CN202777890U - Water vapor separation mechanism - Google Patents
Water vapor separation mechanism Download PDFInfo
- Publication number
- CN202777890U CN202777890U CN 201220429133 CN201220429133U CN202777890U CN 202777890 U CN202777890 U CN 202777890U CN 201220429133 CN201220429133 CN 201220429133 CN 201220429133 U CN201220429133 U CN 201220429133U CN 202777890 U CN202777890 U CN 202777890U
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- separation mechanism
- vapor separation
- circular
- water vapor
- vapor
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Abstract
The utility model discloses a water vapor separation mechanism and overcomes the defects that the potential energy of a high-temperature and high-pressure mixed solution cannot be effectively utilized and a solvent in the mixed solution cannot be repeatedly utilized in a flash distillation device in the prior art. The water vapor separation mechanism comprises a round housing, a steam outlet arranged at the top of the round housing, a material inlet arranged at the bottom of the round housing, and two material outlets arranged on the round housing and positioned on the two sides of the material inlet, wherein a round turbine cavity communicated with the material inlet is formed in the lower end of the round housing; brackets are fixed in the round turbine cavity and the steam outlet respectively; a rotary shaft is arranged between the two brackets; turbine blades are arranged at the lower end of the rotary shaft; fan blades for discharging steam are arranged at the upper end of the rotary shaft; a condensing pipe is also arranged at the upper end of the round housing; a collecting tank is arranged below the condensing pipe; a baffle is also arranged below the collecting tank; and a filter layer is arranged at the ports of the collecting tank. The water vapor separation mechanism is simple in structure, low in cost and convenient to realize. Therefore, the water vapor separation mechanism is suitable for popularization and application.
Description
Technical field
The utility model relates to the treatment facility of one kind of multiple liquid mixtures, specifically, is a kind of water-vapor separation mechanism.
Background technology
In industrial processes, production, to the fluid-mixing separation of mixed uniformly liquid, normally adopt distillating method according to boiling point of liquid difference, common are simple distillation, equlibrium distillation (flash distillation), smart steaming etc., and other special distillating method.In traditional flash distillation operation, the mixing material of HTHP enters separator after by decompression method step-down and carries out gas-liquid separation, and this kind mode does not effectively utilize the potential energy that high temperature high pressure liquid has; On the other hand, through the mixing material after the flash distillation, except the part that is collected, remaining liquid all is converted into gas discharging to atmosphere, to such an extent as to be difficult to some solvent based liquid is reused, causes producing, the increase of processing cost.
The utility model content
The purpose of this utility model is to overcome defects, provide a kind of simple in structure, with low cost, realize the easily flash distillation plant of mixing material.
To achieve these goals, the technical solution adopted in the utility model is as follows:
Water-vapor separation mechanism, comprise circular shell, be arranged on the steam (vapor) outlet at this circular shell top, be arranged on the charging aperture of this circular shell bottom, and two discharging openings that are arranged on the circular shell and are positioned at the charging aperture both sides, be provided with the circular turbine chamber that is communicated with charging aperture in described circular shell lower end, in circular turbine chamber and steam (vapor) outlet, be fixed with respectively support, be provided with a turning cylinder between two supports, this turning cylinder lower end is provided with turbo blade, its upper end then is provided with the fan blade in order to exhaust steam, also be provided with at least one condenser pipe in the circular shell upper end, the condenser pipe below is provided with to collect the feeder of liquid, and this feeder below also is provided with baffle plate, and the port of this feeder is provided with filter course.
Further, described fan blade is positioned at steam (vapor) outlet.
Simultaneously, described turbo blade is positioned at circular turbine chamber.
Further, described turbo blade is evenly distributed on the both sides of turning cylinder.
Further, described circular turbine chamber extends to the outside of circular shell.
Compared with prior art, the beneficial effects of the utility model are:
(1) the utility model is not only simple in structure, and is with low cost, and realizes conveniently;
(2) the utility model is provided with the circular turbine chamber that is communicated with it at the charging aperture place, be provided with turbo blade in it, by turbine mixed liquor is carried out step-down, noise when having reduced work, effectively utilized the potential energy of liquid and fluid, and by driving turning cylinder, realize the balance of flash distillation plant energy; On the other hand, greatly reduce the impact of the interior liquids and gases of flash distillation plant to the device internal structure, prolonged the service life of equipment;
(3) the utility model also has been provided with some condenser pipes in circular shell, mixing material through evaporation process, the solvent based liquid that is converted into gas passes through condenser pipe, again be converted into liquid after the condensation and be collected in the feeder, fixed gas is then discharged from steam (vapor) outlet, thereby realized the purpose of solvent based liquid recycling, reduced widely production, processing cost;
(4) the utility model is provided with filter course in the port of feeder, and its liquid after in order to filter freezing guarantees the degree of purity of the liquid that condensation is collected, and is convenient to recycling.
Description of drawings
Fig. 1 is structural representation of the present utility model.
In the accompanying drawing, the title that Reference numeral is corresponding:
1-circular shell, 2-steam (vapor) outlet, 3-charging aperture, 4-discharging opening, 5-circular turbine chamber, 6-support, 7-turning cylinder, 8-turbo blade, 9-fan blade, 10-condenser pipe, 11-feeder, 12-baffle plate, 13-filter course.
The specific embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.Embodiment of the present utility model includes but not limited to following case.
Embodiment
As shown in Figure 1, water-vapor separation mechanism, comprise circular shell 1, be arranged on the steam (vapor) outlet 2 at this circular shell 1 top, be arranged on the charging aperture 3 of this circular shell 1 bottom, and two discharging openings 4 that are arranged on the circular shell and are positioned at charging aperture 3 both sides, be provided with the circular turbine chamber 5 that is communicated with charging aperture 3 in described circular shell 1 lower end, by turbine mixed liquor is carried out step-down, noise when having reduced work, effectively utilize the ability of liquid and fluid, and by driving turning cylinder, realized the balance of flash distillation plant energy; On the other hand, greatly reduce the impact of the interior liquids and gases of flash distillation plant to the device internal structure, prolonged the service life of equipment.Being fixed with respectively between 6, two supports 6 of support in circular turbine chamber 5 and steam (vapor) outlet 2 is provided with a turning cylinder 7, and these turning cylinder 7 lower ends are provided with turbo blade 8, and its upper end then is provided with the fan blade 9 in order to exhaust steam.
In the present embodiment, also be provided with at least one condenser pipe 10 in circular shell 1 upper end, condenser pipe 10 belows are provided with to collect the feeder 11 of liquid, advance the mixing material that pervaporation is processed, the solvent based liquid that is converted into gas is by condenser pipe, again is converted into liquid after the condensation and is collected in the feeder, and fixed gas is discharged from steam (vapor) outlet again, thereby realized the purpose of solvent based liquid recycling, reduced widely production, processing cost.On the other hand, below feeder 11, also be provided with baffle plate 12.
Present embodiment is provided with filter course 13 in the port of feeder, and its liquid after in order to filter freezing guarantees the degree of purity of the liquid that condensation is collected, and is convenient to recycling.
In order to reach better exhaust effect, described fan blade 9 is positioned at steam (vapor) outlet 2.
In the present embodiment, described turbo blade 8 is positioned at circular turbine chamber 5; Described turbo blade 8 is evenly distributed on the both sides of turning cylinder 7; Described circular turbine chamber 5 extends to the outside of circular shell 1.
According to above-described embodiment, just can realize well the utility model.
Claims (5)
1. water-vapor separation mechanism, comprise circular shell (1), be arranged on the steam (vapor) outlet (2) at this circular shell (1) top, be arranged on the charging aperture (3) of this circular shell (1) bottom, and two discharging openings (4) that are arranged on circular shell (1) upward and are positioned at charging aperture (3) both sides, it is characterized in that: be provided with the circular turbine chamber (5) that is communicated with charging aperture (3) in described circular shell (1) lower end, in circular turbine chamber (5) and steam (vapor) outlet (2), be fixed with respectively support (6), be provided with a turning cylinder (7) between two supports (6), this turning cylinder (7) lower end is provided with turbo blade (8), its upper end then is provided with the fan blade (9) in order to exhaust steam, also be provided with at least one condenser pipe (10) in circular shell (1) upper end, condenser pipe (10) below is provided with to collect the feeder (11) of liquid, the port of this feeder (11) is provided with filter course (13), and its below also is provided with baffle plate (12).
2. water-vapor separation mechanism according to claim 1, it is characterized in that: described fan blade (9) is positioned at steam (vapor) outlet (2).
3. water-vapor separation mechanism according to claim 2, it is characterized in that: described turbo blade (8) is positioned at circular turbine chamber (5).
4. water-vapor separation mechanism according to claim 3, it is characterized in that: described turbo blade (8) is evenly distributed on the both sides of turning cylinder (7).
5. water-vapor separation mechanism according to claim 4, it is characterized in that: described circular turbine chamber (5) extends to the outside of circular shell (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220429133 CN202777890U (en) | 2012-08-28 | 2012-08-28 | Water vapor separation mechanism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220429133 CN202777890U (en) | 2012-08-28 | 2012-08-28 | Water vapor separation mechanism |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202777890U true CN202777890U (en) | 2013-03-13 |
Family
ID=47805238
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220429133 Expired - Fee Related CN202777890U (en) | 2012-08-28 | 2012-08-28 | Water vapor separation mechanism |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202777890U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104523145A (en) * | 2014-12-16 | 2015-04-22 | 沁园集团股份有限公司 | Water dispenser with steam eliminating function |
| CN108379997A (en) * | 2018-04-13 | 2018-08-10 | 郑州轻工业学院 | Small multi-channel steam condenses liquid trap |
-
2012
- 2012-08-28 CN CN 201220429133 patent/CN202777890U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104523145A (en) * | 2014-12-16 | 2015-04-22 | 沁园集团股份有限公司 | Water dispenser with steam eliminating function |
| CN108379997A (en) * | 2018-04-13 | 2018-08-10 | 郑州轻工业学院 | Small multi-channel steam condenses liquid trap |
| CN108379997B (en) * | 2018-04-13 | 2023-04-18 | 郑州轻工业学院 | Small multi-channel steam condensation liquid collector |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130313 Termination date: 20130828 |