CN101349156A - Backwashing high pressure filtering station - Google Patents

Backwashing high pressure filtering station Download PDF

Info

Publication number
CN101349156A
CN101349156A CNA2008101209199A CN200810120919A CN101349156A CN 101349156 A CN101349156 A CN 101349156A CN A2008101209199 A CNA2008101209199 A CN A2008101209199A CN 200810120919 A CN200810120919 A CN 200810120919A CN 101349156 A CN101349156 A CN 101349156A
Authority
CN
China
Prior art keywords
backwash
filtration chamber
back flushing
channel
valve
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.)
Pending
Application number
CNA2008101209199A
Other languages
Chinese (zh)
Inventor
赵雪祥
陈其淼
孙伟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
YUEQING DONGFENG COAL MINE EQUIPMENT CO Ltd
Original Assignee
YUEQING DONGFENG COAL MINE EQUIPMENT CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by YUEQING DONGFENG COAL MINE EQUIPMENT CO Ltd filed Critical YUEQING DONGFENG COAL MINE EQUIPMENT CO Ltd
Priority to CNA2008101209199A priority Critical patent/CN101349156A/en
Publication of CN101349156A publication Critical patent/CN101349156A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Filtration Of Liquid (AREA)

Abstract

The invention relates to a back flushing high-pressure filtration station. A back flushing module is arranged on an assembly box body. A valve body of the back flushing module is provided with an input channel, an output channel, a back flushing channel, an entrance of a left filter chamber and an entrance of a right filter chamber. Valve seats, valve pads and steel balls are respectively arranged in the back flushing channel and the entrances of the right and left filter chambers. The steel balls are respectively matched with right and left operating mechanisms where right and left back flushing switch handles are respectively fixed. An L-shaped channel is arranged inside each steel ball. The entrances of the right and left filter chambers are respectively connected with the right and left filter chambers, and the right and left ends of the back flushing channel are respectively connected with back flushing outlet connectors of the right and left filter chambers. The input channel is connected with a connector of an input port, and the output channel is connected with a connector of an output port. The connectors of the back flushing outlet of the right and left filter chambers are connected with each other through a pipeline, and a one-way valve is arranged in front of the connector of the back flushing outlet. An input ball-shaped check valve is arranged in front of the connector of the input port connector, and an output ball-shaped check valve is arranged behind the connector of the output port. The back flushing high-pressure filtration station can control the inherent cleanliness of working medium emulsion of a hydraulic system for a downhole comprehensive hydraulic support in a coal mine from the source.

Description

Backwash high pressure filtering station
Technical field
The present invention relates to a kind of backwash high pressure filtering device that is used for comprehensive mining hydraulic bracket hydraulic system under the coal mine, refer in particular to a kind of backwash high pressure filtering device.
Technical background
The hydraulic system that comprehensive mining hydraulic bracket adopts under the coal mine, be in down-hole coal ash high pollution situation, hydraulic system source emulsion tank very easily is subjected to the coal ash powder dust pollution, cause heel and toe wear or damage for each seal of hydraulic system, cause hydraulic system unit time internal fault to take place frequently, cause very big harm for the fully-mechanized mining equipment operate as normal.Existing coal production enterprise, hydraulic medium pollution control engineering technological means mainly concentrates on auxilliary establishing system miniaturization filtration and washing engineering device on each function valve member assembly of subsystem application section, and this resolution system is used section pollution control problem.Because Aided Design engineering device is limited by function valve member volume conditions, can not assist and join big traffic engineering device, the pollution problem of hydraulic pressure total system can not be solved in control, certainly will cause whole hydraulic system internal contamination substrate concentration more and more higher, cause subsystem function valve member responsibilities function and dual the increasing the weight of of hydraulic medium filtering function live load.Because the low capacity filter is faced the more and more higher hydraulic medium of pollution concentration directly, the normal mechanical function must be subjected to grievous injury, very easily causes various seal heel and toe wears or damage, influences system's operate as normal efficient.
Summary of the invention
The object of the present invention is to provide a kind of backwash high pressure filtering station, carrying out initial one-level working media from the hydraulic system source filters, improve the inherent cleannes of hydraulic work system medium emulsion from source control, for hydraulic system provides comparatively desirable cleaning medium emulsion, alleviate each element filters medium live load of subsystem, further carry the job stability of high comprehensive mining hydraulic system, reduce each class component sealing maintenance works, improve unit labor productivity, reduce system failure incidence, prolong the application life of each class component of hydraulic system.
For achieving the above object, the invention takes solution to be: a kind of backwash high pressure filtering station, the backwash module is housed on the assembly casing, the valve body of backwash module has input channel, output channel, the backwash passage, filtration chamber, left side inlet and right filtration chamber inlet, valve seat is placed in backwash passage and entrance, left filtration chamber, valve pad and steel ball, steel ball and left operating mechanism are supporting, fix left backwash switch knob on the operating mechanism of a left side, valve seat is placed in backwash passage and entrance, right filtration chamber, valve pad and steel ball, steel ball and right operating mechanism are supporting, fix right backwash switch knob on the right operating mechanism, have L shaped passage in the steel ball, filtration chamber, left side inlet connects left filtration chamber, right filtration chamber inlet connects right filtration chamber, backwash passage left end connects left filtration chamber's backwash outlet connection, backwash passage right-hand member connects right filtration chamber's backwash outlet connection, input channel connects the input port joint, output channel connects the delivery outlet joint, filtration chamber's backwash outlet connection in a left side is connected and preposition one way valve by pipeline with right filtration chamber's backwash outlet connection, the spherical stop valve of the preposition input of input port joint, the spherical stop valve of the rearmounted output of delivery outlet joint.
The duty of filtration chamber is to control each other dielectric fluid flow path direction by backwash switch knob and operating mechanism.In normal operation, liquid medium is by the filtration chamber that flows through of L passage in the steel ball in the valve body, from output channel output, for the hydraulic system applications section provides the working media liquid of cleaning through primary filter.Because during flow of high-pressure fluid process filter chamber, mechanical admixture in the liquid is with filtration resistance, growth along with service time, mechanical admixture is more and more in the filtration chamber, the pressure at two ends difference of filter element is increasing in the filtration chamber, when pressure reduction reaches certain numerical value, then needs to carry out the backwash working programme, otherwise will influence system works efficient, then cause failure accident when serious.Manually carry out the mutual backwash of filtration chamber by switch knob.Drive the operating mechanism that is controlled in the valve body by the switch switch knob.Rotate an operating mechanism input side will be closed to the inlet of next filtration chamber, meanwhile, the backwash of pent filtration chamber is activated.The medium that need purify flows through the filtration chamber in this work fully in backwash process.The medium that has been filtered of a part, through outlet side flow to open etc. in the filtration chamber subject to backwash, flow through round about and the impurity of the inside taken out of by the backwash outlet.The backwash of two filtration chambers often hockets, and that is to say on-streamly ceaselessly to clean two filtration chambers.
This flushing high pressure filtering station, carrying out initial one-level working media from the hydraulic system source filters, improve the inherent cleannes of hydraulic work system medium emulsion from source control, for hydraulic system provides comparatively desirable cleaning medium emulsion, alleviate each element filters medium live load of subsystem, further carry the job stability of high comprehensive mining hydraulic system, reduce each class component sealing maintenance works, improve unit labor productivity, reduce system failure incidence, prolong the application life of each class component of hydraulic system.
Description of drawings
Fig. 1 is present embodiment (removing a assembly casing) structural representation.Fig. 2 is a present embodiment hydraulic system schematic diagram.Fig. 3 is the part sectional structure schematic diagram with manometric backwash module.Fig. 4 is the A-A sectional view among Fig. 3.Fig. 5 is the work of right filtration chamber, operating mechanism handle position figure when left filtration chamber carries out backwash.Fig. 6 is operating mechanism handle position figure when in running order of two filtration chambers.Fig. 7 is the work of left filtration chamber, operating mechanism handle position figure when right filtration chamber carries out backwash.Fig. 8 is a backwash module normal filtration fundamental diagram.Fig. 9 is that filtration chamber, a backwash module left side carries out the backwash fundamental diagram.Figure 10 is that the right filtration chamber of backwash module carries out the backwash fundamental diagram.
Among the figure: 1, one way valve, 2, import spherical stop valve, 3, the input pressure table, 4, the backwash module, 4-1, the input port joint, 4-2, left side filtration chamber's backwash outlet connection, 4-3, valve body, 4-4, left side operating mechanism, 4-5, right operating mechanism, 4-6, right filtration chamber's backwash outlet connection, 4-7, the delivery outlet joint, 4-8, right backwash switch knob, 4-9, right filtration chamber, 4-10, gland, 4-11, retainer ring, 4-12, cylinder barrel, 4-13, filtration chamber, a left side, 4-14, element kit, 4-15, left side backwash switch knob, 4-16, valve pad, 4-17, steel ball, 4-18, valve seat, 5, delivery gauge, 6, export spherical stop valve.
The specific embodiment
Below in conjunction with embodiment and accompanying drawing thereof the present invention is remake description.
Referring to Fig. 1, Fig. 3 and Fig. 4, a kind of backwash high pressure filtering station, backwash module 4 is housed on the assembly casing, the valve body 4-3 of backwash module 4 has input channel, output channel, the backwash passage, filtration chamber, left side inlet and right filtration chamber inlet, valve seat 4-18 is placed in backwash passage and entrance, left filtration chamber, valve pad 4-16 and steel ball 4-17, steel ball 4-17 and left operating mechanism 4-4 are supporting, left side operating mechanism 4-4 goes up fixing left backwash switch knob 4-15, valve seat 4-18 is placed in backwash passage and entrance, right filtration chamber, valve pad 4-16 and steel ball 4-17, steel ball 4-17 and right operating mechanism 4-5 are supporting, right operating mechanism 4-5 goes up fixing right backwash switch knob 4-8, have L shaped passage among the steel ball 4-17, filtration chamber, left side inlet connects the left 4-13 of filtration chamber, right filtration chamber inlet connects the right 4-9 of filtration chamber, backwash passage left end meets left filtration chamber's backwash outlet connection 4-2, backwash passage right-hand member meets right filtration chamber's backwash outlet connection 4-6, input channel meets input port joint 4-1, output channel meets delivery outlet joint 4-7, left side filtration chamber's backwash outlet connection 4-2 is connected and preposition one way valve 1 by pipeline with right filtration chamber's backwash outlet connection 4-6, the spherical stop valve 2 of the input port preposition input of joint 4-1, the spherical stop valve 6 of the rearmounted output of delivery outlet joint 4-7.
Referring to Fig. 3, described left 4-13 of filtration chamber and the right 4-9 of filtration chamber are made of cylinder barrel 4-12, element kit 4-14 and gland 4-14, place element kit 4-14 among the cylinder barrel 4-12, and element kit 4-14 lower port is filled in gland 4-14.
Referring to Fig. 3, retainer ring 4-11 is equipped with in described left 4-13 of filtration chamber and 4-9 lower end, right filtration chamber.The effect of retainer ring 4-11 is to prevent on-stream because of carelessness that element kit 4-14 is looseningly, has guaranteed and can only just can unclamp element kit 4-14 under stress-free state.
Referring to Fig. 1-Fig. 3, Fig. 8-Figure 10, insert input pressure table 3 in the described input channel, insert delivery gauge 5 in the described output channel.Input pressure table 3 and delivery gauge 5 show that respectively the working media highly pressurised liquid filters front and back pressure.When high-pressure fluid was flowed through left 4-13 of filtration chamber and the right 4-9 of filtration chamber, the mechanical admixture in the liquid will be formed and stop up by filtration resistance, produces pressure reduction (input pressure table 3 is different with the value of reading of delivery gauge 5) at the left 4-13 of filtration chamber with 4-9 two ends, right filtration chamber immediately.Mechanical admixture among left side 4-13 of filtration chamber and the right 4-9 of filtration chamber is many more, and pressure differential is big more.
Referring to Fig. 6 and Fig. 8, Fig. 5 and Fig. 9, Fig. 7 and Figure 10, when left backwash switch knob 4-15 and right backwash switch knob 4-8 were in vertical position, left 4-13 of filtration chamber and the right 4-9 of filtration chamber were in the normal filtration state; When left backwash switch knob 4-15 manually turns left to be horizontal when being in vertical position with right backwash switch knob 4-8, the left 4-13 of filtration chamber carries out backwash; Be horizontal when being in vertical position with left backwash switch knob 4-15 when right backwash switch knob 4-8 manually turns right, the right 4-9 of filtration chamber carries out backwash.
It is to be noted, on the assembly casing, can two or more backwash modules 4 be housed parallel connection, the delivery outlet joint 4-7 of first backwash module 4 connects next backwash module 4 input port joint 4-1, by that analogy, the spherical stop valve 6 of the rearmounted output of the delivery outlet joint 4-7 of last backwash module 4.This backwash high pressure filtering station also belongs to protection domain of the present invention.

Claims (4)

1, a kind of backwash high pressure filtering station, it is characterized in that: backwash module (4) is housed on the assembly casing, the valve body (4-3) of backwash module (4) has input channel, output channel, the backwash passage, filtration chamber, left side inlet and right filtration chamber inlet, valve seat (4-18) is placed in backwash passage and entrance, left filtration chamber, valve pad (4-16) and steel ball (4-17), steel ball (4-17) is supporting with left operating mechanism (4-4), left side operating mechanism (4-4) is gone up fixing left backwash switch knob (4-15), valve seat (4-18) is placed in backwash passage and entrance, right filtration chamber, valve pad (4-16) and steel ball (4-17), steel ball (4-17) is supporting with right operating mechanism (4-5), right operating mechanism (4-5) is gone up fixing right backwash switch knob (4-8), have L shaped passage in the steel ball (4-17), filtration chamber, left side inlet connects left filtration chamber (4-13), right filtration chamber inlet connects the right (4-9 of filtration chamber,) backwash passage left end connects left filtration chamber's backwash outlet connection (4-2), backwash passage right-hand member connects right filtration chamber's backwash outlet connection (4-6), input channel connects input port joint (4-1), output channel connects delivery outlet joint (4-7), left side filtration chamber's backwash outlet connection (4-2) is connected and preposition one way valve (1) by pipeline with right filtration chamber's backwash outlet connection (4-6), the spherical stop valve (2) of the preposition input of input port joint (4-1), the rearmounted output of delivery outlet joint (4-7) spherical stop valve (6).
2, backwash high pressure filtering station according to claim 1, it is characterized in that: described left filtration chamber (4-13) and right filtration chamber (4-9) are made of cylinder barrel (4-12), element kit (4-14) and gland (4-14), place element kit (4-14) in the cylinder barrel (4-12), element kit (4-14) lower port is filled in gland (4-14).
3, backwash high pressure filtering station according to claim 2 is characterized in that: retainer ring (4-11) is equipped with in described left filtration chamber (4-13) and lower end, right filtration chamber (4-9).
4, backwash high pressure filtering station according to claim 1 is characterized in that: insert input pressure table (3) in the described input channel, insert delivery gauge (5) in the described output channel.
CNA2008101209199A 2008-09-05 2008-09-05 Backwashing high pressure filtering station Pending CN101349156A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNA2008101209199A CN101349156A (en) 2008-09-05 2008-09-05 Backwashing high pressure filtering station

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA2008101209199A CN101349156A (en) 2008-09-05 2008-09-05 Backwashing high pressure filtering station

Publications (1)

Publication Number Publication Date
CN101349156A true CN101349156A (en) 2009-01-21

Family

ID=40268098

Family Applications (1)

Application Number Title Priority Date Filing Date
CNA2008101209199A Pending CN101349156A (en) 2008-09-05 2008-09-05 Backwashing high pressure filtering station

Country Status (1)

Country Link
CN (1) CN101349156A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103047228A (en) * 2012-12-20 2013-04-17 三一重型装备有限公司 Backwash filter device and working face hydraulic system
CN103861345A (en) * 2014-03-27 2014-06-18 巨隆集团芜湖兴隆液压有限公司 Pipeline type filtering device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103047228A (en) * 2012-12-20 2013-04-17 三一重型装备有限公司 Backwash filter device and working face hydraulic system
CN103047228B (en) * 2012-12-20 2015-06-10 三一重型装备有限公司 Backwash filter device and working face hydraulic system
CN103861345A (en) * 2014-03-27 2014-06-18 巨隆集团芜湖兴隆液压有限公司 Pipeline type filtering device
CN103861345B (en) * 2014-03-27 2015-10-07 巨隆集团芜湖兴隆液压有限公司 A kind of pipeline type filter

Similar Documents

Publication Publication Date Title
CN101614225B (en) Automatic discharge and self-cleaning filter device for emulsion pump station
CN101766927B (en) High-pressure and high-precision backwashing filtration station
CN201271542Y (en) Back washing type high pressure filter station
DE29909100U1 (en) Pipe arrangement with filter
CN201168497Y (en) Back washing type high pressure filter station
CN102258910B (en) Backwashing high-pressure filter station
CN101349156A (en) Backwashing high pressure filtering station
US3306451A (en) Filter assembly having check valve and bypass conduit
CN201613055U (en) High-pressure high-precision backflushing filter station
CN105935679A (en) Multifunctional oil flushing device and application method thereof
CN204093171U (en) A kind of wellhead of water injection well filter
CN206958031U (en) Fully-mechanized mining working hydraulic system filter
CN104533478A (en) Hydraulic system used for recycling emulsified liquid of coal face
CN218280813U (en) High-pressure backwashing filter station
CN204371377U (en) The hydraulic system of emulsion is reclaimed for coal-face
CN214233088U (en) Movable high-pressure automatic backwashing filter device
CN203525402U (en) Backflushing filter and water filter device of pipeline
CN103285646B (en) Automatic backwashing filter
CN210905221U (en) High-pressure emulsion backwashing filter station
CN210905220U (en) Single-cylinder high-pressure emulsion backwashing filter station
CN213680106U (en) Pure all-in-one of full room water purification
CN103623630A (en) Full-automatic high-pressure back-flushing filtering station
CN204365018U (en) Automatic backwashing filter
CN216023569U (en) Back-washing high-pressure filtering station
CN103495306A (en) Automatic backwash filter with rated flow of 900L/min

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Open date: 20090121