CN205360710U - But dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation - Google Patents
But dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation Download PDFInfo
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- CN205360710U CN205360710U CN201620119867.3U CN201620119867U CN205360710U CN 205360710 U CN205360710 U CN 205360710U CN 201620119867 U CN201620119867 U CN 201620119867U CN 205360710 U CN205360710 U CN 205360710U
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Abstract
The utility model discloses a but dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation. It includes hydro -cylinder, hydro -cylinder seat, girder, pressure plate, thrust plate and a plurality of filter frame, the front end of filter frame, rear end are equipped with respectively and bulldoze board, bearing plate, it is equipped with a plurality of seal spring to bulldoze on same circumference between board and the bearing plate, bearing plate and filter plate mounting panel fixed connection, fixed filter plate and filter plate mounting panel fixed connection, fixed mounting has the piston axle on the fixed filter plate, ejecting filter plate and piston axle fixed connection, be equipped with ejecting spring between fixed filter plate and ejecting filter plate. The utility model discloses the improvement has been done on current superhigh pressure elasticity squeezer: through fixed mounting piston axle on fixed filter plate, the ejecting filter plate of the epaxial fixed mounting of piston again, but make original elasticity squeezer become piston varactor pressure filter, through set up ejecting spring between fixed filter plate and ejecting filter plate, realized that the filter cake unloads automatically.
Description
Technical field
This utility model belongs to filtration art, relates to High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after a kind of coal slime flotation.
Background technology
From discarded coal slime, extract the low-ash cleaning cleaned coal of low-sulfur by dosing flotation, be a kind of energy-conserving and environment-protective new technology, this new technology route need use a kind of filtering separation device that High water cut cleaned coal after coal slime flotation can be made directly dehydration.
Applicant is for whole 3 years of the research and development of High water cut cleaned coal dehydration filtering separation device after coal slime flotation, in this process, they have visited domestic main filtering separation device manufacture, have used producer, multi-form technology communication and investigation has been carried out with these producers, the filtering separation devices such as rotary drum vacuum filter, the miscible squeezer of belt, various centrifuge, chamber filter press, elastic sheet frame squeezer have carried out many times lab scale, pilot plant test, achieve substantial amounts of experimental data.But end product finds, it does not have a kind of existing equipment can be directly applied to after coal slime flotation on the dewatering and filtering of High water cut cleaned coal separates, only elastic sheet frame squeezer relatively its requirement.Difficult point mainly has four, and one is that requirement cleaned coal moisture content is low, cleaned coal moisture content≤9% after filtration；Two is that requirement yield is big, and treating capacity is big, cleaned coal absolute treating capacity >=10 ton hour platform；Three is that squeeze pressure is big, >=5.5MPa；Four is should be able to realize automatically unloading mud cake.
And existing filtering separation device all cannot meet these technological requirements, the shortcoming of prior art is as follows:
(1) squeeze pressure is inadequate, domestic squeeze pressure≤5MPa.
(2) treating capacity is inadequate, what the elastic sheet frame squeezer treating capacity of domestic production was maximum is TCYZ200 (1770) type that Shanghai Techase Environment Protection Co., Ltd. produces, and its treating capacity is over dry mud 4 ton hour platform.
(3) moisture content does not reach, moisture content >=20% of existing squeezer filter cake.
(4) can not realizing filter cake automatically to drop, during moisture content≤9% of particularly cleaned coal, filter cake is very dry very hard, is often stuck in filter plate space.
(5) the filter chamber degree of depth of existing filtering separation device is at 10～30mm, and treating capacity is little, and efficiency is low.
Utility model content
The purpose of this utility model is in that to overcome the deficiencies in the prior art, it is provided that a kind of improve on existing supertension elasticity squeezer basis, can meet High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after the coal slime flotation of technological requirement.
The technical solution of the utility model is as follows:
High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after a kind of coal slime flotation, it includes oil cylinder, oil cylinder seat, girder, pressure plare, thrust plate, and is located at the some filter frames between pressure plare and thrust plate；The front and back of filter frame are respectively provided on two sides with push plate, bearing plate；On same circumference, some Packing springs it are provided with between push plate and bearing plate；Bearing plate is fixing with filter plate installing plate to be connected；Fixing filter plate is fixing with filter plate installing plate to be connected；Fixing filter plate is installed with piston shaft；Eject that filter plate and piston shaft are fixing to be connected；At fixing filter plate with eject and be provided with ejector spring between filter plate.
Fixing filter plate is installed with four piston shaft；Four piston shaft are uniformly distributed on same circumference.
At fixing filter plate with eject and be provided with four ejector springs between filter plate on same circumference；Four ejector springs are evenly distributed on same circumference.
The beneficial effects of the utility model:
High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after coal slime flotation of the present utility model, following improvement is done on the basis of existing supertension elasticity squeezer: 1, by fixedly mounting piston shaft on fixing filter plate, on piston shaft, fixed installation ejects filter plate again, make original elastic squeezer become piston type variable and hold pressure filter so that it is disclosure satisfy that the dewatering and filtering separating technology requirement of High water cut cleaned coal after coal slime flotation.2, by fixing filter plate with eject and arrange ejector spring between filter plate, it is achieved that filter cake drops (spring dump) automatically.
After coal slime flotation of the present utility model, High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter, has the advantage that
(1) squeeze pressure of this ultra-high pressure piston type variable capacity squeezer is up to 6～9MPa；
(2) after this ultra-high pressure piston type variable capacity squeezer dehydration, moisture content≤9% of cleaned coal；
(3) the cleaned coal treating capacity of this ultra-high pressure piston type variable capacity squeezer has reached over dry mud 11～13 ton hour platform；(4) decrement of this ultra-high pressure piston type variable capacity squeezer is up to 15%～20%；
(5) this ultra-high pressure piston type variable capacity squeezer sheet frame specialized designs filter cake appliance for releasing single lowering device, solves briquette difficulty and drops problem.
Accompanying drawing explanation
Fig. 1 is the complete machine structure schematic diagram of the ultra-high pressure piston type variable capacity pressure filter in this utility model；
Fig. 2 is the Facad structure schematic diagram of the filter frame assembly in this utility model；
Fig. 3 is the filter frame side view (entering pureed state) in this utility model；
Fig. 4 is the filter frame side view (discharging state) in this utility model.
In figure: 1 enters mud pipe, 2 thrust plates, 3 girders, 4 filter frames, 5 pressure plares, 6 oil cylinder seats, 7 oil cylinders, 8 Hydraulic Stations, 9 ear shoulders, 10 running rollers, 11 bearing plates, 12 fixing filter plates, 13 Packing springs, 14 filter plate installing plates, 15 piston shaft, 16 ejector springs, 17 push plate, 18 eject filter plate, 19 filter clothes
Detailed description of the invention
Below in conjunction with drawings and Examples, this utility model is further described.
As shown in Figure 1, High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after this utility model one coal slime flotation, it includes oil cylinder 7, oil cylinder seat 6, girder 3, pressure plare 5, thrust plate 2, and is located at the parts such as some filter frames 4 between pressure plare 5 and thrust plate 2.
As it is shown on figure 3, the front and back of filter frame 4 are respectively provided on two sides with push plate 17, bearing plate 11；On same circumference, some Packing springs 13 it are provided with between push plate 17 and bearing plate 11；Bearing plate 11 is fixing with filter plate installing plate 14 to be connected；Fixing filter plate 12 is fixing with filter plate installing plate 14 to be connected；Fixing filter plate 12 is uniformly distributed on same circumference and is installed with four piston shaft 15；Eject that filter plate 18 and four piston shaft 15 are fixing to be connected；At fixing filter plate 12 with eject and be provided with four ejector springs 16 (depicting laterally zygomorphic two ejector springs 16 in Fig. 3) between filter plate 18 on same circumference.
As in figure 2 it is shown, filter frame assembly is provided with ear shoulder 9, running roller 10, thus filter frame may be mounted on girder 3.
Work process includes: pre-pressing stage, charging stage, squeezing stage, four main process of pulling plate unloading stage.
Pre-pressing stage: start Hydraulic Station 8 and drive oil cylinder 7 that filter frame 4 is pushed to thrust plate 2 side, make each filter frame 4 closely be adjacent to；As it is shown on figure 3, filter frame 4 outer ring can be extruded shortening at pressure-bearing sheet frame and the Packing spring 13 pushed between sheet frame under oil cylinder working-pressure effect；The elastic range design load of Packing spring 13 can be controlled in 10～30mm.
Charging stage: coal slurry is squeezed in filter frame 4 through entering mud pipe 1 by plunger displacement pump, moisture oozes through filter cloth 19, coal slurry is gradually filled with filter frame 4, concentration gradually rises, meanwhile, the coal slurry of high concentration produces pressure gradually, and promotion ejects filter plate 18 and moves to the inside, ejector spring 16 is compressed, absorption portion potential energy；After ejector spring 16 compression section stroke, fitting with filter plate installing plate 14 in filter plate 18 back that ejects connected together with it, no longer retreats.
The squeezing stage: be again started up oil cylinder 7, filter frame 4 is pushed to thrust plate 2 direction, under high pressure effect, Packing spring 13 is extruded further, as shown in Figure 3, Figure 4, A=65～80mm when the filter chamber degree of depth is from charging is extruded to about B=30～50mm, and pressure can be increased to 5～9MPa, and coal slurry is extruded as briquette (filter cake)；Briquette moisture content is down to about 10%～8%.
In the pulling plate unloading stage: oil cylinder 7 return, the strength release of Packing spring 13, filter frame 4 recovers to free state, by the drawing-plate mechanism that equipment carries, is pulled open successively by filter plate；Pulling open because ejector spring 16 potential energy discharges in process, promotion ejects filter plate 18 and shifts, and this strength can overcome the adhesion between briquette and framework.Such briquette is natural to be separated with framework, deviates from filter frame, completes discharging.
The main technical point of ultra-high pressure piston type variable capacity pressure filter of the present utility model is as follows:
1, big volume, decrement is up to 15%～20%；
2, high pressure, squeeze pressure is up to 5～9MPa；
3, novel auxiliary discharge way (spring dump), can realize filter cake and automatically drop.
Claims (5)
1. High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after a coal slime flotation, it is characterised in that it includes oil cylinder, oil cylinder seat, girder, pressure plare, thrust plate, and is located at the some filter frames between pressure plare and thrust plate；The front end of filter frame, rear end are respectively equipped with push plate, bearing plate；On same circumference, some Packing springs it are provided with between push plate and bearing plate；Bearing plate is fixing with filter plate installing plate to be connected；Fixing filter plate is fixing with filter plate installing plate to be connected；Fixing filter plate is installed with piston shaft；Eject that filter plate and piston shaft are fixing to be connected；At fixing filter plate with eject and be provided with ejector spring between filter plate.
2. High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after coal slime flotation as claimed in claim 1, it is characterised in that be installed with four piston shaft on fixing filter plate.
3. High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after coal slime flotation as claimed in claim 2, it is characterised in that four piston shaft are uniformly distributed on same circumference.
4. High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after the coal slime flotation as described in claim 1,2 or 3, it is characterised in that at fixing filter plate with eject and be provided with four ejector springs between filter plate on same circumference.
5. High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after coal slime flotation as claimed in claim 4, it is characterised in that four ejector springs are evenly distributed on same circumference.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620119867.3U CN205360710U (en) | 2016-02-14 | 2016-02-14 | But dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620119867.3U CN205360710U (en) | 2016-02-14 | 2016-02-14 | But dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation |
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| Publication Number | Publication Date |
|---|---|
| CN205360710U true CN205360710U (en) | 2016-07-06 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620119867.3U Withdrawn - After Issue CN205360710U (en) | 2016-02-14 | 2016-02-14 | But dehydration of high moisture clean coal is with superhigh pressure piston varactor pressure filter after coal slime flotation |
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| CN (1) | CN205360710U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106267936A (en) * | 2016-02-14 | 2017-01-04 | 上海同臣环保有限公司 | High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after a kind of coal slime flotation |
| CN109925771A (en) * | 2019-04-22 | 2019-06-25 | 重庆长能环境科技有限公司 | A kind of compressible oil cylinder sheet frame filter plate of super-pressure |
| CN109987748A (en) * | 2019-04-22 | 2019-07-09 | 重庆长能环境科技有限公司 | A kind of black water intelligent processing method and its equipment |
| CN110078341A (en) * | 2019-04-28 | 2019-08-02 | 中铁四局集团有限公司 | Slurry solid-liquid separator and process |
-
2016
- 2016-02-14 CN CN201620119867.3U patent/CN205360710U/en not_active Withdrawn - After Issue
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106267936A (en) * | 2016-02-14 | 2017-01-04 | 上海同臣环保有限公司 | High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity pressure filter after a kind of coal slime flotation |
| CN106267936B (en) * | 2016-02-14 | 2018-05-25 | 上海同臣环保有限公司 | High water cut cleaned coal dehydration ultra-high pressure piston type variable capacity filter press after a kind of coal slime flotation |
| CN109925771A (en) * | 2019-04-22 | 2019-06-25 | 重庆长能环境科技有限公司 | A kind of compressible oil cylinder sheet frame filter plate of super-pressure |
| CN109987748A (en) * | 2019-04-22 | 2019-07-09 | 重庆长能环境科技有限公司 | A kind of black water intelligent processing method and its equipment |
| CN110078341A (en) * | 2019-04-28 | 2019-08-02 | 中铁四局集团有限公司 | Slurry solid-liquid separator and process |
| CN110078341B (en) * | 2019-04-28 | 2022-04-12 | 中铁四局集团有限公司 | Slurry solid-liquid separator and process |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160706 Effective date of abandoning: 20180525 |