CN207062125U - A kind of super-pressure sludge high-drying degree dehydration device - Google Patents

A kind of super-pressure sludge high-drying degree dehydration device Download PDF

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Publication number
CN207062125U
CN207062125U CN201720926127.5U CN201720926127U CN207062125U CN 207062125 U CN207062125 U CN 207062125U CN 201720926127 U CN201720926127 U CN 201720926127U CN 207062125 U CN207062125 U CN 207062125U
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plate
pressure
sludge
filter press
filter
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蒋正海
蒋经纬
包芳芳
饶宾期
卢锡龙
万延见
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ZHEJIANG HAIHE ENVIRONMENT TECHNOLOGY Co Ltd
China Jiliang University
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ZHEJIANG HAIHE ENVIRONMENT TECHNOLOGY Co Ltd
China Jiliang University
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Abstract

It the utility model is related to a kind of super-pressure sludge high-drying degree dehydration device, including high-voltage oil cylinder (1) and filter-pressing device, the filter-pressing device includes promoting mainly plate (8), multiple press filtration units and thrust plate (15), and press filtration chamber (21) is formed between adjacent press filtration unit;Each press filtration unit includes press filtration frame (14), left filter press plate (22) and right filter press plate (12), logical mud hole is provided with the press filtration frame (14), left filter press plate (22) and right filter press plate (12), the intracavitary sludge pipe (23) for being passed through sludge is equipped with the logical mud hole, sealing ring (10) is provided between described intracavitary sludge pipe (23) and left filter press plate (22) and right filter press plate (12), to play sealing function when the left filter press plate (22) and right filter press plate (12) move left and right.The utility model have be not easy to consume, energy consumption it is low, the advantages of dehydrated sludge moisture content is low.

Description

A kind of super-pressure sludge high-drying degree dehydration device
Technical field
Sewage Sludge Treatment Techniques field is the utility model is related to, specifically a kind of super-pressure sludge high-drying degree dehydration Device.
Background technology
Sludge high-moisture percentage is the bottleneck that govern specific resistance to filtration, and the high sludge of moisture content is not only bulky, and It is right and contained a large amount of organic matters, heavy metal and harmful microorganism is also easily degenerated or be discharged into environment, causes secondary pollution All adversely affected in the follow-up landfill of sludge, burning, recycling etc..Therefore, deeply dehydrating sludge minimizing is Treatment of Sludge primary and foremost purpose, minimizing are to realize the basis of sludge other " three change ", and sludge is more dry, and subsequent treatment disposal more has Profit.
The conventional dehydration equipment of early stage sludge has plate and frame filter press, drum centrifuge and belt type filter filter press, through these Equipment dehydrated sludge moisture content typically in 75%-80%, these sludge because moisture content is too high, cause transport inconvenience and cost compared with Height, and in landfill yard Direct Disposal drying time can not be caused to grow, the large amount of organic and abundant nitrogen phosphorus contained in sludge The nutrients such as potassium, perishable generation stench cause environmental pollution.
It is in the prior art diaphragm plate frame filter press with more deep dehydration device for sludge, squeeze pressure is only 1.6MPa, less efficient, moisture percentage in sewage sludge is higher.As shown in Figure 1-2, when Fig. 1 is barrier film non-bulging, barrier film is close to filter plate On, now dehydration is dehydrated by the feed pressure of mud, pressure typically in 0.8-1.0MPa, Fig. 2 be high-pressure hydraulic pump inject water into every Diaphragm plate inframe portion, bulging barrier film reduce filter chamber area, now diaphragm deflection, but as seen from the figure, diaphragm edge is fixed, deformation Measure very little, and centre position deformation is then very big, the structure inevitably results in sludge and differed by barrier film bulging degree, edge sludge by Bulging degree is small, and middle big by bulging degree, sludge compression degree can be brought different, moisture content is also different, diaphragm plate frame pressure Than small, chamber variable amplitude is small for contracting.In addition, on the market on common elasticity squeezing sheet frame its structure construction, filter is all one Individual overall injection module, filter easily be damaged deformation, and damage after filter need integral replacing so that safeguard into This is higher, it is often more important that, because design feature and squeeze pressure be not high, the currently employed diaphragm plate frame filter press may be by city Political affairs sludge pressing is dehydrated to 60% or so, is reduced much than plate and frame filter press moisture content before, main cause is because barrier film Bulging produces twice pressing to sludge, i.e. sludge press filtration chamber is variable chamber, but the equipment needs to add over dry mud amount 30% or so lime and molysite, so as to considerably increase the amount of sludge, and after the lime added and iron chloride etc. are to sludge Continuous processing disposal brings detrimental effect, runs counter to the minimizing of specific resistance to filtration and innoxious principle.
There is a kind of super-pressure diaphragm plate frame filter press in the prior art, the equipment is in original diaphragm plate frame filter press On upgrading, provide sludge nearly 10MPa pressure by the water that 10MPa is injected in barrier film, and squeezed for two level Journey, that is, feed pressure is begun through, highly pressurised liquid is then injected in barrier film, carry out bulging to barrier film is further carried out to sludge Press dewatering, municipal moisture percentage in sewage sludge can be down to 50% or so after equipment dehydration.Except prior figures 1-3 be present in the equipment The problems of it is outer, an also subject matter be barrier film under so high pressure and large deformation, the service life of barrier film Problem.
Currently there is a kind of superelevation compression elasticity squeezing sludge dewatering equipment, the equipment mainly includes high-voltage oil cylinder, superelevation press filtration Plate, matching board, spring medium, filter cloth specialized, tailgate, push pedal, girder etc. form, the super-pressure squeezing sheet frame include filter frame, filter plate, Filter cloth, operating room, spring and piston plate, spring are arranged between filter frame and filter plate, piston plate be arranged on operating room and filter plate it Between so that filter plate produces compression by piston plate to operating room.Rammer board dehydration is broadly divided into two-stage, and the first order is Filter chamber is transported material to by feed pump, carries out separation of solid and liquid by the pressure of feed pump while charging, i.e., once filtering is de- Water;The second level is elastic squeezing, and one end of equipment is fixed, and the other end applies ambient pressure by hydraulic jack, is passed by elasticity Power apparatus (spring) compresses chamber space and squeezing progress second dehydration is carried out to material.By carrying out super-pressure squeezing to sludge, In 5MPa or so, high-pressure oil pump needs to provide 25-30MPa or so pressure squeeze pressure, moisture percentage in sewage sludge can be down into 50% Left and right.Equally, the superelevation compression elasticity squeezer realizes the change to sludge pressing chamber volume to realize by setting spring Super-pressure extrudes, and because spring often completes the processes such as elongation-compression, it is necessary to bear alternate load, fatigue easily occurs for spring Destroy, spring is a kind of consumable accessory, and 10-20 high-strength spring is needed between every group of sheet frame, and 50-100 block sheet frames then need Will nearly 1000-2000 high-strength spring, moreover, the elastic force for also needing to overcome spring initial when extruding spring is made Actual squeeze pressure is smaller than the pressure that superpressure oil pump is supplied to suffered by sludge during, twice pressing.For example, charging pressure When power is 1MPa, spring must be provided more than 1MPa elastic force so that the maximization of chamber can be kept between filter plate and filter frame, when entering At the end of material squeezing, when high-pressure pump carries out second of high-pressure compressing to sludge, it is necessary to overcome spring to start possessed elastic force, This partial pressure is the pressure of consumption, so as to cause high-pressure pump to be less than actual pressure to pressure caused by sludge.
The compressibility of sewage sludge is good, and compression ratio is big, wants to realize to the dehydration of sludge high-drying degree, then sludge must be carried out Depth-compression, so, the changeability of press filtration chamber size and significantly changeability are to realize the key of high mass dryness fraction dehydration.
Sludge thickness is typically in 25-35mm, from filtration theory, sludge filtration effect and mistake after current press dewatering It is directly proportional to filter power, is inversely proportional with filtration resistance, mud cake is thicker, and the resistance of moisture outflow is bigger, and filtration resistance is bigger, filtering effect Fruit is poorer, so, in order to mitigate filtration resistance, filter effect is improved, sludge should be thinner;But sludge is excessively thin, can influence to locate Efficiency is managed, now it is necessary to ensure mud handling capacity and treatment effeciency by reducing the squeezing time.
Analyzed more than, it can be seen that to realize that the deep dehydration of sludge has to realize sludge pressing chamber volume Changeability, while to sludge carry out high-pressure compressing.Either diaphragm plate frame filter press or superelevation compression elasticity squeezer all has There is the changeability of sludge pressing chamber, but deep dehydration device for sludge has following subject matter at present:(1) commonly The sludge pressing pressure of diaphragm plate frame filter press is smaller, and super-pressure diaphragm plate frame filter press squeeze pressure is enough, but barrier film Life problems;(2) superelevation compression elasticity squeezer is the change for realizing sludge pressing chamber volume by spring, and spring is fragile And substantial amounts of squeeze pressure can be consumed;(3) pressure is bigger, and the sludge on filter plate is close to is more solid, easily forms one The closely knit sludge blanket of layer, the sludge blanket are bonded on filter cloth, increase moisture discharge resistance, influence dehydrating effect;(4) due to sewage High-compressibility, high-moisture percentage and the sewage sludge that sludge has contain capillary water, absorption water and sludge dewatering caused by internal water The characteristics of difficult, it is difficult that high depth dehydration is carried out to sludge completely using mechanical pressure;(5) all pressure arises directly from height The pressure of compressing cylinder, not by the enlarger of any power, cause oil cylinder working-pressure and oil cylinder volume excessive, to equipment sealing and Reliability propose higher requirement;(6) sludge is blocked up, increases filtration resistance, causes costs and poor dehydration results, mud cake inner aqueous Rate is still higher, and sludge overall moisture content is difficult to drop to lower degree.
Utility model content
In view of this, the utility model is directed to part consume existing for prior art greatly, high energy consumption, and dehydrating effect is poor Technical problem, propose one kind be not easy to consume, energy consumption it is low, the low super-pressure sludge high-drying degree dehydration dress of dehydrated sludge moisture content Put.
Technical solution of the present utility model is to provide a kind of super-pressure sludge high-drying degree dehydration dress of following structure Put, including high-voltage oil cylinder and filter-pressing device, the filter-pressing device include promoting mainly plate, multiple press filtration units and thrust plate, adjacent pressure Filter and press filtration chamber formed between unit, the press filtration unit of front end and it is described promote mainly between plate, the press filtration unit of rearmost end and institute State and also form press filtration chamber between thrust plate;
Each press filtration unit includes press filtration frame, left filter press plate and right filter press plate, the press filtration frame, left filter press plate and right press filtration Logical mud hole is provided with plate, the intracavitary sludge pipe for being passed through sludge, described intracavitary sludge are equipped with the logical mud hole Sealing ring is provided between pipe and left filter press plate and right filter press plate, from when the left filter press plate and right filter press plate move left and right To sealing function.
Optionally, the hole between the intracavitary sludge pipe and press filtration frame is with being combined into interference fit, the intracavitary sludge pipe and Hole between left filter press plate and right filter press plate coordinates with gap is combined into.
Optionally, described press filtration frame both sides offer the chute slided for left and right filter plate, described left filter press plate respectively Or/and more mud layer dredging breather pipes are fixedly installed on right filter plate.
Optionally, it is high-pressure water chamber between the left filter press plate and press filtration frame, between right filter press plate and press filtration frame, it is described High-pressure water chamber is connected with high-pressure hydraulic pump and high-pressure water pipeline.
Optionally, be provided with mud layer dredging breather pipe left filter press plate or right filter press plate in be provided with gases at high pressure chamber, In described mud layer dredging breather pipe one end insertion press filtration chamber, in other end insertion heavy pressure gas chamber room, described high pressure gas Fluid chamber is connected with gases at high pressure pipeline and air pump.
Optionally, the super-pressure sludge high-drying degree dehydration device also includes double-crankshaft force amplificatory structure, the double-crankshaft One end of force amplificatory structure is arranged on rear pattern plate, and the other end is connected with secondary push pedal as force side, and described hyperbolic axle power is put Crosshead among great institutions is also connected with the hydraulic stem of high-voltage oil cylinder, and described rear pattern plate passes through regulating bolt and fixed mount phase Even, offer the internal thread being meshed with regulating bolt on described fixed mount, by screw thread pair coordinate adjustable rear pattern plate and The position of double-crankshaft force amplificatory structure.
Optionally, disc spring group is provided between plate and secondary push pedal in described promote mainly, the disc spring group combines for polylith disc spring Together.
Optionally, reinforcing line and filter cloth are additionally provided with the inwall of press filtration chamber, reinforcing line is arranged on inside, the filter Cloth is arranged on the outside of reinforcing line.
Optionally, the upper and lower end parts of the left filter press plate and right filter press plate are equipped with mud-scraping ring, and the mud-scraping ring is with phase Filter press plate motion is answered to scrape mud to realize.
Optionally, described mud layer dredging breather pipe is hollow tube, and multiple apertures are offered thereon, and gases at high pressure can Inside sludge when squeezing is entered by the hollow tube and the aperture opened up, mud layer dredging breather pipe outer layer covers have filter cloth.
Using above structure, the utility model has advantages below:By setting right filter press plate respectively in press filtration frame both sides And left filter press plate, a kind of mobile barrier film effect of existing diaphragm plate frame filter press is served, i.e., sludge is in each of press filtration intracavitary Position receives equal extruding squeezing, sludge uniform force, moreover, using press & filter plate structure is slided, for the pressure of sludge Contracting degree can be controlled arbitrarily, and remarkable result is played for the municipal administration domestic sludge of high compression ratio;Pass through the enlarger of power, the machine Structure force amplifying function can reduce the system configuration of high-pressure pump up to 10-20 times, reduce the seal request of energy consumption and hydraulic system; Due to also having partial moisture mechanically to remove in sludge, this programme is provided with more mud layer dredging breather pipes, with And high pressure gas generator and component, acted on by gases at high pressure, the moisture that mechanical system in sludge is difficult to remove is passed through into height Pressure gas stream mode is taken away, that is, realizes that mechanical expression and high pressure draught carry double effects, so as to further reduce the moisture of sludge, Reach sludge deep minimizing purpose.
Brief description of the drawings
Fig. 1 is the part-structure schematic diagram of the diaphragm plate frame filter press of prior art;
View when Fig. 2 is Fig. 1 structure eardrums;
Fig. 3 is the sectional view of the utility model super-pressure sludge high-drying degree dehydration device;
Fig. 4 is the external structure schematic diagram of the utility model super-pressure sludge high-drying degree dehydration device.
As illustrated, 1, high-voltage oil cylinder, 2, regulating bolt, 3, fixed mount, 4, rear pattern plate, 5, double-crankshaft force amplificatory structure, 6th, secondary push pedal, 7, disc spring group, 8, promote mainly plate, 9, mud-scraping ring, 10, sealing ring, 11, high-pressure water chamber, 12, right filter press plate, 13, high pressure Stomata, 14, press filtration frame, 15, thrust plate, 16, filter cloth, 17, filtrate discharge pipe, 18, gases at high pressure chamber, 19, mud layer dredging it is logical Tracheae, 20, end-face seal ring, 21, press filtration chamber, 22, left filter press plate, 23, intracavitary sludge pipe, 24, air pump, 25, gases at high pressure Pipeline, 26, high-pressure hydraulic pump, 27, high-pressure water pipeline.
Embodiment
The utility model is described in further detail with specific embodiment below in conjunction with the accompanying drawings.
The utility model cover any replacement made in spirit and scope of the present utility model, modification, equivalent method with And scheme.Thoroughly understand in order that the public has to the utility model, in following the utility model preferred embodiment specifically Understand concrete details, and description without these details can also understand that this practicality is new completely for a person skilled in the art Type.In addition, be not drawn to scale accurately completely for the needs of signal in the accompanying drawing of the utility model, This is explained.
As shown in Figures 3 and 4, a kind of super-pressure sludge high-drying degree dehydration device of the utility model, including hydraulic oil are illustrated Cylinder 1, filter frame 14, thrust plate 15, filter cloth 16, end-face seal ring 20, the hydraulic system oil pressure joined together by high-voltage oil cylinder 1 are 15- 20MPa, oil cylinder piston area are multiplied by pressure and are multiplied by press filtration plate suqare, superelevation equal to sludge pressing pressure multiplied by with force amplifying function Sludge high-drying degree dehydration device is pressed also to include power amplification, position adjustment and pressure-keeping mechanism, in order to improve anti-pressure ability, filter plate 14 is adopted It is made of metal material, the both sides of filter frame 14 offer chute respectively, coordinate in the chute of left and right two and are provided with two pieces of movable pressures Filter plate is right filter press plate 12 and left filter press plate 22, is fixedly installed more mud layers dredging breather pipes 19 on left filter press plate 22, two Its volume of formation sludge press filtration chamber 21 can be adjusted, different sludge compression performances according to the motion of left and right filter press plate between filter plate Difference, it can arbitrarily be adjusted.A plurality of reinforcement is provided with thrust plate 15, material is made up of the high alloy material of intensity, thrust Plate 15 is fixed in frame.
It is high-pressure water chamber 11, high-pressure water chamber 11 and high-pressure hydraulic pump 26 and high-pressure water pipeline between two pieces of filter press plates and filter frame 14 27 are connected, and the hydraulic pressure between hydraulic pressure and filter plate and filter frame that high-pressure hydraulic pump provides is 8-10MPa, is also equipped with high-pressure water pipeline Valve, ensure that when mud enters press filtration chamber high-pressure hydraulic pump 26 stops voltage supply, the water in high-pressure water chamber 11 returns to water tank, and mud layer is dredged All in the one end of tracheae 19 insertion sludge press filtration chamber 21, insertion depth and the cake thickness being no more than after finally squeezing, the other end Insert in gases at high pressure chamber 18, gases at high pressure chamber 18 is connected with gases at high pressure pipeline 25 and air pump 24, mud layer dredging ventilation Pipe 19 is hollow tube, offers multiple apertures, when gases at high pressure can enter squeezing by the hollow tube and the aperture opened up Inside sludge, the mud layer dredging outer layer covers of breather pipe 19 have filter cloth, prevent mud granule from entering mud layer dredging passage 19.
Logical mud hole is offered on filter plate 14, right filter press plate 12 and left filter press plate 22, intracavitary dirt is equipped with logical mud hole Mud pipe 23, sludge is led in intracavitary sludge pipe, the hole between intracavitary sludge pipe 23 and press filtration frame 14 is interference fit, with right filter press plate Hole between 12 and left filter press plate 22 coordinates with gap is combined into, described intracavitary sludge pipe 23 and right filter press plate 12 and left filter press plate Sealing ring 10 is provided between 22 so that sludge will not enter high pressure when right filter press plate 12 and left filter press plate 22 can move left and right In water cavity.
The amplification of dehydration device power, position adjustment and pressure-keeping mechanism by double-crankshaft force amplificatory structure 5, rear pattern plate 4, fixed mount 3, Regulating bolt 2, disc spring group 7 form, and double-crankshaft force amplificatory structure 5 is Double-crank shaft bar linkage, including long toggle link, small toggle link, short Toggle link, crosshead, side link etc., the one end of double-crankshaft force amplificatory structure 5 are fixedly mounted on rear pattern plate 4, the other end and secondary push pedal 6 It is connected, hydraulic stem of the crosshead among double-crankshaft force amplificatory structure 5 also with high-voltage oil cylinder 1 is connected, and rear pattern plate 4 is by adjusting spiral shell Bolt 2 is connected with fixed mount 3, and the internal thread being meshed with regulating bolt 2 is offered on fixed mount 3, is coordinated by screw thread pair adjustable The right position of rear pattern plate 4 and double-crankshaft force amplificatory structure 5 is saved, disc spring group 7 is that polylith disc spring is combined, and is pushed away installed in pair Plate 6 and promote mainly between plate 8.
Mud-scraping ring 9 and sealing ring 10 are respectively arranged with right filter press plate 12 and left filter press plate 22 thickness direction, in right press filtration Reinforcing line and filter cloth 16 are additionally provided with plate 12 and left filter press plate 22, reinforcing line is arranged on inside, and filter cloth 16 is arranged on reinforcing line Outside.
It is close to press filtration frame 14 during 21 volume maximum of press filtration chamber for right filter press plate 12 and left filter press plate 22, now thickness is 20mm-25mm, press filtration is reached away from press filtration frame 14 for right filter press plate 12 and left filter press plate 22 during 21 volume minimum of press filtration chamber Stopper slot on frame 14, now thickness is about 6-10mm.
Into before super-pressure sludge high-drying degree dehydration device of the present utility model, sludge can pass through concentration or preliminary de- Water so that enter mud mud moisture content in 90%-85%, whole dewatering time is 30min-45min, terminates to arrange from arm-tie is entered The mud whole work period is 1 hour or so.
Present apparatus operation principle is as follows:
High-voltage oil cylinder promotes Double-crank shaft bar linkage so that is in close contact between each press filtration frame, passes through the end of press filtration frame Face sealing ring will seal between each filter frame, form the big press filtration chamber of a closing, moisture content 90%-85% mud is by entering Dredge pump is pumped into press filtration intracavitary, is now the charging squeezing stage, and under feed pressure effect, moisture is by filter cloth, and sludge Grain is stayed in press filtration chamber, and as feed time is increasingly longer, mud granule stops charging full of press filtration chamber, now press filtration intracavitary The mud cake with certain moisture content is formed, high-pressure hydraulic pump is started working and water is pumped into the chamber between filter press plate and press filtration frame, So that forming high water pressure in chamber, under high water pressure effect, left filter press plate toward left movement, turn right motion, right by right filter press plate The mud cake of beginning is further extruded, and now squeezes the stage for super-pressure, under 8-10MPa super-pressure effect, left pressure Filter plate continues motion of turning right toward left movement, right filter press plate is continued, and the moisture in sludge is gradually squeezed out, while sludge is extruded Must be more and more real, when the moisture of mud cake, which no longer extrudes mud cake, to be compressed again, left and right filter press plate stop motion, in superelevation Press in expressing process, air is entered gases at high pressure chamber by high-pressure pump by gas line, high pressure stomata, is then passed through again Mud layer dredging breather pipe is entered inside sludge, and using hair-dryer principle, being taken out of by air inside sludge can not be by machinery pressure The moisture of extrusion is squeezed, sludge is in the case where high-pressure compressing extrusion dehydration and air carry moisture double action, when reaching the mass dryness fraction of sludge, Water smoking terminates.High-voltage oil cylinder drives Double crank link mechanism, will promote mainly plate toward pulling back, plate pulling device pulls open filter frame, mud cake Fall down, a cycle terminates.The next cycle enters mud again, and now high-pressure hydraulic pump is stopped, while left and right filter press plate and filter frame Between water gone back under feed pressure, i.e., left filter press plate is turned right motion, and right filter press plate is toward left movement so that press filtration chamber reaches again To maximum, it is easy to follow-up super-pressure to squeeze.
Although embodiment is separately illustrated and illustrated above, it is related to the common technology in part, in ordinary skill Personnel apparently, can be replaced and integrate between the embodiments, be related to one of embodiment and the content recorded is not known, then Refer to another embodiment on the books.
Only the utility model preferred embodiment is described above, but is not to be construed as the limit to claim System.The utility model is not only limited to above example, and its concrete structure allows to change.In a word, it is all only in the utility model The various change made in vertical scope of the claims is in the scope of protection of the utility model.

Claims (10)

1. a kind of super-pressure sludge high-drying degree dehydration device, including high-voltage oil cylinder (1) and filter-pressing device, the filter-pressing device include Plate (8), multiple press filtration units and thrust plate (15) are promoted mainly, press filtration chamber (21) is formed between adjacent press filtration unit, front end Press filtration unit and described promote mainly between plate (8), also form press filtration chamber between the press filtration unit of rearmost end and the thrust plate (15) Room (21);
Each press filtration unit includes press filtration frame (14), left filter press plate (22) and right filter press plate (12), the press filtration frame (14), left pressure Logical mud hole is provided with filter plate (22) and right filter press plate (12), the intracavitary dirt for being passed through sludge is equipped with the logical mud hole Mud pipe (23), sealing ring is provided between described intracavitary sludge pipe (23) and left filter press plate (22) and right filter press plate (12) (10), to play sealing function when the left filter press plate (22) and right filter press plate (12) move left and right.
2. super-pressure sludge high-drying degree dehydration device according to claim 1, it is characterised in that:The intracavitary sludge pipe (23) hole between press filtration frame (14), which is matched somebody with somebody, is combined into interference fit, the intracavitary sludge pipe (23) and left filter press plate (22) and right pressure Hole between filter plate (12) coordinates with gap is combined into.
3. super-pressure sludge high-drying degree dehydration device according to claim 2, it is characterised in that:Described press filtration frame (14) Both sides offer the chute slided for left and right filter plate respectively, fix and set on described left filter press plate (22) or/and right filter plate (12) It is equipped with more mud layer dredging breather pipes (19).
4. super-pressure sludge high-drying degree dehydration device according to claim 1, it is characterised in that:The left filter press plate (22) It is high-pressure water chamber (11) between press filtration frame (14), between right filter press plate (12) and press filtration frame (14), described high-pressure water chamber (11) it is connected with high-pressure hydraulic pump (26) and high-pressure water pipeline (27).
5. super-pressure sludge high-drying degree dehydration device according to claim 3, it is characterised in that:Mud layer dredging is being installed Gases at high pressure chamber (18), described mud layer dredging breather pipe (19) are provided with the left filter press plate or right filter press plate of breather pipe (19) In one end insertion press filtration chamber (21), in other end insertion gases at high pressure chamber (18), described gases at high pressure chamber (18) with Gases at high pressure pipeline (25) and air pump (24) are connected.
6. the super-pressure sludge high-drying degree dehydration device according to claim 1 or 3 or 5, it is characterised in that:The super-pressure Sludge high-drying degree dehydration device also includes double-crankshaft force amplificatory structure (5), one end installation of the double-crankshaft force amplificatory structure (5) On rear pattern plate (4), the other end is connected with secondary push pedal (6) as force side, described double-crankshaft force amplificatory structure (5) centre Hydraulic stem of the crosshead also with high-voltage oil cylinder (1) is connected, and described rear pattern plate (4) passes through regulating bolt (2) and fixed mount (3) phase Even, the internal thread being meshed with regulating bolt (2) is offered on described fixed mount (3), is coordinated by screw thread pair after can adjust The position of template (4) and double-crankshaft force amplificatory structure (5).
7. super-pressure sludge high-drying degree dehydration device according to claim 6, it is characterised in that:Plate (8) is promoted mainly described Disc spring group (7) is provided between secondary push pedal (6), the disc spring group (7) is that polylith disc spring is combined.
8. super-pressure sludge high-drying degree dehydration device according to claim 1, it is characterised in that:In press filtration chamber (21) Reinforcing line and filter cloth (16) are additionally provided with inwall, reinforcing line is arranged on inside, and the filter cloth (16) is arranged on the outer of reinforcing line Portion.
9. the super-pressure sludge high-drying degree dehydration device according to claim 1 or 3, it is characterised in that:The left filter press plate (22) and the upper and lower end parts of right filter press plate (12) are equipped with mud-scraping ring (9), the mud-scraping ring (9) with corresponding filter press plate move with Mud is scraped in realization.
10. super-pressure sludge high-drying degree dehydration device according to claim 3, it is characterised in that:Described mud layer dredging Breather pipe (19) is hollow tube, and multiple apertures are offered thereon, and gases at high pressure can pass through the hollow tube and the aperture opened up Inside sludge when entering squeezing, mud layer dredging breather pipe (19) outer layer covers have filter cloth (16).
CN201720926127.5U 2017-07-28 2017-07-28 A kind of super-pressure sludge high-drying degree dehydration device Active CN207062125U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107324630A (en) * 2017-07-28 2017-11-07 浙江海河环境科技有限公司 Super-pressure sludge high-drying degree dehydration device
CN112321125A (en) * 2020-12-02 2021-02-05 北京山清源环保科技有限公司 High-pressure filtering mechanism for filter press

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107324630A (en) * 2017-07-28 2017-11-07 浙江海河环境科技有限公司 Super-pressure sludge high-drying degree dehydration device
CN112321125A (en) * 2020-12-02 2021-02-05 北京山清源环保科技有限公司 High-pressure filtering mechanism for filter press

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