CN203861998U - Device for filtering and automatic backwash of returned liquid on emulsification site - Google Patents
Device for filtering and automatic backwash of returned liquid on emulsification site Download PDFInfo
- Publication number
- CN203861998U CN203861998U CN201420276830.2U CN201420276830U CN203861998U CN 203861998 U CN203861998 U CN 203861998U CN 201420276830 U CN201420276830 U CN 201420276830U CN 203861998 U CN203861998 U CN 203861998U
- Authority
- CN
- China
- Prior art keywords
- liquid
- filter
- emulsion
- recover
- backwash 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
Landscapes
- Filtration Of Liquid (AREA)
Abstract
The utility model provides a device for filtering and automatic backwash of returned liquid on an emulsification site. The device comprises a high-pressure emulsion inlet, a waste liquid recoverer, a recoverer filter element, emulsion boxes, an electromagnetic valve A, an electromagnetic valve B, a site returned liquid inlet, a one-way valve, a returned liquid backwash filter, a filter element and a differential-pressure check valve, wherein the liquid inlet of the returned liquid backwash filter is connected with the site returned liquid inlet and the liquid inlet of the waste liquid recoverer through pipelines; the liquid outlet of the waste liquid recoverer is connected with the emulsion box A; the liquid outlet of the returned liquid backwash filter is connected with the high-pressure emulsion inlet and the emulsion box B through pipelines; the electromagnetic valve A is arranged on the connecting pipeline of the returned liquid backwash filter and the high-pressure emulsion inlet; the electromagnetic valve B is arranged on the connecting pipeline of the returned liquid backwash filter and the emulsion box B. The device has the benefits as follows: the automatic backwash function is realized, on-line cleaning and replacement of the filter element of the device can be carried out during the working process, and the continuous production requirements of a coal mine can be met.
Description
Technical field
The utility model relates to mining equipment technical field, more specifically says that the on-the-spot liquid that returns of a kind of emulsification filters automatic back-flushing device.
Background technology
What colliery mostly adopted with hydraulic test is emulsion is as working media, and the cleannes of emulsion are directly connected to service behaviour and the service life thereof of hydraulic test; Foreign material that emulsion is taken out of in the time recycling in process through hydraulic test and cause coal dust that the factors such as working environment under particle and the coal mine coming off produce etc. all can pollute emulsion with inner-walls of duct through friction, make hydraulic test cisco unity malfunction or cause damage, therefore, emulsion is recycled to filtration in process very important, existing filter does not possess automatic back-flushing function, in the filter course of work, do not realize Hand scarf filter core and renew cartridge more online, can not meet the requirement that colliery serialization is produced.
Summary of the invention
For addressing the above problem, the utility model has designed one can realize automatic back-flushing function, in the course of work, can carry out Hand scarf filter core and renew cartridge more to device, the on-the-spot liquid that returns of emulsification that meets the continuous production requirement in colliery filters automatic back-flushing device, its technical scheme is: the on-the-spot liquid that returns of described emulsification filters automatic back-flushing device by high-pressure emulsion import, waste liquid recover, recover filter core, emulsion box, magnetic valve A, magnetic valve B, on-the-spot time liquid import, check valve, return liquid backwash filter, filter element, differential pressure check valve composition, the inlet that it is characterized in that back liquid backwash filter uses pipeline to return liquid import with scene respectively, the inlet of waste liquid recover connects, return in liquid backwash filter and on-the-spot connecting pipe of returning liquid import and have check valve, return in the connecting pipe of liquid backwash filter and waste liquid recover and have differential pressure check valve, the liquid outlet of waste liquid recover is connected with emulsion box, return liquid backwash filter liquid outlet by pipeline respectively with high-pressure emulsion import, emulsion box connects, return in the connecting pipe of liquid backwash filter and high-pressure emulsion import magnetic valve A is set, return in the connecting pipe of liquid backwash filter and emulsion box magnetic valve B is set.
Waste liquid recover described in the utility model, is characterized in that waste liquid recover inside arranges recover filter core, and waste liquid recover and recover filter core are detachable, convenient cleaning and replacing recover filter core.
Described in the utility model time liquid backwash filter, is characterized in that back that liquid backwash filter inside arranges filter element, and returning liquid backwash filter and filter element is monolithic construction.
Filter process: magnetic valve A closes, magnetic valve B opens, the scene that needs to filter is returned liquid and is returned liquid import by scene and enter back liquid backwash filter and filter through check valve, and the contaminant filter that scene is returned in liquid falls, then enters emulsion box through the magnetic valve B of unlatching.
Backwash process: magnetic valve A opens, magnetic valve B closes, high-pressure emulsion enters back liquid backwash filter through magnetic valve A, carry out backwash to returning liquid backwash filter, because emulsion is with high pressure, so pressure reduction check valve both sides produce pressure differential, in the time that pressure differential reaches 0.3KPA, the conducting of differential pressure check valve, emulsion enters waste liquid recover, then enters emulsion box.
The beneficial effects of the utility model are that the on-the-spot liquid filtration automatic back-flushing device that returns of emulsification is provided with back liquid backwash filter, can realize automatic back-flushing function, in the course of work, can realize Hand scarf filter core and renew cartridge more, meet the continuous production requirement in colliery.
brief description of the drawings:
Accompanying drawing 1 is structural representation of the present utility model, in accompanying drawing 1:
1. high-pressure emulsion import, 2. waste liquid recover, 3. recover filter core, 4. emulsion box, 5. magnetic valve A, 6. magnetic valve B, 7. on-the-spot liquid import, 8. check valve, 9. time liquid backwash filter, 10. filter element, 11. differential pressure check valves of returning.
detailed description of the invention:
1 pair of the utility model describes in further detail by reference to the accompanying drawings, so that the public grasps implementation method of the present utility model better, the utility model specific embodiment is: the on-the-spot liquid that returns of described emulsification filters automatic back-flushing device by high-pressure emulsion import 1, waste liquid recover 2, recover filter core 3, emulsion box 4, magnetic valve A5, magnetic valve B6, on-the-spot time liquid import 7, check valve 8, return liquid backwash filter 9, filter element 10, differential pressure check valve 11 forms, the inlet that it is characterized in that back liquid backwash filter 9 uses pipeline to return liquid import 7 with scene respectively, the inlet of waste liquid recover 2 connects, return in liquid backwash filter 9 and on-the-spot connecting pipe of returning liquid import 7 and have check valve 8, return in the connecting pipe of liquid backwash filter 9 and waste liquid recover 2 and have differential pressure check valve 11, differential pressure check valve 11 is selected 0.3KPa, the liquid outlet of waste liquid recover 2 is connected with emulsion box 4, return liquid backwash filter 9 liquid outlet by pipeline respectively with high-pressure emulsion import 1, emulsion box 4 connects, return in the connecting pipe of liquid backwash filter 9 and high-pressure emulsion import 1 magnetic valve A5 is set, return in the connecting pipe of liquid backwash filter 9 and emulsion box 4 magnetic valve B6 is set.
Waste liquid recover 2 described in the utility model, is characterized in that waste liquid recover 2 inside arrange recover filter core 3, and waste liquid recover 2 is detachable with recover filter core 3, convenient cleaning and replacing recover filter core 3.
Described in the utility model time liquid backwash filter 9, is characterized in that back that liquid backwash filter 9 inside arrange filter element 10, and returning liquid backwash filter 9 is monolithic construction with filter element 10.
Filter process: magnetic valve A5 closes, magnetic valve B6 opens, the scene that needs to filter is returned liquid and is returned liquid import 7 by scene and enter back liquid backwash filter 9 through check valves 8 and filter, and the contaminant filter that scene is returned in liquid falls, then enters emulsion box 4 through the magnetic valve B6 of unlatching.
Backwash process: magnetic valve A5 opens, magnetic valve B6 closes, high-pressure emulsion enters back liquid backwash filter 9 through magnetic valve A5, carry out backwash to returning liquid backwash filter 9, because emulsion is with high pressure, so pressure reduction check valve 11 both sides produce pressure differential, in the time that pressure differential reaches 0.3KPA, 11 conductings of differential pressure check valve, emulsion enters waste liquid recover 2, then enters emulsion box 4.
The beneficial effects of the utility model are that the on-the-spot liquid filtration automatic back-flushing device that returns of emulsification is provided with back liquid backwash filter, can realize automatic back-flushing function, in the course of work, can realize Hand scarf filter core and renew cartridge more, meet the continuous production requirement in colliery.
Claims (3)
1. the on-the-spot liquid that returns of emulsification filters automatic back-flushing device, by high-pressure emulsion import (1), waste liquid recover (2), recover filter core (3), emulsion box (4), magnetic valve A (5), magnetic valve B (6), on-the-spot time liquid import (7), check valve (8), return liquid backwash filter (9), filter element (10), differential pressure check valve (11) composition, the inlet that it is characterized in that back liquid backwash filter (9) uses pipeline to return liquid import (7) with scene respectively, the inlet of waste liquid recover (2) connects, return in liquid backwash filter (9) and on-the-spot connecting pipe of returning liquid import (7) and have check valve (8), return in the connecting pipe of liquid backwash filter (9) and waste liquid recover (2) and have differential pressure check valve (11), the liquid outlet of waste liquid recover (2) is connected with emulsion box (4), return liquid backwash filter (9) liquid outlet by pipeline respectively with high-pressure emulsion import (1), emulsion box (4) connects, return in the connecting pipe of liquid backwash filter (9) and high-pressure emulsion import (1) magnetic valve A (5) is set, return in the connecting pipe of liquid backwash filter (9) and emulsion box (4) magnetic valve B (6) is set.
2. the on-the-spot liquid that returns of emulsification according to claim 1 filters automatic back-flushing device, it is characterized in that waste liquid recover (2) inside arranges recover filter core (3).
3. the on-the-spot liquid that returns of emulsification according to claim 1 filters automatic back-flushing device, it is characterized in that back that liquid backwash filter (9) inside arranges filter element (10), returning liquid backwash filter (9) is monolithic construction with filter element (10).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420276830.2U CN203861998U (en) | 2014-05-28 | 2014-05-28 | Device for filtering and automatic backwash of returned liquid on emulsification site |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201420276830.2U CN203861998U (en) | 2014-05-28 | 2014-05-28 | Device for filtering and automatic backwash of returned liquid on emulsification site |
Publications (1)
Publication Number | Publication Date |
---|---|
CN203861998U true CN203861998U (en) | 2014-10-08 |
Family
ID=51642989
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201420276830.2U Expired - Fee Related CN203861998U (en) | 2014-05-28 | 2014-05-28 | Device for filtering and automatic backwash of returned liquid on emulsification site |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN203861998U (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106110730A (en) * | 2016-08-24 | 2016-11-16 | 苏州依斯倍环保装备科技有限公司 | Emulsion reuse integrating device |
CN109026671A (en) * | 2018-09-17 | 2018-12-18 | 辽宁格瑞特泵业有限公司 | Automatic desilting filter |
CN109611416A (en) * | 2018-12-27 | 2019-04-12 | 浙江中煤机械科技有限公司 | A kind of unloading shock-damping structure and hydraulic system |
-
2014
- 2014-05-28 CN CN201420276830.2U patent/CN203861998U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106110730A (en) * | 2016-08-24 | 2016-11-16 | 苏州依斯倍环保装备科技有限公司 | Emulsion reuse integrating device |
CN109026671A (en) * | 2018-09-17 | 2018-12-18 | 辽宁格瑞特泵业有限公司 | Automatic desilting filter |
CN109611416A (en) * | 2018-12-27 | 2019-04-12 | 浙江中煤机械科技有限公司 | A kind of unloading shock-damping structure and hydraulic system |
CN109611416B (en) * | 2018-12-27 | 2024-01-16 | 浙江中煤机械科技有限公司 | Unloading damping structure and hydraulic system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN203861998U (en) | Device for filtering and automatic backwash of returned liquid on emulsification site | |
CN202762217U (en) | Cutting fluid purifier | |
CN102989711B (en) | Impurity collecting device for oil sprayer | |
CN202228450U (en) | Hydraulic oil tank | |
CN209317164U (en) | Novel online lubricating oil filtering equipment | |
CN208574312U (en) | A kind of production platform water supply well desanding device | |
CN203342527U (en) | Cooling liquid filtering device | |
CN204543791U (en) | A kind of air filtering system for electroplating | |
CN203868042U (en) | High pressure filtering and automatic backwashing device for emulsion | |
CN204234204U (en) | A kind of petroleum transportation filter | |
CN204711692U (en) | A kind of cutting fluid recycling device | |
CN203972129U (en) | A kind of filter | |
CN203257799U (en) | Oil filtering-reusing system for test bed | |
CN204411853U (en) | A kind of heating and filtering water tank of cleaning device | |
CN202946487U (en) | Inlet filter device for oil pump and oil tank | |
CN206342976U (en) | A kind of fixed profit coarse separation oil filter system | |
CN204314134U (en) | A kind of superposing type filtrator for electric furnace creep testing machine | |
CN205145784U (en) | Portable cutting fluid deoiling regenerating unit | |
CN103239932A (en) | Oil-saving oil filter | |
CN203525429U (en) | Movable type dirty oil recycling device | |
CN203389423U (en) | Integrated water treatment device | |
CN102581769B (en) | Cooling oil recycle, energy-saving and emission-reducing device | |
CN203431505U (en) | Automatic desanding device of oil and gas gathering and transportation system | |
CN201502588U (en) | Valve block integrated high-pressure bypass filtering device | |
CN203383863U (en) | AST filter screen system of steam turbine |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141008 Termination date: 20160528 |