CN202785715U - Combined-type sea water desalinization equipment - Google Patents
Combined-type sea water desalinization equipment Download PDFInfo
- Publication number
- CN202785715U CN202785715U CN2012204292043U CN201220429204U CN202785715U CN 202785715 U CN202785715 U CN 202785715U CN 2012204292043 U CN2012204292043 U CN 2012204292043U CN 201220429204 U CN201220429204 U CN 201220429204U CN 202785715 U CN202785715 U CN 202785715U
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- Prior art keywords
- round
- circular
- turbine
- turbine chamber
- sea water
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- 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
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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 combined-type sea water desalinization equipment, and overcomes the defects that a flash distillation plant in the prior art cannot effectively utilize the static energy of high-temperature and high-pressure mixed liquor and cannot recycle the solvent in the mixed liquor. The equipment comprises a round casing, a steam outlet, a feed opening, discharge openings, a round turbine cavity, two brackets, a rotating shaft, turbine blades, fan blades, condensation pipes, a collecting tank, annular evaporation tanks and an auxiliary distillation tank. The steam outlet is formed at the top of the round casing; the feed opening is arranged at the bottom of the round casing; two discharge openings are arranged at two sides of the feed opening on the round casing respectively; the round turbine cavity communicated with the feed opening is arranged at the lower end of the round casing; the two brackets are fixed in the round turbine cavity and the steam outlet respectively; the rotating shaft is arranged between the two brackets; the turbine blades are arranged at the lower end of the rotating shaft; the fan blades used for exhausting steam are arranged at the upper end of the rotating shaft; the condensation pipes are arranged at the upper end of the round casing; the collecting tank is arranged under the condensation pipes; the annular evaporation tanks are evenly distributed at the two sides of the round turbine cavity under the collecting tank; the auxiliary distillation tank is further arranged between the annular evaporation tanks and the round turbine cavity; and the round turbine cavity appears to be a funnel.
Description
Technical field
The utility model relates to the treatment facility of one kind of multiple liquid mixing bodies, specifically, is a kind of combined type sea water desalting equipment.
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:
The combined type sea water desalting equipment, 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, and described circular turbine chamber is doline.
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 very convenient;
(5) 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, the 7-rotation axis, the 8-turbine blade, the 9-fan blade, the 10-prolong, the 11-receiving tank, 12-annular evaporator tank, 13-assists distillation tank.
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, the combined type sea water desalting equipment, 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.
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.
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. combined type sea water desalting equipment, 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), and described circular turbine chamber (5) is doline.
2. combined type sea water desalting equipment according to claim 1, it is characterized in that: described fan blade (9) is positioned at vapour outlet (2).
3. combined type sea water desalting equipment according to claim 2, it is characterized in that: described turbine blade (8) is positioned at circular turbine chamber (5).
4. combined type sea water desalting equipment 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. combined type sea water desalting equipment 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 |
---|---|---|---|
CN2012204292043U CN202785715U (en) | 2012-08-28 | 2012-08-28 | Combined-type sea water desalinization equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN2012204292043U CN202785715U (en) | 2012-08-28 | 2012-08-28 | Combined-type sea water desalinization equipment |
Publications (1)
Publication Number | Publication Date |
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CN202785715U true CN202785715U (en) | 2013-03-13 |
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Application Number | Title | Priority Date | Filing Date |
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CN2012204292043U Expired - Fee Related CN202785715U (en) | 2012-08-28 | 2012-08-28 | Combined-type sea water desalinization equipment |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110272138A (en) * | 2019-08-05 | 2019-09-24 | 马鞍山市新桥工业设计有限公司 | A kind of equipment for sewage treatment |
CN110282770A (en) * | 2019-08-05 | 2019-09-27 | 马鞍山市新桥工业设计有限公司 | A kind of sewage-treatment plant |
-
2012
- 2012-08-28 CN CN2012204292043U patent/CN202785715U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110272138A (en) * | 2019-08-05 | 2019-09-24 | 马鞍山市新桥工业设计有限公司 | A kind of equipment for sewage treatment |
CN110282770A (en) * | 2019-08-05 | 2019-09-27 | 马鞍山市新桥工业设计有限公司 | A kind of sewage-treatment plant |
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Legal Events
Date | Code | Title | Description |
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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 |