CN210964547U - Water vapor filtering separator for chemical production - Google Patents
Water vapor filtering separator for chemical production Download PDFInfo
- Publication number
- CN210964547U CN210964547U CN201921779529.2U CN201921779529U CN210964547U CN 210964547 U CN210964547 U CN 210964547U CN 201921779529 U CN201921779529 U CN 201921779529U CN 210964547 U CN210964547 U CN 210964547U
- Authority
- CN
- China
- Prior art keywords
- separator
- liquid
- main body
- separator main
- guide plate
- 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
Images
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model relates to the technical field of chemical production equipment, in particular to a steam filtering separator for chemical production, which comprises a separator main body, an upper cover and a support frame, wherein the upper end of the separator main body is connected with the upper cover, one side of the upper part of the separator main body, which is close to the upper cover, is provided with a steam inlet, one side of the upper part of the separator main body, which is far away from the steam inlet, is provided with a gas outlet, the lower end of the separator main body is provided with the support frame, the middle part of the lower end of the separator main body is provided with a liquid outlet, the lower end of the liquid outlet is provided with an opening valve, the lower end of the opening valve is connected with a telescopic pipe, the lower end of the telescopic pipe is provided with a liquid collecting barrel, the lower end of the liquid collecting barrel is provided with a movable, the whole effect is good, and stability and practicality are higher, have certain spreading value.
Description
Technical Field
The utility model relates to a chemical production equipment technical field specifically is a steam filtering separator for chemical production.
Background
The gas-water separator is mainly used for separating gas from liquid in an industrial liquid-containing system, improves the drying degree of steam, and reduces the phenomenon that the steam carries water.
The steam filtering separator has long service life, is inconvenient to clean and replace, has poor filtering effect, and needs to be improved by the steam filtering separator for chemical production.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a steam filtering separator for chemical production to solve the problem that proposes among the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme:
a steam filtering separator for chemical production comprises a separator main body, an upper cover and a support frame, wherein the upper cover is connected to the upper end of the separator main body, a steam inlet is formed in one side of the upper portion of the separator main body, which is close to the upper cover, a gas outlet is formed in one side of the upper portion of the separator main body, which is far away from the steam inlet, a support frame is arranged at the lower end of the separator main body, a liquid outlet is formed in the middle of the lower end of the separator main body, an opening valve is arranged at the lower end of the liquid outlet, a telescopic pipe is connected to the lower end of the opening valve, a liquid collecting barrel is arranged at the lower end of the telescopic pipe, a moving trolley is arranged at the lower end of the liquid collecting barrel, liquid guide pipes are arranged in the separator main body, which are close to, the cyclone reversing pipe is internally provided with a liquid guide groove, the liquid guide groove is internally provided with a pre-filtering assembly and a precise filtering assembly, and the lower part of the inside of the separator main body is provided with a liquid separation plate.
Preferably, the pre-filter assembly employs a coalescing filter element.
Preferably, the precise filtering component adopts a gas-liquid separation filter element.
Preferably, the edge of the filter plate is provided with a clamping strip, and the filter plate and the guide plate are clamped through the clamping strip.
Preferably, the separator main body and the liquid guide pipe are provided with support plates at positions close to the guide plate, and the guide plate, the separator main body and the liquid guide pipe are clamped through the support plates.
Preferably, the rotational flow reversing pipe and the guide plate are of an integrated structure, and helical blades are arranged outside the rotational flow reversing pipe.
Compared with the prior art, the beneficial effects of the utility model are that:
1. the utility model discloses in, guide plate through setting up, whirl switching-over pipe, liquid guide groove and filter, the filter flange edge is equipped with the card strip, and filter and guide plate pass through card strip joint, separator main part inside and catheter are close to guide plate department and are equipped with the layer board, and guide plate and separator main part, through the layer board joint between the catheter, whirl switching-over pipe and guide plate structure as an organic whole, form detachable structure, conveniently take out guide plate and whirl switching-over pipe from inside upwards of separator main part, conveniently wash the liquid guide groove, the filter, conveniently change the accurate filtering component and filter assembly in advance.
2. The utility model discloses in, precision filter subassembly and prefiltration subassembly through the setting, prefiltration subassembly adopts the coalescence filter core, the liquid drop of liquid is caught by the inside superfine fiber of coalescence filter core, micron order fibre has formed tortuous passageway to the air current, force the liquid droplet at inertial collision, diffusion interception and direct interception three kinds of filter mechanism's effect under, catch by superfine fiber, liquid surface tension makes the droplet coalesce into bigger liquid drop, because the action of gravity, big liquid drop subsides to coalescence filter core bottom, then flow into the inside bottom of separator main part via the cistern, precision filter subassembly adopts the gas-liquid separation filter core, filter paper with multilayer composite structure, the filter fineness is high, the pollutant carrying capacity is big, long service life, flow density is big, the microfilter size has been reduced.
3. The utility model discloses in, through the whirl switching-over pipe that sets up, whirl switching-over outside of managing is equipped with helical blade, forms the liquid level of congealing by a large scale, and when steam through helical blade, convenient liquid condenses, and the filter effect is good.
Drawings
FIG. 1 is an overall structure diagram of the present invention;
FIG. 2 is an internal structure view of the present invention;
fig. 3 is a structure diagram of the filter plate of the present invention.
In the figure: 1-a separator main body, 2-a water vapor inlet, 3-an upper cover, 4-a gas outlet, 5-an opening valve, 6-a telescopic pipe, 7-a support frame, 8-a moving trolley, 9-a liquid collecting barrel, 10-a precise filtering component, 11-a pre-filtering component, 12-a liquid separating plate, 13-a liquid outlet, 14-a guide plate, 15-a rotational flow reversing pipe, 16-a liquid guide pipe, 17-a liquid guide groove and 18-a filter plate.
Detailed Description
The technical solution in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, rather than all embodiments, and all other embodiments obtained by a person of ordinary skill in the art without creative work belong to the protection scope of the present invention based on the embodiments of the present invention.
Referring to fig. 1-3, the present invention provides a technical solution:
a steam filtering separator for chemical production comprises a separator main body 1, an upper cover 3 and a support frame 7, wherein the upper end of the separator main body 1 is connected with the upper cover 3, one side of the upper part of the separator main body 1, which is close to the upper cover 3, is provided with a steam inlet 2, one side of the upper part of the separator main body 1, which is far away from the steam inlet 2, is provided with a gas outlet 4, the lower end of the separator main body 1 is provided with the support frame 7, the middle of the lower end of the separator main body 1 is provided with a liquid outlet 13, the lower end of the liquid outlet 13 is provided with an opening valve 5, the lower end of the opening valve 5 is connected with a telescopic pipe 6, the lower end of the telescopic pipe 6 is provided with a liquid collecting barrel 9, the lower end of the liquid collecting barrel 9 is provided with a movable trolley 8, the positions, which are close to the steam inlet 2, and the filter plate 18 and the guide plate 14 are clamped through clamping strips, the support plates are arranged inside the separator main body 1 and at the positions, close to the guide plate 14, of the liquid guide tube 16, the guide plate 14 and the separator main body 1 are clamped through the support plates, the lower end of the guide plate 14 is connected with the cyclone reversing tube 15, the cyclone reversing tube 15 and the guide plate 14 are of an integral structure, the spiral blade is arranged outside the cyclone reversing tube 15, the liquid guide groove 17 is formed inside the cyclone reversing tube 15, the pre-filtering assembly 11 and the precise filtering assembly 10 are arranged inside the liquid guide groove 17, the pre-filtering assembly 11 adopts a coalescing filter element, the precise filtering assembly 10 adopts a gas-liquid separation filter element, and the liquid separating plate 12 is arranged at.
The utility model discloses work flow: firstly, water vapor enters the separator main body 1 through the water vapor inlet 2, then passes through the cyclone reversing pipe 15 and passes through the arranged cyclone reversing pipe 15, the spiral blade is arranged outside the cyclone reversing pipe 15 to form a large-area condensate surface, when the water vapor passes through the spiral blade, the liquid is convenient to condense, then the water vapor enters the pre-filtering component 11 through the bottom of the cyclone reversing pipe 15, the pre-filtering component 11 passes through the arranged precise filtering component 10 and the pre-filtering component 11, the pre-filtering component 11 adopts a coalescing filter element, liquid drops are captured by superfine fibers in the coalescing filter element, the micron-sized fibers form a zigzag channel for air flow, the liquid fog drops are forced to be captured by the superfine fibers under the actions of three filtering mechanisms of inertial collision, diffusion interception and direct interception, liquid surface tension enables the small drops to be coalesced into larger-sized drops, and the large-sized drops, then flows into the bottom inside the separator body 1 through the liquid guide groove 17, the precise filtering component 20 adopts a gas-liquid separation filter element, a plurality of layers of filter paper with a composite structure are used, the filtering precision is high, the pollutant carrying capacity is large, the service life is long, the flow density is large, the size of the precise filter is reduced, the liquid on the guide plate 14, the rotational flow reversing pipe 15, the liquid guide pipe 16 and the liquid guide groove 17 is gathered at the lower part inside the separator body 1, then the opening valve 5 is opened, the liquid flows to the extension pipe 6 through the liquid outlet 13 and then enters the liquid collecting barrel 9, when the liquid collecting barrel 9 is full, the full liquid collecting barrel 9 can be pushed away through the movable trolley, so that the liquid collecting barrel 9 is more convenient to carry, the gas is filtered through the pre-filtering component 11 and the precise filtering component 10, then passes through the filter plate 18, enters the gas outlet 4 and, Cyclone reversing tube 15, liquid guide groove 17 and filter 18, 18 edges of filter are equipped with the card strip, and filter 18 and guide plate 14 are through calorie strip joint, 1 inside and liquid guide pipe 16 of separator main part are close to guide plate 25 and are equipped with the layer board, and guide plate 14 and separator main part 1, through the layer board joint between the liquid guide pipe 16, cyclone reversing tube 15 and guide plate 14 structure as an organic whole, form detachable structure, conveniently take out guide plate 14 and cyclone reversing tube 15 from 1 inside upwards of separator main part, conveniently wash liquid guide groove 17, filter 18, conveniently change precision filtration subassembly 10 and prefiltration subassembly 11, whole effectual, and stability and practicality are higher, certain spreading value has.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. The utility model provides a steam filtering separator for chemical production, includes separator main part (1), upper cover (3) and support frame (7), its characterized in that: the separator is characterized in that an upper cover (3) is connected to the upper end of a separator main body (1), a steam inlet (2) is formed in one side of the upper portion of the separator main body (1) close to the upper cover (3), a gas outlet (4) is formed in one side of the upper portion of the separator main body (1) far away from the steam inlet (2), a support frame (7) is arranged at the lower end of the separator main body (1), a liquid outlet (13) is formed in the middle of the lower end of the separator main body (1), an opening valve (5) is arranged at the lower end of the liquid outlet (13), a telescopic pipe (6) is connected to the lower end of the opening valve (5), a liquid collecting barrel (9) is arranged at the lower end of the telescopic pipe (6), a moving trolley (8) is arranged at the lower end of the liquid collecting barrel (9), and liquid guide pipes (16), the separator is characterized in that a guide plate (14) is arranged at the upper end inside the separator body (1), a filter plate (18) is arranged in the middle of the guide plate (14), a cyclone reversing pipe (15) is connected to the lower end of the guide plate (14), a liquid guide groove (17) is arranged inside the cyclone reversing pipe (15), a pre-filtering assembly (11) and a precise filtering assembly (10) are arranged inside the liquid guide groove (17), and a liquid separating plate (12) is arranged at the lower part inside the separator body (1).
2. The water vapor filtering separator for chemical industry production according to claim 1, wherein: the pre-filtering component (11) adopts a coalescence filter element.
3. The water vapor filtering separator for chemical industry production according to claim 1, wherein: the precise filtering component (10) adopts a gas-liquid separation filter element.
4. The water vapor filtering separator for chemical industry production according to claim 1, wherein: the edge of the filter plate (18) is provided with a clamping strip, and the filter plate (18) and the guide plate (14) are clamped through the clamping strip.
5. The water vapor filtering separator for chemical industry production according to claim 1, wherein: supporting plates are arranged inside the separator main body (1) and at the position, close to the guide plate (14), of the liquid guide pipe (16), and the guide plate (14), the separator main body (1) and the liquid guide pipe (16) are clamped through the supporting plates.
6. The water vapor filtering separator for chemical industry production according to claim 1, wherein: the cyclone reversing pipe (15) and the guide plate (14) are of an integral structure, and helical blades are arranged outside the cyclone reversing pipe (15).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921779529.2U CN210964547U (en) | 2019-10-15 | 2019-10-15 | Water vapor filtering separator for chemical production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921779529.2U CN210964547U (en) | 2019-10-15 | 2019-10-15 | Water vapor filtering separator for chemical production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210964547U true CN210964547U (en) | 2020-07-10 |
Family
ID=71440587
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921779529.2U Expired - Fee Related CN210964547U (en) | 2019-10-15 | 2019-10-15 | Water vapor filtering separator for chemical production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210964547U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114534427A (en) * | 2021-07-29 | 2022-05-27 | 遵义大兴复肥有限责任公司 | Float dish production and air treatment equipment |
| CN115090039A (en) * | 2022-06-28 | 2022-09-23 | 扬州大学 | High-efficient gas-liquid cyclone based on 3D prints |
-
2019
- 2019-10-15 CN CN201921779529.2U patent/CN210964547U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114534427A (en) * | 2021-07-29 | 2022-05-27 | 遵义大兴复肥有限责任公司 | Float dish production and air treatment equipment |
| CN115090039A (en) * | 2022-06-28 | 2022-09-23 | 扬州大学 | High-efficient gas-liquid cyclone based on 3D prints |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN210964547U (en) | Water vapor filtering separator for chemical production | |
| AU2007248358B2 (en) | Fiber bed assembly and fiber bed therefor | |
| CN104258660B (en) | Micro pore bubble type air purifier | |
| EP3458174B1 (en) | Filter assembly and method for filtration | |
| DE102015015715B4 (en) | Separation element and fuel cell system | |
| DE102012013743A1 (en) | Wasserabscheidevorrichtung, filter element of a fuel filter and fuel filter | |
| JP2009226322A (en) | Mist filter | |
| CN109097129A (en) | A kind of skid-mounted type purifying device for natural gas | |
| CN207928876U (en) | A kind of filtering layer structure of oil-mist purifying equipment | |
| CN2820279Y (en) | Coalescence filter core | |
| CN212548841U (en) | Oil fume purifier | |
| CN202921124U (en) | Self-circulation revolving liquid composite gas filter | |
| CN208943630U (en) | A kind of extra-high voltage vacuum oil-filter | |
| CN207085407U (en) | A kind of liquid liquid coarse separation device | |
| CN219764825U (en) | Efficient fiber coalescence demister | |
| CN214513543U (en) | Chemical industry sweetener catch fog device | |
| CN110499197A (en) | A kind of horizontal filter separator | |
| CN206063975U (en) | Deflection plate defoaming separator | |
| CN105413275B (en) | High flux antipollution millipore filter and its filter method | |
| CN101066788A (en) | Oil-water separator for treating oil bearing sewage | |
| CN208726963U (en) | A kind of high-efficiency blade demister | |
| CN218793891U (en) | Oil-water separation low-temperature evaporation equipment | |
| TWI857880B (en) | Composite filtration system | |
| CN218421453U (en) | Smoke filtering purifier for rolling mill | |
| CN216825190U (en) | Filter element capable of synchronously separating particulate matters and moisture in oil |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200710 Termination date: 20211015 |