter frame group, 6-hold-down mechanism, 7-filter cloth, 8-filter cloth drive unit, 9-filter cloth correction device, 10-filter chamber, 11-diaphragm of rubber, 12-sealing strip, 13-feed pipe interface, 14-filter frame plate, 15-filtrate frame, 16-filter plate grid, 17-supersonic oscillations plate, 18-temperature sensor, 19-microwave controller, 20-microwave applicator, 21-water under high pressure interface, 22-coaming plate, 23-sealing ring.
The specific embodiment
Below in conjunction with drawings and Examples, the present invention is further illustrated.
As shown in Figure 1-2.
A kind of vertical type full automatic microwave drying filter press, mainly by parts such as frame 2, multiple filter frame group 5, process pipeline 3, hold-down mechanism 6, filter cloth 7, filter cloth drive unit 8, filter cloth correction device 9, filter cloth cleaning device 1, slag bucket 4, wash mills, formed, as shown in Figure 1.The filter press of the present embodiment has adopted six operations altogether: pan feeding filtration-once extruding-ultrasonic washing-secondary extrusion-filtration cakes torrefaction-discharging, and for the ease of washing, therefore the pressure once pushing should be less than the pressure of secondary extrusion.Microwave drying press filtration frame group 5 as one of filter press critical component is mainly comprised of filter frame plate 14, filtrate frame 15, barrier film 11 and coaming plate 22, the press filtration frame group 5 that described barrier film 11, coaming plate 22 is adjacent with bottom surrounds a filter chamber 10, described coaming plate 22 is provided with the feed pipe interface 13 that supplies filtrate and cleaning solution to enter filter chamber 10, between described barrier film 11 and filter frame plate 14, be provided with water under high pressure import 21, thus water under high pressure from water under high pressure import 21 enter backward presses against diaphragm 11 liquid in filtrate in filter chamber 10 is extruded and is realized press filtration function, described filter frame plate 14 is arranged on coaming plate 22, and filtrate frame 15 is fixed on filter frame plate 14, and the filter plate grid 16 of supporting filter cloth 7 is installed in filtrate frame 15, in filtrate frame 15, the bottom of filter plate grid 16 is provided with supersonic oscillations plate 17 and microwave applicator 20, one side of each microwave applicator 20 is all fitted with corresponding microwave controller 19, microwave controller 19 is controlled by the temperature sensor 18 being arranged on barrier film 11, as shown in Figure 2, described barrier film 11, the press filtration frame group 5 that coaming plate 22 is adjacent with bottom surrounds a filter chamber 10, described coaming plate 20 is provided with the feed pipe interface 13 that supplies filtrate and cleaning solution to enter filter chamber 10, between described barrier film 11 and filter frame plate 14, be provided with water under high pressure import 18, thereby water under high pressure from water under high pressure import 18 enter backward presses against diaphragm 11 liquid in filtrate in filter chamber 10 is extruded and is realized press filtration function, described filter frame plate 14 is arranged on coaming plate 22, and filtrate frame 15 is fixed on filter frame plate 14, and the filter plate grid 16 of supporting filter cloth 7 is installed in filtrate frame 15, in filtrate frame 15, the bottom of filter plate grid 16 is provided with supersonic oscillations plate 17, five blocks of supersonic oscillations plates 17 and four microwave applicators 20 are at least installed in each press filtration frame group 5, the side of each microwave applicator 20 is all furnished with corresponding microwave controller 19, five blocks of supersonic oscillations plates 17 and four microwave applicators 20 are arranged in filtrate frame 15 at a distance of certain interleaved between the filtrate frame 15 of every filter frame and filter plate grid 16, its top has been placed with filter plate grid 16, and 7 of filter clothes are placed on filter plate grid 16.Microwave control cleaning solution enters filter chamber 10 from feed pipe interface 13, cleaning solution is filled with filter chamber 10, because liquid is filled with filter chamber 10, diaphragm of rubber 11 is lifted, the high-pressure extrusion water using during by press filtration is for the first time extruded from diaphragm of rubber 11 tops, cleaning solution enters delivery pipe after by filter cake and filter cloth 7, in this process, cleaning solution always contacts with supersonic oscillations plate 17, supersonic oscillations plate 17 produces ultrasonic wave, because supersonic oscillations plate 17 directly contacts with cleaning solution, ultrasonic wave is the propagation of density interphase in cleaning solution take cleaning solution as medium, due to nonlinear interaction, can produce cavitation, the shock wave sending when cavitation bubble is closed suddenly can produce thousands of atmospheric pressures around it, to pollution layer or the direct repeated stock of filter cake, in addition, ultrasonic vibration causes vibration velocity and the acceleration that particle is very large in cleaning solution, also make the dirt on filter cake and filter chamber surface be subject to frequent and fierce impact, thereby reached filter cake and the filter chamber cleaning performance of cleaning comprehensively, press filtration again after cleaning finishes, after finishing, press filtration carries out heating using microwave.Filter cake heating period feed pipe interface 13 and discharge tube 3 are all closed and are formed airtight chamber, microwave carries out heat drying to filter cake, because the water in filter cake is subject to thermal evaporation, diaphragm of rubber 11 is lifted, the water under high pressure of secondary extrusion is got rid of from water under high pressure interface, microwave penetrates filter cake and can be absorbed when inner, and its energy is instantaneous to be transferred heat energy to and filter cake (comprising nexine filter cake and contained moisture thereof) entirety is heated up.Now, nexine water vapour pressure rises sharply, under the driving of this pressure, steam is got rid of to material top layer, and first drying layer forms at filter cake internal layer, then expansion from inside to outside, realize the dry of filter cake, filtration cakes torrefaction device, according to the composition difference of filter cake, can be selected different power by microwave controller 19, temperature sensor 18 is the temperature in on-line measurement filter chamber constantly, thereby realizes the On-line Control to dry operating temperature.
Filter cloth 7 of the present invention is driven by filter cloth cycling mechanism, and cloth cycling mechanism is as shown in Fig. 3-6, and it is mainly by filter cloth drive unit 8, filter cloth correcting device 9, filter cloth cleaning device 1, removable deflector roll 12 ' and multiple cylinder deflector roll 10 ' form, as shown in Figure 2.Multiple cylinder deflector rolls 10 ' formed the work travel route of filter cloth 7, are all used filter cloth 7 two sides, filter residue 11 ' fall into from both sides slag bucket 4, removable deflector roll 12 in the course of the work ' make filter cloth 7 keep certain rate of tension.Removable deflector roll 12 ' be arranged on column 19 ' upper end in order to tensioner filter cloth 7, filter cloth drive unit 8 is arranged on column 19 ' lower end, a cylinder deflector roll 10 ' so that filter cloth 7 two sides are all used is respectively installed in each filter frame group 5 both sides, filter cloth cleaning device 1 is installed in the bottom of orlop filter frame group 5 and in the cloth side of entering of filter cloth drive unit 8, filter cloth correction device 9 is installed, filter cloth 7 from filter cloth drive unit 8 go out cloth side walk around removable deflector roll 12 ' enter in filter press main frame, each cylinder deflector roll 10 ' guiding under pass through successively each filter frame group 5, and from a side of orlop filter frame group 5, enter filter cloth cleaning device 1 fabric input mouth that enters filter cloth drive unit 8 after cleaning after 9 corrections of filter cloth deviation correcting device and enter next circulation.
During concrete enforcement, filter cloth drive unit 8 can adopt the structure shown in Fig. 3, also designed, designed as required, filter cloth drive unit shown in Fig. 3 mainly by left motor 15 ', right motor 18 ', belt 14 ', left driven roller 16 ', right driven roller 17 ', hold-down roller 13 ' composition, the left driven roller 16 of left motor 15 ' and right motor 18 ' by belt 14 ' drives correspondence separately ', right driven roller 17 ' rotation, and drive by the filter cloth 7 on their surfaces of hold-down roller 13 ' be pressed on and move, left motor 15 ' and right motor 18 ' rotating speed adjustable and be controlled by filter cloth correction device 9.Described filter cloth correcting device 9 mainly by two infrared generators 25 ' and two infrared receivers 24 ' and corresponding conventional control circuit form, two infrared generators 25 ' be arranged on respectively both sides of filter cloth, two infrared receivers 24 ' be also arranged on filter cloth 7 corresponding positions, both sides, infrared generator 25 ' and infrared receiver 24 ' be all contained on body 2 to limit the driving range of filter cloth 7, when filter cloth 7 sideslip, the infrared receiver 24 of one side ' will not receive infrared ray, so just control this side decelerating through motor, thereby two motor differentials make filter cloth 7 times just, as shown in Figure 4.Can designed, designed as the described filter cloth cleaning device 1 of one of water-saving result key technology, also can adopt the structure shown in Fig. 5, in Fig. 5, filter cloth cleaning device mainly by filter cloth clean upper deflector roll 23 ', filter cloth clean lower guide roll 20 ', water jet 21 ' and hairbrush 22 ' form, in filter cloth cyclic process filter cloth clean on deflector roll 23 ' and filter cloth clean lower guide roll 20 ' guide effect under filter cloth 7 from both sides hairbrush 22 ' between pass through, the water spray of water jet 21 ' constantly, hairbrush 22 ' effect under filter cloth 7 obtained effectively cleaning.
The cyclic process of whole filter cloth was driven by filter cloth drive unit 8 before this, through removable deflector roll 12 ' the realize tensioning of filter cloth, again by several cylinder deflector rolls 10 ' formation operating path, then through filter cloth cleaning device 1, filter cloth 7 is cleaned, finally by filter cloth correcting device 9, carry out tuningout and turn back to again on driven roller.
The part that the present invention does not relate to all prior art that maybe can adopt same as the prior art is realized.

Claims (4)

1. a vertical type full automatic microwave drying filter press, it comprises frame (2) and is arranged on the multiple press filtration frame groups (5) in frame (2), it is characterized in that described press filtration frame group (5) is mainly by filter frame plate (14), filtrate frame (15), barrier film (11) and coaming plate (22) composition, described barrier film (11), the press filtration frame group (5) that coaming plate (22) is adjacent with bottom surrounds a filter chamber (10), described coaming plate (22) is provided with the feed pipe interface (13) that supplies filtrate and cleaning solution to enter filter chamber (10), between described barrier film (11) and filter frame plate (14), be provided with water under high pressure import (21), water under high pressure from water under high pressure import (21) enter backward presses against diaphragm (11) thus the liquid in filtrate in filter chamber (10) is extruded and is realized press filtration function, it is upper that described filter frame plate (14) is arranged on coaming plate (22), and it is upper that filtrate frame (15) is fixed on filter frame plate (14), and the filter plate grid (16) of supporting filter cloth (7) is installed in filtrate frame (15), in filtrate frame (15), the bottom of filter plate grid (16) is provided with supersonic oscillations plate (17) and microwave applicator (20), one side of each microwave applicator (20) is all fitted with corresponding microwave controller (19), and microwave controller (19) is controlled by the temperature sensor (18) being arranged on barrier film (11).
2. vertical type full automatic microwave drying filter press according to claim 1, is at least provided with four microwave applicators (20) of uniformly-spaced arranging in the each press filtration frame group (5) described in it is characterized in that.
3. vertical type full automatic microwave drying filter press according to claim 1, it is characterized in that described coaming plate (22) and barrier film contact-making surface and and the contact-making surface of the filtrate frame (15) of adjacent press filtration frame group (5) between sealing ring (23) is all installed.
4. vertical type full automatic microwave drying filter press according to claim 1 and 2, is characterized in that the temperature of described microwave applicator (20) is adjustable, by the temperature of temperature sensor (18) on-line measurement filter cake, realizes On-line Control.
CN201410040212.2A 2014-01-28 2014-01-28 Vertical type full automatic microwave drying filter press Active CN103752057B (en)

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CN103752057B CN103752057B (en) 2015-11-18

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104567336A (en) * 2015-01-15 2015-04-29 中国建筑材料科学研究总院 Filter pressing and drying die
CN108786205A (en) * 2017-06-22 2018-11-13 太仓市思卡拓机械科技有限公司 A kind of apparatus for treating sewage of automatic drying filter screen
CN112779718A (en) * 2020-12-29 2021-05-11 珠海格力电器股份有限公司 Washing device and control method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104567336A (en) * 2015-01-15 2015-04-29 中国建筑材料科学研究总院 Filter pressing and drying die
CN108786205A (en) * 2017-06-22 2018-11-13 太仓市思卡拓机械科技有限公司 A kind of apparatus for treating sewage of automatic drying filter screen
CN112779718A (en) * 2020-12-29 2021-05-11 珠海格力电器股份有限公司 Washing device and control method
CN112779718B (en) * 2020-12-29 2022-03-01 珠海格力电器股份有限公司 Washing device and control method

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