CN204841419U - Conduction oil clarifier - Google Patents
Conduction oil clarifier Download PDFInfo
- Publication number
- CN204841419U CN204841419U CN201520587301.9U CN201520587301U CN204841419U CN 204841419 U CN204841419 U CN 204841419U CN 201520587301 U CN201520587301 U CN 201520587301U CN 204841419 U CN204841419 U CN 204841419U
- Authority
- CN
- China
- Prior art keywords
- housing
- conduction oil
- filter core
- ceramic membrane
- membrane 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.)
- Active
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides a conduction oil clarifier, which comprises a housin, be equipped with feed inlet and discharge gate on the casing, the discharge gate is located the casing top, the inside orifice plate that is equipped with of casing, orifice plate lower extreme rigid coupling and intercommunication have the ceramic membrane filter core of a plurality of vertical settings, conduction oil warp the ceramic membrane filter core filters the back and flows from the discharge gate, casing upper portion is equipped with the blowback device, the back blow port on the casing is connected to the blowback device, the back blow port is located discharge gate department, it is equipped with row cinder notch to be located the casing lower extreme for the discharge of sediment matter, feed inlet, discharge gate and row's cinder notch department all are equipped with the valve. The utility model discloses an it can filter at the wire pair conduction oil to set up the ceramic membrane filter core, and the filter effect is high, sets up the blowback device on the casing, can wash away it when the ceramic membrane filter core covers sediment matter for ceramic membrane filter core life obtains improving, has reduced use cost.
Description
Technical field
The utility model relates to a kind of cleaning equipment, particularly relates to a kind of conduction oil clarifier.
Background technology
Conduction oil in use, along with the lengthening of service time, carbonization can be there is gradually, become viscosity to increase, even form coking body, generate carbon deposit at pipeline and heat exchanger inwall, reduce pipeline transmission capacity, affect heat exchange effect, therefore regularly must comprise heating equipment to heat-conducting oil furnace and pipeline and clean.And cleaning is divided into two kinds of modes: decompose cleaning and on-line cleaning.The dismounting of the equipment such as pipeline, heating equipment decomposed when decomposing cleaning, clean separately by physics or chemical method, this method is time-consuming, and cost is higher; On-line cleaning is that the conduction oil in system is given off a part, injects a certain proportion of cleaning agent, cleaning agent and conduction oil used in combination, in running, the slag such as carbon residue of assembling is removed cleaning.Existing on-line cleaning equipment also exists structure imperfection, such as existing equipment mostly realizes filtering by filter screen, but by filter screen, filter effect is bad on the one hand, on the other hand along with the growth of service time, filter screen can cover one deck slag, cause the filter effect reducing filter screen.
Summary of the invention
Problem to be solved in the utility model is to provide a kind of conduction oil clarifier, can run, carry out heat conduction oil filtration by ceramic membrane filter core under the operating mode of HTHP, then is blown down by the slag that it covers by back-blowing device, improves filter effect.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is: a kind of conduction oil clarifier, comprise housing, described housing is provided with charging aperture and discharging opening, described discharging opening is positioned at case top, described enclosure interior is provided with orifice plate, and described orifice plate lower end is affixed and be communicated with the ceramic membrane filter core of some vertical settings, and conduction oil flows out from discharging opening after described ceramic membrane filter core is filtered; Housing upper is provided with back-blowing device, and described back-blowing device is connected to the back blow port on housing, and described back blow port is positioned at discharge outlet; Be positioned at housing lower end and be provided with slag-drip opening, for the discharge of slag; Described charging aperture, discharging opening and slag-drip opening place are equipped with valve.
As preferably, described back-blowing device comprises gas bag and nitrogen gas generator, described gas bag is connected to back blow port by tracheae, described nitrogen gas generator is filled with high pressure nitrogen in gas bag, described gas bag is blown into described high pressure nitrogen by tracheae and back blow port in housing, and described high pressure nitrogen enters in described ceramic membrane filter core and washes away ceramic membrane filter core.
As preferably, described back-blowing device comprises high-pressure pump and is connected to the pipeline of back blow port, and described high-pressure pump pumps into conduction oil by described pipeline and back blow port in housing, and described conduction oil enters in ceramic membrane filter core and washes away ceramic membrane filter core.
As preferably, the screeding device be positioned at above orifice plate is provided with in described housing, described screeding device comprises the casing be sealedly attached in inner walls, cylinder is provided with in described casing, the output of cylinder is connected with scraper plate through described orifice plate, what described scraper plate was provided with sheathed ceramic membrane filter core scrapes hole, described in scrape the aperture in hole identical with the external diameter of ceramic membrane filter core.
As preferably, side, described housing lower end is provided with residual liquid discharge mouth, and described residual liquid discharge mouth place is connected with valve.
As preferably, described housing is provided with the gauge port of Bonding pressure table and connects the thermometer mouth of thermometer.
As preferably, described housing lower end is connected with support, and described support circumference is fixed in housing lower end, for supporting described housing.
The advantage that the utility model has and good effect are: can filter conduction oil online by arranging ceramic membrane filter core, and filter effect is high, housing arranges back-blowing device, can when ceramic membrane filter core covers slag, it is washed away, ceramic membrane filter core is improved service life, reduces use cost.
Accompanying drawing explanation
Fig. 1 is overall structure schematic diagram of the present utility model
Fig. 2 is the I place enlarged drawing of the utility model Fig. 1
In figure:
1, housing; 2, charging aperture; 3, discharging opening; 4, ceramic membrane filter core; 5, orifice plate; 6, slag-drip opening; 7, valve; 8, gas bag; 9, nitrogen gas generator; 10, back blow port; 11, casing; 12, cylinder; 13, scraper plate; 14, residual liquid discharge mouth; 15, gauge port; 16, thermometer mouth; 17, support.
Detailed description of the invention
Below in conjunction with accompanying drawing, specific embodiment of the utility model is illustrated:
Embodiment 1:
As shown in Figure 1, the utility model provides a kind of conduction oil clarifier, for carrying out in-line purification to conduction oil, can not change conduction oil, without the need to stopping purifying conduction oil of production.Concrete, this conduction oil clarifier comprises housing 1, and housing 1 is provided with charging aperture 2 and discharging opening 3, and wherein charging aperture 2 is positioned at the middle part of housing 1, for the inflow from the conduction oil in conduction oil Trunk Line; Discharging opening 3 is positioned at case top, for the outflow of the conduction oil after filtering;
Orifice plate 5 is provided with in the inside of housing 1, affixed and be communicated with the ceramic membrane filter core 4 of some vertical settings in orifice plate 5 lower end, conduction oil flows out from discharging opening 3 after ceramic membrane filter core 4 is filtered, concrete, conduction oil flows into from charging aperture 2, contacts afterwards with ceramic membrane filter core 4, and filters the slags such as carbon residue by ceramic membrane filter core 4, filtered conduction oil flows into housing 1 top through orifice plate 5 in ceramic membrane filter core 4, and flows out from discharging opening 3.In the present embodiment, the number of ceramic membrane filter core 4 can be arranged as required, specifically can be set to 10-90.
Along with the growth of the time used, one deck slag can be covered on the outer wall of ceramic membrane filter core 4, time has been grown and the decline of ceramic membrane filter core 4 filter effect can be caused even cannot to filter, therefore back-blowing device is set on housing 1 top, back-blowing device is connected to the back blow port 10 on housing 1, for washing away ceramic membrane filter core 4 outer wall, concrete back-blowing device carries conduction oil or high pressure nitrogen in ceramic membrane filter core 4, and by conduction oil or high pressure nitrogen, the slag to outer wall washes away.
Slag-drip opening 6 is provided with, for the discharge of slag in the lower end of housing 1; In the present embodiment, be equipped with valve 7 at charging aperture 2, discharging opening 3 and slag-drip opening 6 place, this valve 7 can be electrically operated valve, for the Ka Guan to each mouthful.
In the present embodiment, back-blowing device comprises gas 8 and nitrogen gas generator 9, wherein gas bag 8 is connected to back blow port 10 by tracheae, concrete scour process is: nitrogen gas generator 9 is filled with high pressure nitrogen in gas bag 8, gas bag 8 is blown into high pressure nitrogen by tracheae and back blow port 10 in housing 1, high pressure nitrogen enters in ceramic membrane filter core 4, washing away the outer wall of ceramic membrane filter core 4 from inside to outside, to wash away the slag on outer wall.
In order to better realize the removal of the slag to ceramic membrane filter core 4 outer wall, as shown in Figure 2, the screeding device be positioned at above orifice plate 5 is provided with in housing 1, this screeding device comprises the casing 11 be sealedly attached on housing 1 inwall, cylinder 12 is provided with in casing 11, the output of cylinder 12 is connected with scraper plate 13 through orifice plate 5, drives the outer wall of scraper plate 13 pairs of ceramic membrane filter core 4 to strike off work by cylinder 12.What scraper plate 13 was provided with sheathed ceramic membrane filter core 4 scrapes hole, and the aperture of scraping hole is identical with the external diameter of ceramic membrane filter core 4.And when not carrying out striking off work, cylinder 12 is in contraction state, and scraper plate 13 is close to the below of orifice plate 5, when slag is too much, cylinder 12 stretches out and drives scraper plate 13 to move down, and washes away rear residual slag strike off by scraper plate 13 pairs of back-blowing devices.
Also be provided with residual liquid discharge mouth 14 in the side, lower end of housing 1, between deslagging to the discharge of the conduction oil of remnants, described residual liquid discharge mouth 14 place is connected with valve 7.
Housing 1 be provided with the gauge port 15 of Bonding pressure table and connect the thermometer mouth 16 of thermometer, respectively the pressure and temperature in housing 1 being monitored by Pressure gauge and thermometer.
Be connected with support 17 in the lower end of housing 1, its circumference is fixed in the lower end of housing 1, for supporting above-mentioned housing 1.
Embodiment 2:
The present embodiment and the difference of embodiment 1 are that the structure of back-blowing device is different, and all the other structures are all identical with embodiment 1, do not repeat them here, only set forth back-blowing device:
The back-blowing device of the present embodiment comprises high-pressure pump and is connected to the pipeline of back blow port 10, high-pressure pump pumps into conduction oil by pipeline and back blow port 10 in housing 1, conduction oil enters in ceramic membrane filter core 4, the outer wall of ceramic membrane filter core 4 is washed away from inside to outside, and then the slag on outer wall is washed away.
Above embodiment of the present utility model has been described in detail, but described content being only preferred embodiment of the present utility model, can not being considered to for limiting practical range of the present utility model.All equalizations done according to the utility model scope change and improve, and all should still belong within this patent covering scope.
Claims (7)
1. a conduction oil clarifier, it is characterized in that: comprise housing (1), described housing (1) is provided with charging aperture (2) and discharging opening (3), described discharging opening (3) is positioned at housing (1) top, described housing (1) inside is provided with orifice plate (5), described orifice plate (5) lower end is affixed and be communicated with the ceramic membrane filter core (4) of some vertical settings, and conduction oil flows out from discharging opening (3) after described ceramic membrane filter core (4) is filtered; Housing (1) top is provided with back-blowing device, and described back-blowing device is connected to the back blow port (10) on housing (1), and described back blow port (10) is positioned at discharging opening (3) place; Be positioned at housing (1) lower end and be provided with slag-drip opening (6), for the discharge of slag; Described charging aperture (2), discharging opening (3) and slag-drip opening (6) place are equipped with valve (7).
2. conduction oil clarifier according to claim 1, it is characterized in that: described back-blowing device comprises gas bag (8) and nitrogen gas generator (9), described gas bag (8) is connected to back blow port (10) by tracheae, described back blow port (10) is positioned at discharging opening (3) place, described nitrogen gas generator (9) is filled with high pressure nitrogen in gas bag (8), described gas bag (8) is blown into described high pressure nitrogen by tracheae and back blow port (10) in housing (1), described high pressure nitrogen enters in described ceramic membrane filter core (4) and washes away ceramic membrane filter core (4).
3. conduction oil clarifier according to claim 1, it is characterized in that: described back-blowing device comprises high-pressure pump and is connected to the pipeline of back blow port (10), described high-pressure pump pumps into conduction oil by described pipeline and back blow port (10) in housing (1), and described conduction oil enters in ceramic membrane filter core (4) and washes away ceramic membrane filter core (4).
4. the conduction oil clarifier according to Claims 2 or 3, it is characterized in that: in described housing (1), be provided with the screeding device being positioned at orifice plate (5) top, described screeding device comprises the casing (11) be sealedly attached on housing (1) inwall, cylinder (12) is provided with in described casing (11), the output of cylinder (12) is connected with scraper plate (13) through described orifice plate (5), what described scraper plate (13) was provided with sheathed ceramic membrane filter core (4) scrapes hole, described aperture of scraping hole is identical with the external diameter of ceramic membrane filter core (4).
5. conduction oil clarifier according to claim 4, is characterized in that: described housing (1) side, lower end is provided with residual liquid discharge mouth (14), and described residual liquid discharge mouth (14) place is connected with valve (7).
6. conduction oil clarifier according to claim 1, is characterized in that: described housing (1) is provided with the gauge port (15) of Bonding pressure table and connects the thermometer mouth (16) of thermometer.
7. conduction oil clarifier according to claim 1, it is characterized in that: described housing (1) lower end is connected with support (17), described support (17) circumference is fixed in housing (1) lower end, for supporting described housing (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520587301.9U CN204841419U (en) | 2015-08-06 | 2015-08-06 | Conduction oil clarifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520587301.9U CN204841419U (en) | 2015-08-06 | 2015-08-06 | Conduction oil clarifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204841419U true CN204841419U (en) | 2015-12-09 |
Family
ID=54732017
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520587301.9U Active CN204841419U (en) | 2015-08-06 | 2015-08-06 | Conduction oil clarifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204841419U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105478010A (en) * | 2015-12-28 | 2016-04-13 | 青岛科技大学 | Micropore filtering device for coking wastewater treatment and filtering and cleaning method of micropore filtering device |
| CN105645616A (en) * | 2015-12-28 | 2016-06-08 | 青岛科技大学 | Coking wastewater combined treatment system and method thereof |
| CN111672198A (en) * | 2020-05-28 | 2020-09-18 | 金川集团股份有限公司 | High-efficient heavy oil filter |
| CN113088324A (en) * | 2021-04-14 | 2021-07-09 | 山东英可利新材料技术有限公司 | Method for extracting carbon nano material from waste lubricating oil, heavy oil or asphalt |
| CN113144907A (en) * | 2021-01-22 | 2021-07-23 | 赣州佳广智能装备科技有限公司 | Electrodialysis purification method for biological pharmacy |
-
2015
- 2015-08-06 CN CN201520587301.9U patent/CN204841419U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105478010A (en) * | 2015-12-28 | 2016-04-13 | 青岛科技大学 | Micropore filtering device for coking wastewater treatment and filtering and cleaning method of micropore filtering device |
| CN105645616A (en) * | 2015-12-28 | 2016-06-08 | 青岛科技大学 | Coking wastewater combined treatment system and method thereof |
| CN105645616B (en) * | 2015-12-28 | 2019-02-26 | 青岛科技大学 | A kind of coking wastewater joint processing system and method |
| CN111672198A (en) * | 2020-05-28 | 2020-09-18 | 金川集团股份有限公司 | High-efficient heavy oil filter |
| CN113144907A (en) * | 2021-01-22 | 2021-07-23 | 赣州佳广智能装备科技有限公司 | Electrodialysis purification method for biological pharmacy |
| CN113088324A (en) * | 2021-04-14 | 2021-07-09 | 山东英可利新材料技术有限公司 | Method for extracting carbon nano material from waste lubricating oil, heavy oil or asphalt |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204841419U (en) | Conduction oil clarifier | |
| CN111135718A (en) | Sewage filtering device and filtering method | |
| CN202778063U (en) | Backwashing basket type filter | |
| CN104436774B (en) | Mechanical filter | |
| CN107019949A (en) | Rotary drum fine fack formula solid-liquid separating equipment | |
| CN216259530U (en) | Raw water filtering device with backwashing function | |
| CN202315489U (en) | Backwashing precision water filter | |
| CN105126429A (en) | Residual oil back-wash filtering system and residual oil back-wash filtering method | |
| CN201267734Y (en) | H type high-efficient filtering equipment | |
| CN210584038U (en) | Metallurgical turbid water spiral-flow type filter | |
| CN210448352U (en) | Coking circulation ammonia water processing system | |
| CN103446792A (en) | Filtering device | |
| CN110201447A (en) | A kind of cyclic ammonia water filter device and its automatic backflushing washing method | |
| CN207641293U (en) | Lithium carbonate filter | |
| CN201030254Y (en) | Highly effective screen filter | |
| CN2753438Y (en) | Backflush visual filter | |
| CN207641305U (en) | Lithium carbonate filter device | |
| CN201744207U (en) | Integrated filter | |
| CN220976620U (en) | Air-flushing cleaning type domestic sewage purifier | |
| CN216825077U (en) | Alkali liquor purification and recovery device based on cluster filtration method | |
| CN210521955U (en) | Self-cleaning filter | |
| CN103721458A (en) | Manufacture method of recoil water filtering device used during calcium alginate production | |
| CN204319851U (en) | Mechanical filter | |
| CN214232994U (en) | Back flush filter | |
| CN219355433U (en) | Self-cleaning filter device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 255400 Xinhua Road, Linzi District, Zibo, Shandong Province, No. 161 Patentee after: Shandong English New Material Technology Co., Ltd. Address before: 250000 Xinhua Road, Linzi District, Zibo, Shandong Province, No. 161 Patentee before: Shandong Enkli Chemical Co., Ltd. |