CN206492277U - A kind of filter residue output mechanism and filter press - Google Patents
A kind of filter residue output mechanism and filter press Download PDFInfo
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- CN206492277U CN206492277U CN201621369655.7U CN201621369655U CN206492277U CN 206492277 U CN206492277 U CN 206492277U CN 201621369655 U CN201621369655 U CN 201621369655U CN 206492277 U CN206492277 U CN 206492277U
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- filter
- press filtration
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- cylinder
- material conveying
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Abstract
The utility model relates to a kind of filter residue output mechanism and filter press, a kind of filter residue output mechanism, including fixed mount, motor and circulation material conveying band, wherein：Circulation material conveying band front and back end is arranged with active rotating shaft and driven spindle respectively, motor, active rotating shaft and driven spindle are fixed on fixed mount, motor connects active rotating shaft by shaft coupling, and circulation material conveying band upper surface is material containing face, and circulation material conveying band is connected with strainer；Filter-pressing device is provided with a kind of filter press, including frame, frame, filter-pressing device includes the press filtration cylinder being coaxially oppositely arranged and locked mode set, and press filtration cylinder top is provided with drain pipe port provided with the charging mouth of pipe, press filtration cylinder bottom and locked mode set bottom, press filtration cylinder front end is discharging opening, wherein：Including a kind of above-mentioned filter residue output mechanism, circulation material conveying band is arranged on relative position below discharging opening.The utility model provides a kind of efficiency high, good effect of separating solid from liquid, and energy centralized collection filter residue meets filter residue output mechanism and filter press that cultivation industry is used.
Description
Technical field
The utility model is related to a kind of filter residue output mechanism and filter press.
Background technology
Filter press is widely applied to field of Environment Protection as a kind of ripe dehydration equipment, as sewage sludge processing
Visual plant.Mechanical dewatering equipment mainly has belt filter press, plate and frame filter press and sleeping spiral shell sedimentation centrifuge in the past, now commonly uses railway carriage or compartment
Formula filter press, vertical hydraulic filter press, diaphragm machine and high pressure board and frame machine.During Sludge landfill, sludge dewatering can greatly reduce sludge
Accumulation place, save the expense that occurs in transportation；When carrying out compost treatment to sludge, sludge dewatering can guarantee that compost
It is smoothed out and (typically requires that sludge has relatively low moisture content in composting process)；If carrying out sludge incineration, focus on, sludge
Dehydration rate height can greatly reduce thermal energy consumption, harm reduction thing processing cost.
The low plastic plate frame pressure filters filter cake moisture content of belt filter press power consumption is low, but sleeping spiral shell sedimentation centrifuge is to sludge stream
Measure the strong adaptability of fluctuation, airtight performance is good, treating capacity is big, occupation of land is small.China past sewage treatment plant mostly using centrifuge,
Belt filter press and plate and frame filter press, small sewage treatment plant typically use thickening all-in-one.Chamber-type press filter is now commonly used,
Diaphragm filter press, and super-pressure vertical hydraulic filter press, its technology are unique, are the ideal equipments of sludge dewatering.Can continuity
Work, belt-type squeezing-dewatering machine has 3 working regions, i.e. gravity dewatering zone, wedge-shaped press-area and shearing press-area,
Its press type belongs to two-dimentional squeezing, is mainly used in sludge dewatering, but its application expands.The dehydration of belt filter press
Effect compares dependence chemical agent, reduces mud and sewage processing cost.
Plate and frame type filter-press：Intermittent pressure filtration facility, for the separation of various solid-liquid suspensions.
Chamber-type press filter：It is to grow up after 1960s.It is characterized in that filter pressure is high, maximum pressure is
Up to 4.5MPa；Unit filter area is big, and the existing 2050 squares product of foreign countries comes out, and domestic maximum filtering area is up to 2000
Square, filter cake liquid content is low, and the filter cake water capacity after squeezing can reduce by 5% one 15% again；Corrosion resistance is good, and filter plate can be used
A variety of enhanced plastics, lightweight, elastic good, corrosion-resistant, wide adaptability；Running expense is low, can be achieved many and works continuously, joins
Machine is controlled.Modern filter press is more based on van-type.
But, the material component such as sludge is complicated, relative density is smaller, particle is thinner, and often colloidal state situation, determines
The characteristics of it is difficult dehydration, so up to the present is in addition to super-pressure vertical hydraulic filter press, remaining filter press increases drying
Or through Exposure to Sunlight process to reduce Residual oil (liquid) rate.
Existing filter, can not all meet the excrement solid-liquid separating treatment of scale raising, there is efficiency on the market
Low, high energy consumption, compression ratio is low, the phenomenon such as unfavorable storage.The screw compression filter that present plant generally uses, per hour only
Pig or the chicken manure of 3 cubic metres of solid-liquids mixing can be handled, and the excrement water content dealt is up to 80%, sunshine or wind again
It is dry 2 days, it can be only achieved recovery and require.There is solid-liquid separation effect poor, efficiency is low, time-consuming, it is impossible to meet scale raising
Excrement solid-liquid separating treatment.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of efficiency high, good effect of separating solid from liquid, can centralized collection
Filter residue, meets filter residue output mechanism and filter press that cultivation industry is used.
In order to solve the above technical problems, a kind of filter residue output mechanism of the present utility model, including fixed mount, motor and circulation
Feeding belt, wherein：Circulation material conveying band front and back end is arranged with active rotating shaft and driven spindle respectively, motor, active rotating shaft and driven
Rotating shaft is fixed on fixed mount, and motor connects active rotating shaft by shaft coupling, and circulation material conveying band upper surface is material containing face, and circulation is sent
Material strip is connected with strainer.
A kind of above-mentioned filter residue output mechanism, circulation material conveying band both sides are provided with striker plate, and striker plate is fixed on fixed mount.
The utility model is used after said structure, and circulation material conveying band connection active rotating shaft and driven spindle, motor drive master
Dynamic axis of rotation, active rotating shaft drives circulation material conveying band and driven spindle to rotate, and realizes purpose of the circulation material conveying with cycle rotation；
Circulation material conveying band is connected with strainer, adjusts the rate of tension of circulation material conveying band, realizes extension circulation material conveying with service life
Purpose；Circulation material conveying band both sides are provided with striker plate, prevent circulation material conveying band material in splicing or transported material from dropping out material containing face.
Filter-pressing device is provided with a kind of filter press, including frame, frame, filter-pressing device includes the press filtration being coaxially oppositely arranged
Cylinder and locked mode set, press filtration cylinder top are provided with before drain pipe port, press filtration cylinder provided with the charging mouth of pipe, press filtration cylinder bottom and locked mode set bottom
Hold as discharging opening, wherein：Including a kind of above-mentioned filter residue output mechanism, circulation material conveying band is arranged on relative position below discharging opening
Put.Material enters filter-pressing device by feeding the mouth of pipe, and filter-pressing device carries out separation of solid and liquid to material, and the liquid material of generation passes through
Drain pipe port is discharged, and solid material is discharged by discharging opening, and solid material is sent to by the splicing below discharging opening of circulation material conveying band
Collecting zone.
A kind of above-mentioned filter press, filter-pressing device also includes master cylinder and auxiliary oil cylinder, and master cylinder and auxiliary oil cylinder are arranged on
Frame two ends, press filtration cylinder front end is provided with provided with fixed outer leaching net in plunger shaft, press filtration chamber provided with press filtration chamber, rear end, living
Fill in and press filtration piston is provided with chamber, master cylinder connection press filtration reciprocating motion of the pistons, auxiliary oil cylinder connection locked mode set is moved back and forth, locked mode set
Axle center is provided with axial slip chamber, and press filtration piston nose is connected with Inner filter net, and Inner filter net is attached in axial slip chamber to by end.
Auxiliary oil cylinder driving locked mode set advance is connected with press filtration cavity seal, Inner filter net is connected in axial slip chamber to by end, material from
The moisture that charging aperture is inputted in press filtration chamber, material is filtered out by outer leaching net and Inner filter net, from drain pipe port discharge, material input
After a certain amount of, master cylinder promotes press filtration piston nose to advance in press filtration chamber along locked mode set direction, and the moisture in material is again
Filtered out by outer leaching net and Inner filter net, solid material is retained in press filtration chamber, realize the purpose of separation of solid and liquid；Work as solid material
Water content reaches after standard that auxiliary oil cylinder driving locked mode set is retreated to be separated with press filtration chamber, and master cylinder driving press filtration piston promotes solid
Body material advances, and solid material is pushed into totally Inner filter net and press filtration piston are drawn back into original position again after discharging opening, makes solid material
On the circulation material conveying band for freely falling to lower section filter residue output mechanism.
A kind of above-mentioned filter press, the charging mouth of pipe is arranged on press filtration chamber top and leads to outer leaching net, and drain pipe port is set respectively
The bottom of the bottom and axial slip intracavitary end in press filtration chamber outer end is put, discharging opening is arranged on press filtration chamber front end.
A kind of above-mentioned filter press, outer leaching net and Inner filter net are respectively spring filter cylinder.
A kind of above-mentioned filter press, is provided with drainage channel, drainage channel connection press filtration between outer leaching net outer wall and press filtration cylinder
The drain pipe port of chamber outer end bottom.Moisture in material is filtered out from outer leaching net to be flow to after drainage channel from hose nozzle outflow.
A kind of above-mentioned filter press, frame is provided with guide rail, and locked mode is put provided with pulley, and locked mode set is connected to by pulley
On guide rail.Locked mode set connects guide rail by pulley, is moved along the rail under auxiliary oil cylinder driving.
A kind of above-mentioned filter press, the discharging opening of press filtration cylinder tilts down setting.The moisture for filtering out material is freely flow to
Press filtration chamber outer end bottom and the drain pipe port of axial slip intracavitary end bottom, make solid material freely be dropped from discharging opening.
A kind of above-mentioned filter press, Inner filter net is to by end, provided with sliding set, sliding set slides with axial slip chamber to be positioned.It is sliding
Shifting is enclosed under master cylinder driving and moved in sliding chamber.
The utility model is mainly used in the excrement solid-liquid separating treatment on pig and chicken plant, is its follow-up solid excrement
Just reclaim and the discharge of water body environmental protection treatment is prepared.
It is an advantage of the invention that in order to produce high efficiency, continuous production, directly go out formula, meet the excrement that cultivation industry uses and consolidate
Liquid separates filter-pressing device.Using this filter press, 10~50 cubic metres of solid-liquid mixtures can be handled per hour.Material after separation
Humidity is 50~60 adjustable, meets and dissipates stacking type entrucking movement requirement.
Brief description of the drawings
The utility model is described in further detail below in conjunction with the specific embodiment in accompanying drawing, but not constituted pair
Any limitation of the present utility model.
Fig. 1 is the cross-sectional view of utility model filter residue output mechanism；
Fig. 2 is Fig. 1 A-A cross-sectional views；
Fig. 3 is the cross-sectional view of the utility model filter press embodiment die opening state；
Fig. 4 is the cross-sectional view of the utility model filter press embodiment mode-lock status；
Fig. 5 is the cross-sectional view of another embodiment of the utility model filter press；
Fig. 6 is Fig. 5 B-B cross-sectional views.
Embodiment
As shown in Figures 1 to 6, a kind of filter residue output mechanism of the present utility model, including fixed mount 1, motor 2 and circulation are sent
Material strip 3, it is characterised in that：The front and back end of circulation material conveying band 3 is arranged with active rotating shaft 31 and driven spindle 32, motor 2, active respectively
Rotating shaft 31 and driven spindle 32 are fixed on fixed mount 1, and motor 2 connects active rotating shaft 31, circulation material conveying band 3 by shaft coupling 21
Upper surface is material containing face, and circulation material conveying band 3 is connected with strainer 34.
The both sides of circulation material conveying band 3 are provided with striker plate 33, and striker plate 33 is fixed on fixed mount 1.
Filter-pressing device 5 is provided with a kind of filter press, including frame 4, frame 4, filter-pressing device 5 includes what is be coaxially oppositely arranged
Press filtration cylinder 54 and locked mode set 55, press filtration 54 tops of cylinder cover 55 bottoms and are provided with provided with the charging mouth of pipe 51, press filtration 54 bottoms of cylinder and locked mode
Drain pipe port 52,54 front ends of press filtration cylinder are discharging opening 53, wherein：Including a kind of above-mentioned filter residue output mechanism, circulation material conveying band 3
It is arranged on the lower section relative position of discharging opening 53.
Filter-pressing device 5 also includes master cylinder 56 and auxiliary oil cylinder 57, and master cylinder 56 and auxiliary oil cylinder 57 are arranged on 4 liang of frame
End, press filtration 54 front ends of cylinder are provided with plunger shaft 542, press filtration chamber 541 provided with fixed outer filter provided with press filtration chamber 541, rear end
Press filtration piston 7 is provided with net 6, plunger shaft 542, the connection press filtration of master cylinder 56 piston 7 is moved back and forth, the connection locked mode set of auxiliary oil cylinder 57
55 move back and forth, and locked mode covers 55 axle center and is provided with axial slip chamber 551, and the front end of press filtration piston 7 is connected with Inner filter net 8, Inner filter net 8 to
It is attached to by end in axial slip chamber 551.
The charging mouth of pipe 51 is arranged on the top of press filtration chamber 541 and leads to outer leaching net 6, and drain pipe port 52 is separately positioned on press filtration chamber
The bottom and the inner bottom of axial slip chamber 551 of the outer end of room 541, discharging opening 53 are arranged on the front end of press filtration chamber 541.
Outer leaching net 6 and Inner filter net 8 are respectively spring filter cylinder.
Drainage channel 61, the outer end of the connection press filtration of drainage channel 61 chamber 541 are provided between the outer wall of outer leaching net 6 and press filtration cylinder 54
The drain pipe port 52 of bottom.
Frame 4 is provided with guide rail 41, and locked mode set 55 is provided with pulley 552, and locked mode set 55 is connected to guide rail by pulley 552
On 41.
The discharging opening 53 of press filtration cylinder 54 tilts down setting.
Inner filter net 8 is to by end, provided with sliding set 81, sliding set 81 slides with axial slip chamber 551 to be positioned.
The utility model is when specifically used, and the driving locked mode of auxiliary oil cylinder 57 set 55 advances to be tightly connected with press filtration chamber 541,
Inner filter net 8 is connected in axial slip chamber 551 to by end, the moisture that material is inputted in press filtration chamber 541, material from charging aperture 51
Filtered out, discharged from drain pipe port 52 by outer leaching net 6 and Inner filter net 8, after material input is a certain amount of, master cylinder 56 promotes press filtration to live
Fill in 7 front ends in press filtration chamber 541 along 55 directions of locked mode set to advance, the moisture in material is again by outer leaching net 6 and Inner filter net 8
Filter out, solid material is retained in press filtration chamber 541, realize the purpose of separation of solid and liquid；When solid material water content reaches standard
Afterwards, the driving of auxiliary oil cylinder 57 locked mode set 55 is retreated separates with press filtration chamber 541, and the driving press filtration of master cylinder 56 piston 7 promotes solids
Material advances, and solid material is pushed into totally Inner filter net 8 and press filtration piston 7 are drawn back into original position again after discharging opening 53, makes solid material
On the circulation material conveying band 3 for freely falling to lower section filter residue output mechanism.
In summary, such as specification and diagramatic content actual sample is made and through test is used for multiple times in the utility model,
In terms of the effect using test, provable the utility model can reach its desired purpose, and practical value is unquestionable.
Embodiment provided above is only used for convenient illustration the utility model, not makees any formal limit to the utility model
System, any those of ordinary skill in the art, if not departing from the range of the utility model carries technical characteristic,
Using the equivalent embodiment for locally changing or modifying made by the utility model disclosed technology content, and without departing from this practicality
New technical characteristic content, in the range of still falling within the utility model technical characteristic.
Claims (10)
1. a kind of filter residue output mechanism, including fixed mount (1), motor (2) and circulation material conveying band (3), it is characterised in that：Circulation is sent
Material strip (3) front and back end is arranged with active rotating shaft (31) and driven spindle (32) respectively, motor (2), active rotating shaft (31) and driven
Rotating shaft (32) is fixed on fixed mount (1), and motor (2) connects active rotating shaft (31), circulation material conveying band (3) by shaft coupling (21)
Upper surface is material containing face, and circulation material conveying band (3) is connected with strainer (34).
2. a kind of filter residue output mechanism according to claim 1, it is characterised in that：Circulation material conveying band (3) both sides are provided with gear
Flitch (33), striker plate (33) is fixed on fixed mount (1).
3. being provided with filter-pressing device (5) in a kind of filter press, including frame (4), frame (4), filter-pressing device (5) includes coaxial relative
The press filtration cylinder (54) and locked mode set (55) of setting, press filtration cylinder (54) top provided with the charging mouth of pipe (51), press filtration cylinder (54) bottom with
Locked mode set (55) bottom is provided with drain pipe port (52), and press filtration cylinder (54) front end is discharging opening (53), it is characterised in that：Including right
It is required that a kind of 1 to 2 any described filter residue output mechanism, circulation material conveying band (3) is arranged on relative position below discharging opening (53).
4. a kind of filter press according to claim 3, it is characterised in that：Filter-pressing device (5) also includes master cylinder (56)
With auxiliary oil cylinder (57), master cylinder (56) and auxiliary oil cylinder (57) are arranged on frame (4) two ends, and press filtration cylinder (54) front end is provided with press filtration chamber
Room (541), rear end are provided with the outer leaching net (6) provided with fixation in plunger shaft (542), press filtration chamber (541), plunger shaft (542)
Provided with press filtration piston (7), master cylinder (56) connection press filtration piston (7) is moved back and forth, and auxiliary oil cylinder (57) connection locked mode set (55) is past
Multiple motion, locked mode set (55) axle center is provided with axial slip chamber (551), and press filtration piston (7) front end is connected with Inner filter net (8), interior filter
Net (8) is attached in axial slip chamber (551) to by end.
5. a kind of filter press according to claim 3 or 4, it is characterised in that：The charging mouth of pipe (51) is arranged on press filtration chamber
(541) lead to outer leaching net (6) on top, and drain pipe port (52) is separately positioned on the bottom of press filtration chamber (541) outer end and axially sliding
The inner bottom of chamber (551) is moved, discharging opening (53) is arranged on press filtration chamber (541) front end.
6. a kind of filter press according to claim 4, it is characterised in that：Outer leaching net (6) and Inner filter net (8) are respectively spring
Formula filter cylinder.
7. a kind of filter press according to claim 5, it is characterised in that：Between outer leaching net (6) outer wall and press filtration cylinder (54)
Provided with drainage channel (61), drainage channel (61) connects the drain pipe port (52) of press filtration chamber (541) outer end bottom.
8. a kind of filter press according to claim 3, it is characterised in that：Frame (4) is provided with guide rail (41), locked mode set
(55) pulley (552) is provided with, locked mode set (55) is connected on guide rail (41) by pulley (552).
9. a kind of filter press according to claim 3, it is characterised in that：The discharging opening (53) of press filtration cylinder (54) dips down
Tiltedly set.
10. a kind of filter press according to claim 4, it is characterised in that：Inner filter net (8) Xiang Youduan covers provided with sliding
(81), sliding set (81) slides with axial slip chamber (551) and positioned.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621369655.7U CN206492277U (en) | 2016-12-14 | 2016-12-14 | A kind of filter residue output mechanism and filter press |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621369655.7U CN206492277U (en) | 2016-12-14 | 2016-12-14 | A kind of filter residue output mechanism and filter press |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206492277U true CN206492277U (en) | 2017-09-15 |
Family
ID=59800500
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621369655.7U Expired - Fee Related CN206492277U (en) | 2016-12-14 | 2016-12-14 | A kind of filter residue output mechanism and filter press |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206492277U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110217963A (en) * | 2019-06-03 | 2019-09-10 | 广东恒鑫智能装备股份有限公司 | A kind of vertical sludge extruding-desiccation machine |
-
2016
- 2016-12-14 CN CN201621369655.7U patent/CN206492277U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110217963A (en) * | 2019-06-03 | 2019-09-10 | 广东恒鑫智能装备股份有限公司 | A kind of vertical sludge extruding-desiccation machine |
| CN110217963B (en) * | 2019-06-03 | 2021-11-23 | 广东恒鑫智能装备股份有限公司 | Vertical sludge extrusion dehydrator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170915 Termination date: 20191214 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |