CN202785716U - Compound distillation sea water desalinization equipment - Google Patents
Compound distillation sea water desalinization equipment Download PDFInfo
- Publication number
- CN202785716U CN202785716U CN2012204292325U CN201220429232U CN202785716U CN 202785716 U CN202785716 U CN 202785716U CN 2012204292325 U CN2012204292325 U CN 2012204292325U CN 201220429232 U CN201220429232 U CN 201220429232U CN 202785716 U CN202785716 U CN 202785716U
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- circular
- round
- tank
- turbine chamber
- turbine
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses compound distillation sea water desalinization equipment and solves defect that in the prior art, a flash vaporization device can not effectively utilize static energy of high-temperature and high-pressure mixed solution and can not utilize solvent in the mixed solution repeatedly. The compound distillation sea water desalinization equipment comprises a round casing, a steam outlet formed at the top of the round casing, a feed opening formed at the bottom of the round casing, and discharge openings formed on the round casing and positioned on two sides of the feed opening; a round turbine cavity communicated with the feed opening is arranged at the lower end of the round casing; a bracket is fixed in the round turbine cavity as well as the steam outlet; a rotating shaft is arranged between the two brackets; a turbine blade is arranged at the lower end of the rotating shaft, and a fan blade used for exhausting steam is arranged at the upper end; a condensation tube is arranged at the upper end of the round casing; a collecting tank is arranged below the condensation tube; an annular evaporation tank is arranged below the collecting tank; an auxiliary distillation tank is arranged between the annular evaporation tank and the round turbine cavity; the round turbine cavity is funneled; and a filtering layer is arranged at the port of the collecting tank.
Description
Technical field
The utility model relates to the treatment facility of one kind of multiple liquid mixing bodies, specifically, is a kind of compound distillation equipment for desalting seawater.
Background technology
In industrial processes, production, to the mixed stream separation of mixed uniformly liquid, normally adopt distillating method according to boiling point of liquid difference, common are simple distillation, equilibrium distillation (flash distillation), smart steaming etc., and other special distillating method.In traditional flash distillation operation, the mixing liquid of High Temperature High Pressure 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 liquid after the flash distillation, except the part that is collected, remaining liquid all is converted into gaseous emission to atmosphere, to such an extent as to be difficult to some solvent based liquid is reused, causes producing, the increase of tooling 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 liquid.
To achieve these goals, the technical solution adopted in the utility model is as follows:
Compound distillation equipment for desalting seawater, comprise circular shell, be arranged on the vapour outlet at this circular shell top, be arranged on the opening for feed of this circular shell bottom, and two discharge ports that are arranged on the circular shell and are positioned at the opening for feed both sides, be provided with the circular turbine chamber that is communicated with opening for feed in described circular shell lower end, in circular turbine chamber and vapour outlet, be fixed with respectively support, be provided with a rotation axis between two supports, this rotation axis lower end is provided with turbine blade, its upper end then is provided with the fan blade in order to exhaust vapour, also be provided with at least one prolong in the circular shell upper end, the prolong below is provided with to collect the receiving tank of liquid, this receiving tank below also is provided with the annular evaporator tank that is evenly distributed on circular turbine chamber both sides, be evenly equipped with aperture on it, between annular evaporator tank and circular turbine chamber, also be provided with auxiliary distillation tank, on annular evaporator tank, also be provided with the temperature sensor that is connected with outside indicator gauge by signal wire, and described circular turbine chamber is doline, and the port of receiving tank is provided with filtering layer.
Further, described fan blade is positioned at vapour outlet.
Simultaneously, described turbine blade is positioned at circular turbine chamber.
Further, described turbine blade is evenly distributed on the both sides of rotation axis.
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 opening for feed place, be provided with turbine blade in it, by turbine mixed solution is carried out step-down, noise when having reduced work, effectively utilized the potential energy of liquid and fluid, and by driving rotation axis, 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 work-ing life of equipment;
(3) the utility model also has been provided with some prolongs in circular shell, mixing liquid through evaporation process, the solvent based liquid that is converted into gas passes through prolong, again be converted into liquid after the condensation and be collected in the receiving tank, non-condensable gas is then discharged from vapour outlet, thereby realized the purpose of solvent based liquid recycling, reduced widely production, tooling cost;
(4) the utility model also is provided with the annular evaporator tank that is evenly distributed on circular turbine chamber both sides below receiving tank, be evenly equipped with aperture on it, the mixing liquid that ejects in the turbine chamber falls on the annular evaporator tank, through after the evaporation process, the liquid of leaving over the again aperture from the evaporator tank flows in the circular shell, to reach the purpose of collection, distillation realizes just very convenient;
(5) the utility model also is provided with the temperature sensor that is connected with outside indicator gauge by signal wire on annular evaporator tank, this temperature sensor is in order to detect the temperature of evaporator tank, the assurance vaporization temperature has avoided useful liquid to be evaporated in working range effectively;
(6) circular turbine chamber is doline in the utility model, and by funnel shaped grading profile, the mixing liquid of High Temperature High Pressure antihypertensive effect in turbine chamber is better.
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-vapour outlet, 3-opening for feed, 4-discharge port, 5-circular turbine chamber, the 6-support, 7-rotation axis, 8-turbine blade, 9-fan blade, 10-prolong, the 11-receiving tank, 12-annular evaporator tank, 13-assists distillation tank, 14-temperature sensor, 15-filtering layer.
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, compound distillation equipment for desalting seawater, comprise circular shell 1, be arranged on the vapour outlet 2 at this circular shell 1 top, be arranged on the opening for feed 3 of this circular shell 1 bottom, and two discharge ports 4 that are arranged on the circular shell and are positioned at opening for feed 3 both sides, be provided with the circular turbine chamber 5 that is communicated with opening for feed 3 in described circular shell 1 lower end, by turbine mixed solution is carried out step-down, noise when having reduced work, effectively utilize the ability of liquid and fluid, and by driving rotation axis, 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 work-ing life of equipment.Be provided with a rotation axis 7 in circular turbine chamber 5 and vapour outlet 2 interior being fixed with respectively between 6, two supports 6 of support, these rotation axis 7 lower ends are provided with turbine blade 8, and its upper end then is provided with the fan blade 9 in order to exhaust vapour.
In the present embodiment, also be provided with at least one prolong 10 in circular shell 1 upper end, prolong 10 belows are provided with to collect the receiving tank 11 of liquid, advance the mixing liquid that pervaporation is processed, the solvent based liquid that is converted into gas is by prolong, again is converted into liquid after the condensation and is collected in the receiving tank, and non-condensable gas is discharged from vapour outlet again, thereby realized the purpose of solvent based liquid recycling, reduced widely production, tooling cost.
The utility model also is provided with the annular evaporator tank 12 that is evenly distributed on circular turbine chamber 5 both sides below receiving tank 11, between circular turbine chamber and receiving tank, also be provided with auxiliary distillation tank 13, be evenly equipped with aperture on it, the mixing liquid that ejects in the turbine chamber falls on the annular evaporator tank 12, through after the evaporation process, the liquid of leaving over the again aperture from the evaporator tank flows in the circular shell, and to reach the purpose of collection, distillation realizes very convenient.
The utility model also is provided with the temperature sensor 14 that is connected with outside indicator gauge by signal wire on annular evaporator tank 12, this temperature sensor 14 is in order to detect the temperature of evaporator tank, the assurance vaporization temperature has avoided useful liquid to be evaporated in working range effectively.
Present embodiment is provided with filtering layer 15 in the port of receiving tank 11, and its liquid after in order to filter freezing guarantees the 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 vapour outlet 2.
In the present embodiment, described turbine blade 8 is positioned at circular turbine chamber 5; Described turbine blade 8 is evenly distributed on the both sides of rotation axis 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. compound distillation equipment for desalting seawater, comprise circular shell (1), be arranged on the vapour outlet (2) at this circular shell (1) top, be arranged on the opening for feed (3) of this circular shell (1) bottom, and two discharge ports (4) that are arranged on circular shell (1) upward and are positioned at opening for feed (3) both sides, it is characterized in that: be provided with the circular turbine chamber (5) that is communicated with opening for feed (3) in described circular shell (1) lower end, in circular turbine chamber (5) and vapour outlet (2), be fixed with respectively support (6), be provided with a rotation axis (7) between two supports (6), this rotation axis (7) lower end is provided with turbine blade (8), its upper end then is provided with the fan blade (9) in order to exhaust vapour, also be provided with at least one prolong (10) in circular shell (1) upper end, prolong (10) below is provided with to collect the receiving tank (11) of liquid, this receiving tank (11) below also is provided with the annular evaporator tank (12) that is evenly distributed on circular turbine chamber (5) both sides, be evenly equipped with aperture on it, between annular evaporator tank (12) and circular turbine chamber (5), also be provided with auxiliary distillation tank (13), on annular evaporator tank (12), also be provided with the temperature sensor (14) that is connected with outside indicator gauge by signal wire, and described circular turbine chamber (5) is doline, is provided with filtering layer (15) in the port of receiving tank (11).
2. compound distillation equipment for desalting seawater according to claim 1, it is characterized in that: described fan blade (9) is positioned at vapour outlet (2).
3. compound distillation equipment for desalting seawater according to claim 2, it is characterized in that: described turbine blade (8) is positioned at circular turbine chamber (5).
4. compound distillation equipment for desalting seawater according to claim 3, it is characterized in that: described turbine blade (8) is evenly distributed on the both sides of rotation axis (7).
5. compound distillation equipment for desalting seawater 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 |
|---|---|---|---|
| CN2012204292325U CN202785716U (en) | 2012-08-28 | 2012-08-28 | Compound distillation sea water desalinization equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012204292325U CN202785716U (en) | 2012-08-28 | 2012-08-28 | Compound distillation sea water desalinization equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202785716U true CN202785716U (en) | 2013-03-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012204292325U Expired - Fee Related CN202785716U (en) | 2012-08-28 | 2012-08-28 | Compound distillation sea water desalinization equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202785716U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103939153A (en) * | 2014-05-05 | 2014-07-23 | 北京良明同创水处理设备开发中心 | Integrated thermoelectric fresh water co-generation combined cooling, heating and power system |
-
2012
- 2012-08-28 CN CN2012204292325U patent/CN202785716U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103939153A (en) * | 2014-05-05 | 2014-07-23 | 北京良明同创水处理设备开发中心 | Integrated thermoelectric fresh water co-generation combined cooling, heating and power system |
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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 |