CN208802977U - A kind of multi-chamber multistage filters pressing sludge dehydration device - Google Patents
A kind of multi-chamber multistage filters pressing sludge dehydration device Download PDFInfo
- Publication number
- CN208802977U CN208802977U CN201820406930.0U CN201820406930U CN208802977U CN 208802977 U CN208802977 U CN 208802977U CN 201820406930 U CN201820406930 U CN 201820406930U CN 208802977 U CN208802977 U CN 208802977U
- Authority
- CN
- China
- Prior art keywords
- plate
- filters pressing
- range line
- oil cylinder
- filter
- 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.)
- Expired - Fee Related
Links
- 239000010802 sludge Substances 0.000 title claims abstract description 79
- 230000018044 dehydration Effects 0.000 title claims abstract description 34
- 238000006297 dehydration reaction Methods 0.000 title claims abstract description 34
- 230000005540 biological transmission Effects 0.000 claims abstract description 30
- 230000007246 mechanism Effects 0.000 claims abstract description 28
- 239000004744 fabric Substances 0.000 claims description 24
- 238000007906 compression Methods 0.000 claims description 11
- 230000006835 compression Effects 0.000 claims description 10
- 238000006243 chemical reaction Methods 0.000 claims description 5
- 238000006073 displacement reaction Methods 0.000 claims description 4
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 238000009434 installation Methods 0.000 claims description 3
- 230000002787 reinforcement Effects 0.000 claims description 2
- 238000000034 method Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000001914 filtration Methods 0.000 description 6
- 230000008569 process Effects 0.000 description 5
- 230000014509 gene expression Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000010801 sewage sludge Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 241000145637 Lepturus Species 0.000 description 1
- 241001494479 Pecora Species 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 230000000994 depressogenic effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- -1 i.e. Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000001141 propulsive effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 230000017260 vegetative to reproductive phase transition of meristem Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/122—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D25/00—Filters formed by clamping together several filtering elements or parts of such elements
- B01D25/12—Filter presses, i.e. of the plate or plate and frame type
- B01D25/21—Plate and frame presses
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Treatment Of Sludge (AREA)
- Filtration Of Liquid (AREA)
Abstract
The utility model relates to a kind of multi-chamber multistage filters pressing sludge dehydration devices, including filters pressing head plate (8), filters pressing tailgate (11), power device and multiple filter press plates (10), it further includes fixed support plate (4), intermediate pressure transmission plate (17), force amplificatory structure (16), pull rod (3) and internal contracting brake mechanism (2);The pull rod (3) is placed through in the fixed support plate (4) and intermediate pressure transmission plate (17), and the force amplificatory structure (16) is installed between the intermediate pressure transmission plate (17) and the filters pressing head plate (8);The power device includes level-one oil cylinder (1) and two-level oil cylinder (5), the level-one oil cylinder (1) and two-level oil cylinder (5) arranged in series;Internal contracting brake mechanism holds pull rod tightly after the completion of the level-one oil cylinder promotes;The force amplificatory structure (16) is for amplifying the power of two-level oil cylinder;The filter press plate is equipped with filter plate range line device (9), forms pressure-variable filter chamber room between two neighboring filter press plate.
Description
Technical field
The utility model relates to sewage sludge process field, specifically a kind of multi-chamber multistage filters pressing sludge dewatering dress
It sets.
Background technique
Sludge high-moisture percentage is the bottleneck for restricting specific resistance to filtration, and the high sludge of moisture content is not only bulky, but also
Contained a large amount of organic matters, heavy metal and harmful microorganism is also easy corruption or can be discharged into environment, and causes secondary pollution, to dirt
The subsequent landfill of mud, burning, resource utilization etc. all adversely affect.Therefore, deeply dehydrating sludge minimizing is sludge
Primary and foremost purpose is handled, minimizing is the basis for realizing sludge other " three change ", and sludge is more dry, disposes to subsequent processing more advantageous.
The common dehydration equipment of early stage sludge has plate and frame filter press, drum centrifuge and belt type filter filter press, through these
After equipment dehydration, moisture percentage in sewage sludge generally in 75%-80%, these sludge because moisture content is excessively high, and cause transport inconvenient and at
This is higher, and drying time can not be caused long in landfill yard Direct Disposal, the large amount of organic that contains in sludge and abundant
The nutrients such as N P and K, perishable generation stench cause environmental pollution.
It is currently on the market diaphragm plate frame filter press with more deep dehydration device for sludge, but in dehydration, efficiency
Lower, squeeze pressure is only 1.6MPa, and squeezing is injected sewage inside diaphragm plate frame by high-pressure hydraulic pump, and bulging diaphragm reduces
Filter chamber area, diaphragm plate frame are squeezed by the plastic deformation of sheet frame;Diaphragm plate frame compression ratio is small, and the opposite duty cycle is long.In addition,
On the market common elasticity squeezing sheet frame structure structurally, filter plate is all the injection molding module an of entirety, and filter plate is easy
Impaired deformation, and the filter plate after damage needs integral replacing, so that maintenance cost is higher, it is often more important that, due to structure
Feature and squeeze pressure be not high, the currently employed diaphragm plate frame filter press may by municipal sludge press dewatering to 60% or so,
It is reduced much than plate and frame filter press moisture content before, main cause is because diaphragm bulging generates twice pressing to sludge, i.e.,
Sludge press filtration chamber is variable chamber, but the equipment needs to add the lime and molysite of over dry mud amount 30% or so, thus greatly
The amount of sludge is increased greatly, and the meeting such as the lime added and iron chloride processing disposition subsequent to sludge brings unfavorable shadow
It rings, violates the minimizing and innoxious principle of specific resistance to filtration.
Current there are also a kind of superelevation compression elasticities to squeeze sludge dewatering equipment, which mainly includes high-voltage oil cylinder, superelevation filters pressing
Plate, matching board, spring medium, filter cloth specialized, tailgate, push plate, girder etc. composition, the super-pressure squeezing sheet frame include filter frame, filter plate,
Filter cloth, operating room, spring and piston plate, spring are set between filter frame and filter plate, piston plate setting operating room and filter plate it
Between, so that filter plate generates compression to operating room by piston plate.Rammer board dehydration is broadly divided into two-stage, and the first order is
Filter chamber is transported material to by feed pump, charging while is separated by solid-liquid separation by the pressure of feed pump, i.e., primary 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 cylinder, is passed by elasticity
Power device (spring) compresses chamber space and carries out squeezing progress second dehydration to material.By carrying out super-pressure squeezing to sludge,
For squeeze pressure in 5MPa or so, high-pressure oil pump needs to provide the pressure of 25-30MPa or so, moisture percentage in sewage sludge can be down to 50%
Left and right.Equally, which realizes the change to sludge pressing chamber volume by setting spring to realize
Super-pressure squeezes, and since spring often completes the processes such as elongation-compression, needs to bear alternating load, spring is easy to happen fatigue
It destroys, spring is a kind of vulnerable part, and 10-20 high-strength spring is needed between every group of sheet frame, and 50-100 block sheet frame then needs
Will nearly 1000-2000 high-strength spring, moreover, the elastic force that also needs to overcome spring initial when squeezing spring is made
The actual squeeze pressure suffered by sludge when, twice pressing is smaller than the pressure that superpressure oil pump is supplied to.For example, charging pressure
When power is 1MPa, spring must be provided greater than 1MPa elastic force so that be able to maintain the maximization of chamber between filter plate and filter frame, when into
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, is less than actual pressure to pressure caused by sludge so as to cause high-pressure pump.
For existing market there are also a kind of super-pressure diaphragm plate frame filter press, which is on original diaphragm plate frame filter press
Upgrading, the water by injecting 10MPa in diaphragm provides the nearly pressure of 10MPa to sludge, and is second level expressing process,
Feed pressure is begun through, highly pressurised liquid is then injected in diaphragm, bulging is carried out to diaphragm, further sludge is pressed
Dehydration is squeezed, municipal moisture percentage in sewage sludge can be down to 50% or so after equipment dehydration.There are a main problems to be for the equipment
Diaphragm influences the problem of the service life of diaphragm under so high pressure and large deformation.
By analyzing above, it can be seen that the deep dehydration of Yao Shixian 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 there are following main problems for deep dehydration device for sludge 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 diaphragm
Service life is not high;(2) superelevation compression elasticity squeezer is the variation for realizing sludge pressing chamber volume by spring, and spring is easy to damage
And a large amount of squeeze pressure can be consumed;(3) pressure is bigger, more solid in the sludge being tightly attached on filter plate, and easy to form one
The closely knit sludge blanket of layer, the sludge blanket are bonded on filter cloth, increase moisture and resistance is discharged, influence dehydrating effect;(4) all pressures
Power arises directly from the pressure of high-voltage oil cylinder, not the enlarger Jing Guo any power, leads to oil cylinder working-pressure and oil cylinder volume mistake
Greatly, to equipment sealing and reliability more stringent requirements are proposed.
Utility model content
In view of this, the utility model is more for above-mentioned vulnerable part of the existing technology, energy consumption is high, oil cylinder working-pressure requirement
High, the still higher technical problem of dehydrated sludge moisture content proposes that a kind of few easy workout part, low energy consumption, and passes through force amplificatory structure
Pressure is amplified, the lower multi-chamber multistage filters pressing sludge dehydration device of dehydrated sludge moisture content.
The technical solution of the utility model is to provide a kind of with flowering structure multi-chamber multistage filters pressing sludge dewatering dress
It sets, including filters pressing head plate, filters pressing tailgate, power device and multiple filter press plates, the multiple filter press plate is located at filters pressing head plate and pressure
It filters between tailgate, it further includes fixed support plate, intermediate pressure transmission plate, force amplificatory structure, pull rod and internal contracting brake mechanism;The drawing
Bar is placed through in the fixed support plate and intermediate pressure transmission plate, and the force amplificatory structure is installed on the intermediate pressure transmitting
Between plate and the filters pressing head plate;
The power device includes level-one oil cylinder and two-level oil cylinder, the level-one oil cylinder and two-level oil cylinder's arranged in series, right
Sludge carries out classification pressurization;
Internal contracting brake mechanism holds pull rod tightly after the completion of the level-one oil cylinder promotes, fixed support plate and intermediate pressure transmission plate shape
At an entirety, level-one oil cylinder no longer stress;
The force amplificatory structure is small in the variation of filters pressing later period cake thickness for amplifying the power of two-level oil cylinder, into
And it realizes two-level oil cylinder and effectively pushes generation hyperpressure;
The filter press plate is concave-convex filter press plate, and the filter press plate is equipped with filter plate range line device, two neighboring filter press plate
Between form pressure-variable filter chamber room, filter plate range line device defines the two neighboring filters pressing in the closed situation in pressure-variable filter chamber room
The maximum distance of plate.
Optionally, the pull rod includes band-type brake teeth, locking bar groove and pull rod boss, and the locking bar groove is for drawing
Lever lock ring is by draw lever locking and is fixed on the left side of intermediate pressure transmission plate, and the intermediate pressure transmission plate is for installing pull rod
Hole be a step through-hole, and be fitted close with pull rod boss, reaction force by intermediate pressure transmission plate by oil cylinder
It is transmitted on pull rod by boss and pull rod lock ring, the pull rod lock ring pulling pull rod is simultaneously synchronous with intermediate pressure transmission plate
It moves right.
Optionally, the internal contracting brake mechanism can be fitted close with band-type brake teeth, and draw lever locking is fixed on fixed support plate
On, be transferred to fixed support plate convenient for the power on pull rod, the internal contracting brake mechanism include semicircular ring in band-type brake, band-type brake interlocking bar,
The outer semicircular ring of band-type brake and band-type brake force oil cylinder, there is the boss ring matched with band-type brake teeth in the band-type brake annulus inside, described
Band-type brake interlocking bar by be located at upper and lower two sides band-type brake inside and outside semicircular ring link together, i.e., band-type brake force cylinder action when band-type brake
Interior semicircular ring is by outside thrust, and the outer semicircular ring of band-type brake is by inside pulling force.
Optionally, the concave-convex filter press plate side is punch structure, and the other side is cavity die structure, the filters pressing head plate
For cavity die structure, filters pressing tailgate is punch structure, is allowed to be capable of forming closed filters pressing chamber with adjacent filter press plate, described
Filter press plate convexity mode structure is embedded into formation filters pressing chamber, the filters pressing head plate and filters pressing tail in the cavity die structure of adjacent filter plate
There are several pieces of filter press plates between plate, self-adjusting balance module is set between multiple filter press plates, the self-adjusting balance module includes
Convex bulb plate, recessed bulb plate and hose.
Optionally, the filter plate range line device includes range line card slot, range line bolt and range line connecting rod, the range line card
Circular hole and a square groove there are two opening on slot, wherein for square groove for installing range line bolt, the range line bolt can be in side
It is slided within the scope of certain distance in shape slot, the range line connecting rod is the cylindrical bar for being provided with two sections of half slots, and tail portion is shorter
Half slot is mounted in range line card slot for avoiding interference with the movement of range line bolt, and the tail portion of the range line connecting rod is alternately fixed
Be installed in the circular hole of range line card slot, head may pass through the circular hole of the adjacent range line card slot in right side, the range line bolt to
Corresponding range line connecting rod can be blocked by being inside moved to bottom.
Optionally, the filter plate range line device be installed on filter press plate two sides and symmetrical, described bolt synchronizing moving
Bar through the same side range line bolt, and by guide rod driving cylinder drive it to move synchronously, realize range line bolt insertion and
It extracts, to determine whether range line connecting rod is stuck in range line card slot.
Optionally, the concave-convex filter press plate includes filter plate body, liner plate, reinforces lining cloth and filter cloth, the liner plate and plus
Strong lining cloth is fixed on filter plate body two sides, and the filter cloth setting is being reinforced on the outside of lining cloth, is uniformly opened on the liner plate
If several limbers and netted guiding gutter, the filter plate body top offers air inlet and air channel, and lower part offers water flowing
Slot and apopore, air inlet are connect with high-pressure pump by tracheae.
Optionally, the enlarger of the power is Double row connecting rod mechanism, and the compression that force-displacement behavior meets sludge is special
Linearity curve generates hyperpressure for amplifying power caused by two-level oil cylinder, when to realizing sludge second level filters pressing,
Including several connecting rods.The relationship of power suffered by sludge and sludge compression displacement is power and sludge compressed-bit suffered by sludge
The relationship of shifting constitutes compression property curve.
Optionally, the fixed support plate, pull rod support frame and filters pressing tailgate are fixed in the rack of whole device, described
Intermediate pressure transmission plate, filters pressing head plate and filter press plate be in suspended state and can control and move freely.
Optionally, in filter press plate two sides and it is symmetrically installed with idler wheel, there is track with matching below idler wheel, from
And make idler wheel with filter press plate along track horizontal movement.
Using the above structure, the utility model has the advantage that (1) is less than second level oil due to the power that level-one oil cylinder generates
The reaction force that cylinder and force amplificatory structure generate, therefore the pull rod of the utility model use and internal contracting brake mechanism are acted in two-level oil cylinder
When remove the power of level-one oil cylinder and not only protected level-one oil cylinder but also saved electric energy, internal contracting brake mechanism will after the completion of level-one oil cylinder promotes
Pull rod is held tightly, and fixed support plate and intermediate pressure transmission plate form an entirety, the reaction generated when acting on two-level oil cylinder
Power can be safely and effectively fully transmitted on fixed support plate, level-one oil cylinder no longer stress;(2) required for mechanical expression mud cake
Pressure is very big, if it is especially substantially unchanged without the thickness of larger pressure mud cake when the later period, therefore the utility model
It joined force amplificatory structure, for amplifying the power of two-level oil cylinder, even if may be implemented to remain unchanged energy in filters pressing later period oil cylinder
Effectively push generation hyperpressure;(3) the utility model uses concave-convex filter press plate, and filters pressing head plate is cavity die structure, filters pressing tail
Plate is punch structure, has several pieces of concave-convex filter press plates between filters pressing head plate and filters pressing tailgate, punch structure is embedded in adjacent filter plate
Punch structure in while form filters pressing chamber with first plate, the mutually embedding two closed filters pressing chambers in formation first place of tailgate, with this
It realizes and becomes chamber sludge press filtration, the self-adjusting balance module of setting can effectively adjust multiple filters pressing chambers later due to processing and cooperating
Force direction offset issue brought by inaccurate;(4) the utility model uses filter plate and limits distance means, for realizing pressing
In the closed situation in filter chamber room, the distance of adjacent two filter plate does not exceed the limit value of setting;(5) setting high pressure gas, which is blown, fills
It sets, the moisture that some mechanical expressions can't get out can be taken away by gas, form mechanical expression and be superimposed pneumatic conveying drying double effects.
Detailed description of the invention
Fig. 1 is the front view of the utility model multi-chamber multistage filters pressing sludge dehydration device;
Fig. 2 is the axonometric drawing of the utility model multi-chamber multistage filters pressing sludge dehydration device;
Fig. 3 is the 3-D view of the filter plate range line device of the utility model multi-chamber multistage filters pressing sludge dehydration device;
Fig. 4 is the cross-sectional view of the filter plate range line device of the utility model multi-chamber multistage filters pressing sludge dehydration device;
Fig. 5 is the front view of the filter plate range line bolt of the utility model multi-chamber multistage filters pressing sludge dehydration device;
Fig. 6 is the structural schematic diagram of the internal contracting brake mechanism of the utility model multi-chamber multistage filters pressing sludge dehydration device;
Fig. 7 is the structural schematic diagram of the pull rod of the utility model multi-chamber multistage filters pressing sludge dehydration device.
As shown, 1, level-one oil cylinder, 2, internal contracting brake mechanism, semicircular ring in 2-1, band-type brake, 2-3,2-2, band-type brake interlocking bar are embraced
The outer semicircular ring of lock, 2-4, band-type brake force oil cylinder, 3, pull rod, 3-1, band-type brake teeth, 3-2, locking bar groove, 3-3, pull rod boss, 4,
Fixed support plate, 5, two-level oil cylinder, 6, pull rod lock ring, 7, pull rod support frame, 8, filters pressing head plate, 9, filter plate range line device, 9-1,
Range line card slot, 9-2, range line bolt, 9-3, range line connecting rod, 10, filter press plate, 11, filters pressing tailgate, 12, plunger pump, 13, idler wheel,
14, guide rail, 15, bolt synchronizing moving bar, 16, force amplificatory structure, 17, intermediate pressure transmission plate, 18, rack, 19, self-adjusting balance
Module, 20, air inlet.
Specific embodiment
The utility model is described in further detail in the following with reference to the drawings and specific embodiments.
The utility model cover any substitution made in the spirit and scope of the utility model, modification, equivalent method with
And scheme.In order to make the public have thorough understanding to the utility model, in following the preferred embodiment in the utility model specifically
Concrete details is illustrated, and that this can also be understood completely is practical new for description without these details for a person skilled in the art
Type.In addition, be not drawn to scale accurately completely in the attached drawing of the utility model for the needs of signal,
This is explained.
As shown in Figure 1, the multi-chamber multistage filters pressing sludge dehydration device of the utility model is illustrated, including filters pressing head plate 8,
Filters pressing tailgate 11, power device and multiple filter press plates 10, the multiple filter press plate 10 be located at filters pressing head plate 8 and filters pressing tailgate 11 it
Between, it further includes fixed support plate 4, intermediate pressure transmission plate 17, force amplificatory structure 16, pull rod 3 and internal contracting brake mechanism 2;The drawing
Bar 3 is placed through in the fixed support plate 4 and intermediate pressure transmission plate 17, and the force amplificatory structure 16 is installed on the intermediate pressure
Between power transmission plate 17 and the filters pressing head plate 8;
The power device includes level-one oil cylinder 1 and two-level oil cylinder 5, and the level-one oil cylinder 1 and two-level oil cylinder 5 connect cloth
It sets, classification pressurization is carried out to sludge;
Internal contracting brake mechanism 2 holds pull rod 3 tightly after the completion of the level-one oil cylinder 1 promotes, fixed support plate 4 and intermediate pressure transmitting
Plate 17 forms an entirety, the no longer stress of level-one oil cylinder 1;
The force amplificatory structure 16 is small in the variation of filters pressing later period cake thickness for amplifying the power of two-level oil cylinder 5,
And then realize that two-level oil cylinder effectively pushes generation hyperpressure;
The filter press plate 10 is concave-convex filter press plate, and the filter press plate 10 is equipped with filter plate range line device 9, two neighboring pressure
Pressure-variable filter chamber room is formed between filter plate, filter plate range line device 9 defines adjacent two in the closed situation in pressure-variable filter chamber room
The maximum distance of a filter press plate.
The pull rod 3 and internal contracting brake mechanism 2, the reaction force generated when for acting on two-level oil cylinder 5 are safely and effectively complete
Ground is transmitted on fixed support plate 4, and internal contracting brake mechanism 2 holds pull rod 3 tightly after the completion of level-one oil cylinder 4 promotes, and fixed support plate 4 is in
Between pressure transmitting plates 17 formed an entirety, level-one oil cylinder 4 is not in stress.Force amplificatory structure 16, for by the power of two-level oil cylinder 5
It amplifies, it is small in the variation of filters pressing later period cake thickness, and then realize that oil cylinder effectively pushes generation hyperpressure.Filter press plate 10 with
And filter plate range line device 9, for realizing chamber sludge press filtration is become, filter plate range line device 9 realizes the case where filters pressing chamber is closed
Under, the distance of adjacent two filter plate does not exceed some setting numerical value.The internal contracting brake mechanism 2 can be close in band-type brake teeth 3-1
Pull rod 3 is locked on fixed support plate 4, is transferred to fixed support plate 4 convenient for the power on pull rod 3, described embraces by cooperation
Brake mechanism 2 includes the outer semicircular ring 2-3 of semicircular ring 2-1, band-type brake interlocking bar 2-2, band-type brake and band-type brake force oil cylinder 2-4, institute in band-type brake
There is the boss ring matched with band-type brake teeth 3-1 on the inside of the band-type brake annulus stated, the band-type brake interlocking bar 2-2 will be located at upper and lower two
Semicircular ring links together inside and outside the band-type brake of side, i.e., band-type brake force oil cylinder 2-4 movement when band-type brake in semicircular ring 2-1 by outside
Thrust, the outer semicircular ring 2-3 of band-type brake is by inside pulling force.
The filter press plate 10 includes filter plate body, liner plate, reinforces lining cloth and filter cloth, and the liner plate and reinforcement lining cloth are fixed
On filter plate body two sides, the filter cloth setting is being reinforced on the outside of lining cloth, and several water flowings are uniformly opened up on the liner plate
Hole and netted guiding gutter, making moisture by setting liner plate, more easily outflow and high pressure gas are easy to be distributed to entire mud chamber
Dehydrating effect is improved in interior, and lining cloth is reinforced in setting, protects filter cloth, improves filter cloth service life, the filter plate body top opens up
There are air inlet 20 and air channel, lower part offers water-flowing trough and apopore.10 side of filter press plate is punch structure side
It is cavity die structure, the filters pressing head plate 8 is cavity die structure, and filters pressing tailgate 11 is punch structure, is allowed to and adjacent filter press plate
10 are capable of forming closed filters pressing chamber, and the 10 convexity mode structure of filter press plate is embedded into shape in the cavity die structure of adjacent filter plate
At filters pressing chamber, there are several pieces of filter press plates 10 between the filters pressing head plate 8 and filters pressing tailgate 11, in the muti-piece filter press plate
Between be also provided with self-adjusting balance module 19, the self-adjusting balance module includes convex bulb plate, recessed bulb plate and hose.
The filter plate range line device 9 includes range line card slot 9-1, range line bolt 9-2 and range line connecting rod 9-3, the limit
Away from being opened on card slot 9-1 there are two circular hole and a square groove, wherein square groove is for installing range line bolt 9-2, the range line
Bolt 9-2 can be slided within the scope of the certain distance in square groove, and the range line connecting rod 9-3 is the circle for being provided with two sections of half slots
Mast, the shorter half slot in tail portion is mounted in range line card slot 9-1 for avoiding interference with the movement of range line bolt 9-2, described
The tail portion of range line connecting rod 9-3 is alternately fixedly installed in the circular hole of range line card slot 9-1, and head may pass through the adjacent range line in right side
The circular hole of card slot 9-1, the range line bolt 9-2, which is moved into bottom, can block corresponding range line connecting rod 9-3.
The force amplificatory structure 16 is for amplifying power caused by two-level oil cylinder 5, to realize sludge second level
Hyperpressure is generated when filters pressing.The force amplificatory structure 16 is respectively by hydraulic steering gear adopting cross piece, the first toggle, the second toggle, third toggle
Composition, the force amplificatory structure 16 is hinged with intermediate pressure transmission plate 17, filters pressing head plate 8, two-level oil cylinder 5 respectively, is amplified by power
Mechanism, force amplifying function can achieve 10-20 times, then the oil pressure of short stroke oil cylinder or oil cylinder area can accordingly reduce 10-20
Times, the stroke and force amplifying function of force amplificatory structure can be realized by adjusting toggle length thereon and installation site, so that should
The movement of force amplificatory structure and mechanical characteristic meet sludge compression property.
The filter plate range line device 9 includes range line card slot 9-1, range line bolt 9-2 and range line connecting rod 9-3.Rectangular range line
Circular hole and a square groove there are two opening on card slot 9-1, range line bolt 9-2, which is mounted in square groove, to be slided in a certain range
Dynamic, the range line connecting rod 9-3 is the cylindrical bar for being provided with two sections of half slots, range line connecting rod 9-3 and the fixed company of range line card slot 9-1
It connects, two adjacent range line connecting rod 9-3 are staggered installation of in two circular holes of range line card slot 9-1, the shorter half slot in tail portion
For avoiding interference with the movement of range line bolt 9-2 in range line card slot 9-1, head may pass through the adjacent range line card slot in right side
The circular hole of 9-1, the range line bolt 9-2, which is moved into bottom, can block corresponding range line connecting rod 9-3.When progress level-one squeezing
When, range line bolt 9-2 and range line connecting rod 9-3 are inserted into corresponding range line card slot 9-1 the function of realizing range line, and material enters chamber
Afterwards, chamber volume constantly increases, when chamber is in maximum volume, the further shifting of range line bolt 9-2 card card range line connecting rod 9-3
It is dynamic.After all grades of squeezings, two pieces of filter plates must be pulled open, mud cake can just be fallen down, and at this time pull out range line bolt 9-2
Out, enable the head of range line connecting rod 9-3 to detach from range line card slot 9-1, realize that chamber opens dump.
The fixed support plate 4, pull rod support frame 7 and filters pressing tailgate 11 are fixed on 18 in the rack of whole device, described
Intermediate pressure transmission plate 17, filters pressing head plate 8 and filter press plate 10 can realize left and right move freely.In 10 two sides of filter press plate and symmetrically
Idler wheel 13 is installed, there is track with matching below idler wheel 13, so that idler wheel is with filter press plate 10 along rail
Road horizontal movement.
The high pressure gas component includes high-pressure pump, gas supervisor and gas service pipe, the gas service pipe and institute
There is the air inlet 20 on filter press plate 10 and filters pressing head plate 8, filters pressing tailgate 8 to be connected, gas pressure is generally in 0.5-0.8MPa.It is logical
Crossing the moisture content of the cake that mechanical expression mode obtains, there are a limiting values, further to subtract its moisture content, realize high mass dryness fraction, can
It carries further to deviate from the moisture on mud cake surface using air-flow.With this configuration, high pressure gas can enter filters pressing cavity
It is interior, by the effect of gas, the moisture of sludge is taken out of, it is similar to using hair dryer to dry up the principle of wet hair in daily life,
The moisture removal that swiftly flowing gas can cannot remove mechanical system, meanwhile, the mud cake of part on filter plate can also be blown
It falls, again, is blown off the mud granule being blocked on filter cloth mesh by the effect of high-speed gas, reduce the resistance of moisture outflow
Power.
Present apparatus working principle is as follows: starting to work into before mud (upper a cycle dump terminates), whole device is in
Original state;I.e. fixed support plate, intermediate pressure transmission plate and filters pressing head plate are in the maximum position far from filters pressing tailgate.This
When start new round cycling, filters pressing head plate is pushed into its extreme position as power mechanism by level-one oil cylinder;That is filters pressing head plate
Most nearby apart from filters pressing tailgate, multi-chamber is depressed into closed state, and intracavitary volume is minimum.Then by bolt synchronizing moving bar by
Original relieving state is advanced to locking state, by the laterally movable scope limitation of each piece of filter press plate in a thin tail sheep model
It encloses, guarantees that off-limits relative movement will not occur for filter press plate.Start while removing level-one oil cylinder motive force into mud, into
Expect under pressure effect, the filter press plate close to filters pressing tailgate can be moved toward the direction far from filters pressing tailgate, when moving to chamber volume
When maximum, Bit andits control mechanism limitation filter plate cannot move again, and mud subsequently enters next chamber, and next filter plate is also in mud
Slurry pressure pushes lower past separate tailgate direction to move to chamber maximum position until filter plate Bit andits control mechanism limits, with such
Push away, when being moved to chamber maximum position together with filters pressing head plate to last one piece of filter plate, each chamber volume of whole device it
With reach maximum value, continue charging until feed pressure be not enough to by sludge be pressed into filters pressing chamber, charging stop, which is first
Grade dehydration.Following level-one oil cylinder restores motive force, pushes intermediate pressure transmission plate to apply pressure and acts on filters pressing head plate
On, filters pressing head plate is pushed at its maximum displacement, the chamber for filling sludge at this time is compacted, and completes level-one squeezing.Due to when one
It when grade squeezing is completed, needs to lock pull rod in a certain position, therefore designs the pull rod with the groove structure of discontinuous, work as level-one
When filters pressing head plate is advanced into farthest by oil cylinder, the card slot of pull rod least significant end just with internal contracting brake mechanism it is embedding and, internal contracting brake mechanism will draw
Lever lock extremely in the position, guarantees relatively fixed between intermediate pressure transmission plate and fixed support plate under the action of pull rod.At this point,
Two-level oil cylinder starts to act on, and kick acts on intermediate pressure transmission plate, by the enlarger of power by filters pressing head plate to being pushed forward
Into keeping it close to filters pressing tailgate again, that is, further decrease chamber volume, complete second level expressing process.When expressing process is completed
Enter dump link afterwards, first bolt synchronizing moving bar is extracted to the state of relieving at this time, removes two-level oil cylinder, level-one oil cylinder respectively
Propulsive force, filter press plate is pulled open one by one under the action of plate pulling device at this time, at the same high pressure gas blow, will stick on filter plate
Mud cake is blown off, and can blow clean the mud granule being blocked on filter cloth mesh, is ready for next period.When all
Filter plate all pulls open, and sludge is fallen down, and the entire duty cycle terminates.
Although embodiment is separately illustrated and is 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
It can 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 embodiments, and specific structure is allowed to vary.In short, all only in the utility model
Made various change is within the protection scope of the present utility model in vertical scope of protection of the claims.
Claims (10)
1. a kind of multi-chamber multistage filters pressing sludge dehydration device, including filters pressing head plate (8), filters pressing tailgate (11), power device and
Multiple filter press plates (10), the multiple filter press plate (10) are located between filters pressing head plate (8) and filters pressing tailgate (11), and feature exists
In: it further includes fixed support plate (4), intermediate pressure transmission plate (17), force amplificatory structure (16), pull rod (3) and internal contracting brake mechanism
(2);The pull rod (3) is placed through in the fixed support plate (4) and intermediate pressure transmission plate (17), the force amplificatory structure
(16) it is installed between the intermediate pressure transmission plate (17) and the filters pressing head plate (8);
The power device includes level-one oil cylinder (1) and two-level oil cylinder (5), and the level-one oil cylinder (1) and two-level oil cylinder (5) connect
Arrangement, carries out classification pressurization to sludge;
Internal contracting brake mechanism (2) holds pull rod (3) tightly after the completion of the level-one oil cylinder (1) promotes, fixed support plate (4) and intermediate pressure
Transmission plate (17) forms an entirety, level-one oil cylinder (1) no longer stress;
The force amplificatory structure (16) is small in the variation of filters pressing later period cake thickness for amplifying the power of two-level oil cylinder (5),
And then realize that two-level oil cylinder effectively pushes generation hyperpressure;
The filter press plate (10) is concave-convex filter press plate, and the filter press plate (10) is equipped with filter plate range line device (9), two neighboring
Pressure-variable filter chamber room is formed between filter press plate, filter plate range line device (9) defines the phase in the closed situation in pressure-variable filter chamber room
The maximum distance of adjacent two filter press plates.
2. multi-chamber multistage filters pressing sludge dehydration device according to claim 1, it is characterised in that: the pull rod (3)
Including band-type brake teeth (3-1), locking bar groove (3-2) and pull rod boss (3-3), the locking bar groove (3-2) is used for Draw bar lock
The left side of intermediate pressure transmission plate (17) is locked and be fixed in pull rod (3) by ring (6), and the intermediate pressure transmission plate (17) is used
In installation pull rod (3) hole be a step through-hole, and with pull rod boss (3-3) be fitted close, by intermediate pressure transmission plate
(17) it is transmitted on pull rod (3) by the reaction force of oil cylinder by boss and pull rod lock ring (6), the pull rod lock ring
(6) hold pull rod (3) and with intermediate pressure transmission plate (17) synchronize move right.
3. multi-chamber multistage filters pressing sludge dehydration device according to claim 1 or 2, it is characterised in that: the band-type brake
Mechanism (2) and band-type brake teeth (3-1) are fitted close, and pull rod (3) is locked on fixed support plate (4), is convenient for pull rod (3)
On power be transferred to fixed support plate (4), the internal contracting brake mechanism (2) includes semicircular ring in band-type brake (2-1), band-type brake interlocking bar
The outer semicircular ring (2-3) of (2-2), band-type brake and band-type brake exert a force oil cylinder (2-4), in the band-type brake in semicircular ring and the outer semicircular ring of band-type brake
There is the boss ring matched with band-type brake teeth (3-1) in side, and the band-type brake interlocking bar (2-2) will be located at the band-type brake of upper and lower two sides
Inside and outside semicircular ring links together, i.e., semicircular ring (2-1) is pushed away by outside in band-type brake when band-type brake force oil cylinder (2-4) acts
Power, the outer semicircular ring (2-3) of band-type brake is by inside pulling force.
4. multi-chamber multistage filters pressing sludge dehydration device according to claim 1, it is characterised in that: the filter press plate
(10) side is punch structure, and the other side is cavity die structure, and the filters pressing head plate (8) is cavity die structure, filters pressing tailgate (11)
For punch structure, it is allowed to be capable of forming closed filters pressing chamber with adjacent filter press plate (10), the filter press plate (10) convexity
Mode structure is embedded into formation filters pressing chamber, the filters pressing head plate (8) and filters pressing tailgate (11) in the cavity die structure of adjacent filter plate
Between have several pieces of filter press plates (10), be also provided with self-adjusting balance module (19), institute between the muti-piece filter press plate (10)
The self-adjusting balance module stated includes convex bulb plate, recessed bulb plate and hose.
5. multi-chamber multistage filters pressing sludge dehydration device according to claim 1, it is characterised in that: the filter plate range line
Device (9) includes range line card slot (9-1), range line bolt (9-2) and range line connecting rod (9-3), is opened on the range line card slot (9-1)
There are two circular hole and a square grooves, and wherein for square groove for installing range line bolt (9-2), the range line bolt (9-2) can
It is slided within the scope of certain distance in square groove, the range line connecting rod (9-3) is the cylindrical bar for being provided with two sections of half slots, tail
The shorter half slot in portion is mounted in range line card slot (9-1) for avoiding interference with the movement of range line bolt (9-2), the range line
The tail portion of connecting rod (9-3) is alternately fixedly installed in the circular hole of range line card slot (9-1), and head may pass through the adjacent range line in right side
The circular hole of card slot (9-1), the range line bolt (9-2), which is moved into bottom, can block corresponding range line connecting rod (9-3).
6. multi-chamber multistage filters pressing sludge dehydration device according to claim 5, it is characterised in that: the filter plate range line
Device (9) is installed on two sides of filter press plate (10) and symmetrical, and the multi-chamber multistage filters pressing sludge dehydration device further includes bolt
Synchronizing moving bar (15), the bolt synchronizing moving bar (15) and are driven through the range line bolt (9-2) of the same side by guide rod
Cylinder of taking offence drives it to move synchronously, realize range line bolt (9-2) into and out to whether determine range line connecting rod (9-3)
It is stuck in range line card slot (9-1).
7. multi-chamber multistage filters pressing sludge dehydration device according to claim 1 or 4, it is characterised in that: the filters pressing
Plate (10) includes filter plate body, liner plate, reinforces lining cloth and filter cloth, and the liner plate and reinforcement lining cloth are fixed on filter plate body two sides
On, the filter cloth setting is being reinforced on the outside of lining cloth, and several limbers and netted guiding gutter, institute are uniformly opened up on the liner plate
The filter plate body top stated offers air inlet (20) and air channel, and lower part offers water-flowing trough and apopore, the air inlet
(20) it is connect by tracheae with high-pressure pump.
8. multi-chamber multistage filters pressing sludge dehydration device according to claim 1, it is characterised in that: the power enlarger
Structure (16) is Double row connecting rod mechanism, and force-displacement behavior meets the compression property curve of sludge, is used for two-level oil cylinder (5) institute
The power of generation amplifies, and generates hyperpressure when to realizing sludge second level filters pressing comprising several connecting rods.
9. multi-chamber multistage filters pressing sludge dehydration device according to claim 1, it is characterised in that: the fixed support plate
(4), pull rod support frame (7) and filters pressing tailgate (11) are fixed in the rack (18) of whole device, the intermediate pressure transmitting
Plate (17), filters pressing head plate (8) and filter press plate (10) can be achieved left and right and move freely.
10. multi-chamber multistage filters pressing sludge dehydration device according to claim 1, it is characterised in that: in filter press plate (10)
Two sides and be symmetrically installed with idler wheel (13), have track with matching below idler wheel (13) so that idler wheel with
Filter press plate (10) is along track horizontal movement.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2017102263452 | 2017-04-08 | ||
CN201710226345 | 2017-04-08 |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208802977U true CN208802977U (en) | 2019-04-30 |
Family
ID=61031784
Family Applications (11)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201711016434.0A Active CN107572741B (en) | 2017-04-08 | 2017-10-27 | The municipal sludge depth minus quantization device of microwave-assisted processing |
CN201711016114.5A Active CN107585983B (en) | 2017-04-08 | 2017-10-27 | Municipal sludge depth reduction method for microwave auxiliary treatment |
CN201711023697.4A Expired - Fee Related CN107555759B (en) | 2017-04-08 | 2017-10-27 | Microwave improves dehydration and drying sludge treating system |
CN201711023698.9A Active CN107698126B (en) | 2017-04-08 | 2017-10-27 | Microwave improves dehydration and drying sludge treating system |
CN201711073443.3A Active CN107670353B (en) | 2017-04-08 | 2017-11-05 | Multi-chamber sludge high-dryness dewatering device |
CN201711073442.9A Active CN107638724B (en) | 2017-04-08 | 2017-11-05 | Embedded multi-cavity sludge high-dryness dewatering device |
CN201711388377.9A Active CN108503176B (en) | 2017-04-08 | 2017-12-20 | Microwave improves dehydration and drying method for sludge treatment |
CN201711497457.8A Active CN108101340B (en) | 2017-04-08 | 2017-12-31 | High-dryness sewage sludge dewatering method with double effects of mechanical squeezing and air flow carrying |
CN201810249136.4A Active CN108358422B (en) | 2017-04-08 | 2018-03-26 | Multi-cavity multi-stage filter pressing sludge dewatering method |
CN201820406930.0U Expired - Fee Related CN208802977U (en) | 2017-04-08 | 2018-03-26 | A kind of multi-chamber multistage filters pressing sludge dehydration device |
CN201810255306.XA Active CN108358423B (en) | 2017-04-08 | 2018-03-26 | Multi-cavity multi-stage filter-pressing sludge dewatering device |
Family Applications Before (9)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201711016434.0A Active CN107572741B (en) | 2017-04-08 | 2017-10-27 | The municipal sludge depth minus quantization device of microwave-assisted processing |
CN201711016114.5A Active CN107585983B (en) | 2017-04-08 | 2017-10-27 | Municipal sludge depth reduction method for microwave auxiliary treatment |
CN201711023697.4A Expired - Fee Related CN107555759B (en) | 2017-04-08 | 2017-10-27 | Microwave improves dehydration and drying sludge treating system |
CN201711023698.9A Active CN107698126B (en) | 2017-04-08 | 2017-10-27 | Microwave improves dehydration and drying sludge treating system |
CN201711073443.3A Active CN107670353B (en) | 2017-04-08 | 2017-11-05 | Multi-chamber sludge high-dryness dewatering device |
CN201711073442.9A Active CN107638724B (en) | 2017-04-08 | 2017-11-05 | Embedded multi-cavity sludge high-dryness dewatering device |
CN201711388377.9A Active CN108503176B (en) | 2017-04-08 | 2017-12-20 | Microwave improves dehydration and drying method for sludge treatment |
CN201711497457.8A Active CN108101340B (en) | 2017-04-08 | 2017-12-31 | High-dryness sewage sludge dewatering method with double effects of mechanical squeezing and air flow carrying |
CN201810249136.4A Active CN108358422B (en) | 2017-04-08 | 2018-03-26 | Multi-cavity multi-stage filter pressing sludge dewatering method |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810255306.XA Active CN108358423B (en) | 2017-04-08 | 2018-03-26 | Multi-cavity multi-stage filter-pressing sludge dewatering device |
Country Status (1)
Country | Link |
---|---|
CN (11) | CN107572741B (en) |
Families Citing this family (32)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108987058B (en) * | 2018-07-24 | 2021-07-27 | 国网福建省电力有限公司 | Insulating oil intelligence photovoltaic conversion microwave heating oil filter |
CN109045838A (en) * | 2018-08-08 | 2018-12-21 | 成都赋阳技术开发有限公司 | A kind of filtering and purifying of mud waste water |
CN109455897A (en) * | 2018-10-30 | 2019-03-12 | 饶宾期 | Microwave hot air jet stream cooperates with drying method |
CN109231764B (en) * | 2018-10-30 | 2023-11-14 | 明阳(宁波)环保科技有限公司 | Microwave hot air jet flow cooperative drying device |
CN109231768B (en) * | 2018-10-30 | 2022-01-18 | 浙江诺曼环保工程技术有限公司 | Mechanical filter pressing microwave coupling dehydration drying method |
CN109231769B (en) * | 2018-10-30 | 2023-12-26 | 深圳市中科绿建环保工程有限公司 | Mechanical filter-pressing microwave coupling dehydration desiccation integrated device |
CN109354374A (en) * | 2018-11-22 | 2019-02-19 | 国网天津市电力公司电力科学研究院 | A kind of novel drying method for sludge |
CN109331510A (en) * | 2018-12-03 | 2019-02-15 | 四川央润新泥环境科技有限公司 | A kind of filter press box casing locking device |
CN109502945B (en) * | 2018-12-26 | 2024-06-25 | 毅康科技有限公司 | High-dryness sludge dewatering device and use method thereof |
CN109553258A (en) * | 2019-01-21 | 2019-04-02 | 毅康科技有限公司 | A kind of sludge dehydrating and drying system and method for sludge treatment |
CN109734266A (en) * | 2019-02-28 | 2019-05-10 | 北京净界新宇环保科技有限公司 | Oily sludge minimizing processing method |
CN109775955A (en) * | 2019-03-14 | 2019-05-21 | 江苏卡托科技有限公司 | Sludge treatment equipment |
CN111233100B (en) * | 2019-03-28 | 2022-08-23 | 金达泰克电子系统(北京)有限公司 | Device for treating radioactive waste water, capable of automatically installing and replacing membrane in membrane stack |
CN110065257B (en) * | 2019-04-19 | 2021-07-20 | 广西长寿奥秘科技有限公司 | Squeezing device for processing edible oil and facilitating adjustment of squeezing interlayer |
CN112047603A (en) * | 2019-06-05 | 2020-12-08 | 宁波热电股份有限公司 | Sludge treatment method and sludge treatment device thereof |
CN111072252A (en) * | 2019-12-10 | 2020-04-28 | 浙江雅顿环境科技有限公司 | Sludge drying machine for treating gelatin sludge |
CN111256770B (en) * | 2020-01-22 | 2021-07-13 | 哈尔滨东安实业发展有限公司 | Multi-oil product displacement lubricating oil flow and pressurizing tester |
CN112047595A (en) * | 2020-07-31 | 2020-12-08 | 张家港市大新污水处理有限公司 | Sludge drying process without adding flocculant |
CN112253020A (en) * | 2020-11-03 | 2021-01-22 | 凌贝利 | Drilling fluid solid-liquid separation equipment that borehole operation was used |
CN112321125B (en) * | 2020-12-02 | 2024-08-02 | 北京山清源环保科技有限公司 | High-pressure filtering mechanism for filter press |
CN112624555A (en) * | 2020-12-25 | 2021-04-09 | 无锡国联环保科技股份有限公司 | Method and system for thermal alkali hydrolysis treatment of sludge |
CN112759219A (en) * | 2021-01-15 | 2021-05-07 | 杭州秀澈环保科技有限公司 | Deep dehydration process for sludge |
CN113024072A (en) * | 2021-02-05 | 2021-06-25 | 集美大学 | Automatic sludge dewatering and squeezing equipment and method |
CN113860702B (en) * | 2021-05-12 | 2023-09-19 | 中国计量大学 | Multi-field coupling automatic sewage sludge dehydration method |
CN113443807B (en) * | 2021-08-30 | 2021-11-19 | 天津市星拓科技发展有限公司 | High-pressure sealed filter plate unit structure and using method |
CN113788599A (en) * | 2021-09-17 | 2021-12-14 | 中广核环保产业有限公司 | Sludge dewatering pretreatment equipment |
CN114873892A (en) * | 2022-05-24 | 2022-08-09 | 道诚环境科技(山东)有限公司 | Rotary sludge press-filtering and drying device |
CN115636565A (en) * | 2022-08-30 | 2023-01-24 | 广州嘉康环保技术有限公司 | Culture sludge treatment method |
CN117285224B (en) * | 2023-11-27 | 2024-02-02 | 深圳市洪桦环保科技有限公司 | Multistage filter-pressing type sludge dewatering equipment |
CN117383640B (en) * | 2023-12-11 | 2024-03-08 | 成都凯亚美环保机械制造股份有限公司 | High-efficient low temperature vacuum dehydration mummification complete sets |
CN117839282A (en) * | 2024-03-09 | 2024-04-09 | 福建省创绿机械股份有限公司 | One-way diaphragm filter plate type filter press |
CN118426427B (en) * | 2024-07-03 | 2024-09-03 | 山东智奇环境技术有限公司 | Monitoring system and method for municipal industrial sludge recycling treatment |
Family Cites Families (46)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4310424A (en) * | 1980-07-23 | 1982-01-12 | Champion International Corporation | Apparatus and method for removing suspended solids from a stream |
GB8812360D0 (en) * | 1988-05-25 | 1988-06-29 | Lucas Ind Plc | Fluid control device & braking system |
JP3359409B2 (en) * | 1994-01-12 | 2002-12-24 | 株式会社ナガオカ | Pressurized dehydrator for sludge treatment and sludge treatment method |
US5480222A (en) * | 1995-05-01 | 1996-01-02 | Janel Hydro Co. | Automotive hydraulic braking system |
DE19752653B4 (en) * | 1997-11-27 | 2007-08-16 | Dieffenbacher Gmbh + Co. Kg | Plant and filter press for dehumidifying pasty solids |
JP4090099B2 (en) * | 1998-01-20 | 2008-05-28 | 株式会社 神崎高級工機製作所 | Axle drive |
DE19956617A1 (en) * | 1999-11-25 | 2001-06-07 | Hoesch & Soehne Eberhard | Filter plate of a filter press |
NL1014739C2 (en) * | 2000-03-24 | 2001-02-05 | Duyvis Machinenfab Bv | Press to separate cocoa mass into cocoa cake and cocoa butter. |
TW553221U (en) * | 2002-04-30 | 2003-09-11 | Jr-Shi Liang | Sludge dehydration device |
US7396472B2 (en) * | 2004-03-09 | 2008-07-08 | Duby Sean R | Filter plate assembly for filter |
JP4542928B2 (en) * | 2005-03-18 | 2010-09-15 | 株式会社宇野澤組鐵工所 | Method and apparatus for squeezing slurry |
DE102007039583A1 (en) * | 2006-09-14 | 2008-03-27 | Dehydry Anlagenbau Ag | Method for dehumidifying and drying of solid liquid mixtures, by supplying suspension to be treated over channels into a device, and transferring the filtrate over the channels in simultaneous refining of the solid portion as filter cake |
JP2008012524A (en) * | 2006-12-01 | 2008-01-24 | Justec Co Ltd | Solid-liquid separator |
CN101254368B (en) * | 2007-12-14 | 2011-07-27 | 胡杭虎 | Sludge squeezing filtering method and sludge strong press-pate machine used for the method |
CN201136834Y (en) * | 2007-12-14 | 2008-10-22 | 胡杭虎 | Strong sludge dewaterer |
CN201245538Y (en) * | 2008-08-04 | 2009-05-27 | 胡杭虎 | Strong sludge dehydrator |
CN201267984Y (en) * | 2008-09-24 | 2009-07-08 | 沪东重机有限公司 | Hydraulic drawing device with locating function |
CN201267860Y (en) * | 2008-10-16 | 2009-07-08 | 济南汇和机电设备有限公司 | Squeezed riveting device |
CN101544459B (en) * | 2009-05-11 | 2011-04-13 | 浙江华章科技有限公司 | Plate-type sludge dewatering machine and dewatering method therefor |
CN101570198B (en) * | 2009-05-27 | 2011-06-15 | 上海尤加工程机械科技有限公司 | Synchronous braking system for suspended type digger |
CN201482269U (en) * | 2009-08-14 | 2010-05-26 | 赵恩 | Horizontal press filter |
CN201668983U (en) * | 2010-05-13 | 2010-12-15 | 廖一浩 | Locking and separating device of filter press |
CN102225260B (en) * | 2011-04-29 | 2013-05-29 | 山东省科学院新材料研究所 | Automatic filter-pressing dehydration device and working method thereof |
CN102229464B (en) * | 2011-06-02 | 2013-03-27 | 杭州中威净水材料有限公司 | Preparation and method for drying sludge through deep dehydrating |
CN102350108B (en) * | 2011-08-29 | 2013-11-20 | 浙江金鸟压滤机有限公司 | Dynamic filtering pressing dehydrator |
US20160355426A1 (en) * | 2011-12-21 | 2016-12-08 | General Electric Company | Microwave processing of wastewater sludge |
CN102836581B (en) * | 2012-08-14 | 2015-03-25 | 佛山市金凯地过滤设备有限公司 | Pressure filter and pressing filtering method thereof |
CN102827661A (en) * | 2012-08-31 | 2012-12-19 | 燕山大学 | Sludge fuelization treatment process of urban sewage treatment plant |
CN104014185B (en) * | 2014-06-23 | 2015-09-30 | 中国计量学院 | Mud centrifugal filter press dewater unit |
CN104150738B (en) * | 2014-08-11 | 2016-01-13 | 华东理工常熟研究院有限公司 | A kind of drying method of organism particulate mud and portable anhydration system |
CN204246922U (en) * | 2014-11-10 | 2015-04-08 | 成都樵枫科技发展有限公司 | For the filter element cell structure of pressure drum filter |
CN104803575B (en) * | 2015-03-25 | 2017-03-29 | 浙江威治环保科技有限公司 | Supertension sewage sludge deep dehydrator |
CN104817246B (en) * | 2015-03-25 | 2017-02-22 | 中国计量大学 | Ultrahigh-pressure deep dehydration method for sewage sludge |
CN104784997A (en) * | 2015-04-16 | 2015-07-22 | 佛山市金凯地过滤设备有限公司 | Horizontal spring filter press with reverse-blow air-drying structure |
CN105314811A (en) * | 2015-06-08 | 2016-02-10 | 上海同臣环保有限公司 | Deep sludge dewatering technology |
CN105330118B (en) * | 2015-10-27 | 2018-06-22 | 湖州旺能机械设备制造有限公司 | A kind of sludge filter press and method for sludge treatment |
CN105819636B (en) * | 2015-12-31 | 2018-05-18 | 中国计量大学 | High mass dryness fraction sewage sludge treatment system |
CN105536310A (en) * | 2016-01-25 | 2016-05-04 | 佛山市金凯地过滤设备有限公司 | Filter pressing method for removing residual water conveniently and filter press adopting filter pressing method |
CN105727608B (en) * | 2016-02-19 | 2018-01-09 | 泰安市民乐机械制造有限公司 | The all-hydraulic deep dehydration automatic pressure filter of intelligence |
CN205627231U (en) * | 2016-05-27 | 2016-10-12 | 泰安市民乐机械制造有限公司 | Automatic standard -sized sheet pressure filter of high pressure degree of depth dehydration |
CN106007336A (en) * | 2016-07-12 | 2016-10-12 | 河南永泽环境科技有限公司 | Sludge dewatering method achieved by combining microwaves with compound flocculating agent |
CN106045275A (en) * | 2016-07-21 | 2016-10-26 | 黄志荣 | Sludge drying system |
CN106057058A (en) * | 2016-07-25 | 2016-10-26 | 西北农林科技大学 | Spiral mobile mechanical model weight box |
CN106517720B (en) * | 2016-11-22 | 2019-04-26 | 哈尔滨工业大学 | A kind of sewage sludge multistage based on multiple spot into mud couples sheet frame filter-press dehydration device and its application method |
CN207775041U (en) * | 2017-10-27 | 2018-08-28 | 浙江威治环保科技有限公司 | A kind of microwave conditioning dehydration and drying sludge treating system |
CN207775034U (en) * | 2017-10-27 | 2018-08-28 | 浙江威治环保科技有限公司 | A kind of municipal sludge depth minus quantization device of microwave radiation technology processing |
-
2017
- 2017-10-27 CN CN201711016434.0A patent/CN107572741B/en active Active
- 2017-10-27 CN CN201711016114.5A patent/CN107585983B/en active Active
- 2017-10-27 CN CN201711023697.4A patent/CN107555759B/en not_active Expired - Fee Related
- 2017-10-27 CN CN201711023698.9A patent/CN107698126B/en active Active
- 2017-11-05 CN CN201711073443.3A patent/CN107670353B/en active Active
- 2017-11-05 CN CN201711073442.9A patent/CN107638724B/en active Active
- 2017-12-20 CN CN201711388377.9A patent/CN108503176B/en active Active
- 2017-12-31 CN CN201711497457.8A patent/CN108101340B/en active Active
-
2018
- 2018-03-26 CN CN201810249136.4A patent/CN108358422B/en active Active
- 2018-03-26 CN CN201820406930.0U patent/CN208802977U/en not_active Expired - Fee Related
- 2018-03-26 CN CN201810255306.XA patent/CN108358423B/en active Active
Also Published As
Publication number | Publication date |
---|---|
CN107585983B (en) | 2023-10-24 |
CN108101340B (en) | 2020-02-04 |
CN108358422A (en) | 2018-08-03 |
CN108358423A (en) | 2018-08-03 |
CN107585983A (en) | 2018-01-16 |
CN107670353B (en) | 2023-11-17 |
CN108503176A (en) | 2018-09-07 |
CN107638724A (en) | 2018-01-30 |
CN108101340A (en) | 2018-06-01 |
CN108358422B (en) | 2020-11-27 |
CN107670353A (en) | 2018-02-09 |
CN108503176B (en) | 2019-11-01 |
CN108358423B (en) | 2021-07-02 |
CN107555759B (en) | 2019-10-01 |
CN107572741A (en) | 2018-01-12 |
CN107555759A (en) | 2018-01-09 |
CN107698126A (en) | 2018-02-16 |
CN107638724B (en) | 2023-02-07 |
CN107698126B (en) | 2019-11-01 |
CN107572741B (en) | 2019-11-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN208802977U (en) | A kind of multi-chamber multistage filters pressing sludge dehydration device | |
CN106927658B (en) | High-dryness dewatering device for thin-layer sludge | |
CN102267794B (en) | Sludge dehydrator | |
CN101254368B (en) | Sludge squeezing filtering method and sludge strong press-pate machine used for the method | |
CN108404474B (en) | Split type multi-cavity filter-pressing sludge dewatering method | |
CN107008042B (en) | Sewage sludge reduction dewatering device based on electromagnetic force | |
CN106946435A (en) | High throughput sewage sludge depth quantitative reduction method | |
CN101088944A (en) | Enhanced sludge dewatering machine | |
CN103722762A (en) | Rubbish crushing, hydraulic squeezing, dewatering, drying and separating all-in-one machine | |
CN201320424Y (en) | High-power dewaterer of sludge | |
CN106946436B (en) | Multistage sewage sludge depth reduction method | |
CN201099651Y (en) | Sludge strong dewaterer | |
CN108529848B (en) | Split type filter-pressing sludge dewatering method | |
CN205360710U (en) | But dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation | |
CN106943779B (en) | Large-treatment-capacity sewage sludge depth reduction device | |
CN201136834Y (en) | Strong sludge dewaterer | |
CN107008041B (en) | Sewage sludge reduction dehydration method based on electromagnetic force | |
CN101164928B (en) | Sludge strong force dewatering machine | |
CN106267936B (en) | High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity filter press after a kind of coal slime flotation | |
CN108585425B (en) | Split type filter-pressing sludge dewatering device | |
CN207062125U (en) | A kind of super-pressure sludge high-drying degree dehydration device | |
CN208907069U (en) | A kind of clamshell type multi-chamber filters pressing sludge dehydration device | |
CN206188620U (en) | High -pressure dehydrator | |
CN201510794U (en) | Belt-type and pressing-type filter | |
CN210845399U (en) | Automatic plate-pulling pressure filter of polypropylene high-pressure diaphragm |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190430 |