CN206051602U - A kind of efficient tower type distills Water generator - Google Patents
A kind of efficient tower type distills Water generator Download PDFInfo
- Publication number
- CN206051602U CN206051602U CN201621086689.5U CN201621086689U CN206051602U CN 206051602 U CN206051602 U CN 206051602U CN 201621086689 U CN201621086689 U CN 201621086689U CN 206051602 U CN206051602 U CN 206051602U
- Authority
- CN
- China
- Prior art keywords
- condenser
- distilled water
- steam
- water
- baffle plates
- 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
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
This utility model is related to a kind of efficient tower type distillation Water generator of medical use, it is mainly made up of steam inlet, steam selector, water inlet, serpentine heating pipe, waste gas displacer, overflow pipe, liquidometer, demister, distilled water baffle plate, the first condenser, steam vent A, tower body, steam vent B, the second condenser, 30 ° of baffle plates, distilled water outlet, the 3rd condenser and distillation water collectors, it is characterised in that:Tower body left part has steam inlet, steam selector, steam vent B, the second condenser, 30 ° of baffle plates, distilled water outlet, the 3rd condenser and distillation water collectors, there are water inlet, serpentine heating pipe, demister, distilled water baffle plate, the first condenser, 30 ° of baffle plates in inside, and right part has waste gas displacer, overflow pipe, liquidometer, steam vent A.First condenser is designed using U-tube, and the second condenser and the 3rd condenser are designed using coil;The inclination angle of 30 ° of baffle plates is 30 °.
Description
Technical field
This utility model is related to a kind of efficient tower type distillation Water generator of medical use.
Background technology
With society and the development of production, in opposite bioplasm quantity and form, there is high requirement, many fields are required for
The other distilled water of medical grade is used, and such as distilled water is required in terms of modern mechanical production, scientific experimentss, medical treatment and pharmacy etc., and
The water of nature is not pure water, and it is distillation to obtain pure water cost performance highest approach.Tower distilled water unit is that a class is more early
The old-fashioned distilled water unit of sizing production, foreign countries have tended to superseded, but domestic many producers or hospital pharmacy are still in application.Which is not enough
It is that the water yield in evaporation boiler is unsuitable excessive, the pressure for heating steam is also unsuitable excessive, in case droplet is scurried in condenser and is affected
The quality of distilled water.And it is only used for Batch Process, it is impossible to continuously produced, equipment is taken off using metal ion after a period of time
Fall and cause to generate water by trace heavy metal element pollution, and form easy bacterial growth of incrustation scale etc..It is easy in process of production
Cause wastage of material and environmental pollution;Distillation is that water is heated into vapor, and the process of water is then re-formed through condensation.
The content of the invention
This utility model purpose is the efficiency that distilled water is generated to improve distillation Water generator, there is provided a kind of high efficiency tower
Formula distills Water generator, convenient to use, time saving and energy saving, can improve the efficiency for generating distilled water.
The technical scheme adopted by this utility model is:
A kind of efficient tower type of this utility model distills Water generator, mainly by steam inlet, steam selector, water inlet,
Serpentine heating pipe, waste gas displacer, overflow pipe, liquidometer, demister, distilled water baffle plate, the first condenser, steam vent A, tower
Body, steam vent B, the second condenser, 30 ° of baffle plates, distilled water outlet, the 3rd condenser and distillation water collector compositions, its feature
It is:Tower body left part have steam inlet, steam selector, steam vent B, the second condenser, 30 ° of baffle plates, distilled water outlet, the 3rd
Condenser and distillation water collector, inside have water inlet, serpentine heating pipe, demister, distilled water baffle plate, the first condenser, 30 °
Baffle plate, right part have waste gas displacer, overflow pipe, liquidometer, steam vent A.First condenser is designed using U-tube, the second condensation
Device and the 3rd condenser are designed using coil;The inclination angle of 30 ° of baffle plates is 30 °;Distilled water baffle plate is designed using rounding angie type,
Its purpose is to allow the distilled water for condensing out to flow toward on the left of tower body, and flow to distilled water outlet outflow;Demister is used for
The drop of gas entrainment in knockout tower;Liquidometer is located at the right lower quadrant of tower body, for the height of liquid level in observing tower body.
Advantage of the present utility model:Convenient to use, time saving and energy saving, maintenance is simple, can effectively improve generation distilled water
Efficiency.
Description of the drawings
Fig. 1 is the structural representation that a kind of efficient tower type of this utility model distills Water generator.
In figure:1. steam inlet, 2. steam selector, 3. water inlet, 4. serpentine heating pipe, 5. waste gas displacer, 6. overflows
Flow tube, 7. liquidometer, 8. demister, 9. distilled water baffle plate, 10. the first condenser, 11. steam vent A, 12. tower bodies, 13. aerofluxuss
Hole B, 14. second condensers, 15.30 ° of baffle plates, 16. distilled water outlets, 17. the 3rd condensers, 18. distillation water collectors.
Specific embodiment
Below in conjunction with the accompanying drawings this utility model is described further.
As shown in figure 1, a kind of efficient tower type of this utility model distills Water generator, mainly selected by steam inlet 1, steam
Device 2, water inlet 3, serpentine heating pipe 4, waste gas displacer 5, overflow pipe 6, liquidometer 7, demister 8, distilled water baffle plate 9, first
Condenser 10, steam vent A 11, tower body 12, steam vent B 13,14,30 ° of baffle plates 15 of the second condenser, distilled water outlet 16,
Three condensers 17 and distillation water collector 18 are constituted, it is characterised in that:12 left part of tower body have steam inlet 1, steam selector 2,
Steam vent B 13,14,30 ° of baffle plates 15 of the second condenser, distilled water outlet 16, the 3rd condenser 17 and distillation water collector 18,
There are water inlet 3, serpentine heating pipe 4, demister 8, distilled water baffle plate 9,10,30 ° of baffle plates 15 of the first condenser in inside, and right part has useless
Gas displacer 5, overflow pipe 6, liquidometer 7, steam vent A 11.
As shown in figure 1, steam enters tower body 12 after steam selector 2 is selected by steam inlet 1, by snakelike heating
Discharged by waste gas displacer 5 after pipe 4 and water heat exchange, vapor is water is vaporized into after heat exchange upwardly through demister 8, is removed in gas
The drop of entrainment, is condensed the drop Jing distilled water baffle plate 9 and 30 ° of baffle plates 15 that are formed by distilled water outlet 16 by the first condenser 10
Flow out, remainder gas is condensed into water into the second condenser 14 by steam vent B 13 and enters the 3rd condenser 17 of people, and before
The condensed water of formation flows into distillation water collector 18 after condensing again together.
As shown in figure 1, being closed under 11 normalities of steam vent A;Liquidometer 7 is provided with 12 lower left side of tower body, is used for
Liquid level in monitoring tower;If too high, unnecessary water is flowed out by overflow pipe 6, it is too low then by the water delivery inwards of water inlet 3.
Claims (3)
1. a kind of efficient tower type distills Water generator, mainly by steam inlet (1), steam selector (2), water inlet (3), snakelike
Heating tube (4), waste gas displacer (5), overflow pipe (6), liquidometer (7), demister (8), distilled water baffle plate (9), the first condensation
Device (10), steam vent A (11), tower body (12), steam vent B (13), the second condenser (14), 30 ° of baffle plates (15), distilled water outlets
(16), the 3rd condenser (17) and distillation water collector (18) composition, it is characterised in that:Tower body (12) left part has steam inlet
(1), steam selector (2), steam vent B (13), the second condenser (14), 30 ° of baffle plates (15), distilled water outlet (16), the 3rd
Condenser (17) and distillation water collector (18), inside have water inlet (3), serpentine heating pipe (4), demister (8), distilled water gear
Plate (9), the first condenser (10), 30 ° of baffle plates (15), right part have waste gas displacer (5), overflow pipe (6), liquidometer (7), aerofluxuss
Hole A (11).
2. a kind of efficient tower type according to claim 1 distills Water generator, it is characterised in that:First condenser (10) is adopted
Designed with U-tube, the second condenser (14) and the 3rd condenser (17) are designed using coil;The inclination angle of 30 ° of baffle plates (15)
For 30 °.
3. a kind of efficient tower type according to claim 1 distills Water generator, it is characterised in that:Distilled water baffle plate (9) is adopted
Designed with rounding angie type, its purpose is to allow the distilled water for condensing out to flow toward on the left of tower body (12), and flow to distilled water
Outlet (16) is flowed out;Drop of the demister (8) for gas entrainment in knockout tower;Bottom right of the liquidometer (7) positioned at tower body (12)
Portion, for observing the height of the interior liquid level of tower body (12).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621086689.5U CN206051602U (en) | 2016-09-28 | 2016-09-28 | A kind of efficient tower type distills Water generator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621086689.5U CN206051602U (en) | 2016-09-28 | 2016-09-28 | A kind of efficient tower type distills Water generator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206051602U true CN206051602U (en) | 2017-03-29 |
Family
ID=58366098
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621086689.5U Expired - Fee Related CN206051602U (en) | 2016-09-28 | 2016-09-28 | A kind of efficient tower type distills Water generator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206051602U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112340798A (en) * | 2020-10-20 | 2021-02-09 | 郭绵君 | Industrial prefabricated distilled water preparation device |
-
2016
- 2016-09-28 CN CN201621086689.5U patent/CN206051602U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112340798A (en) * | 2020-10-20 | 2021-02-09 | 郭绵君 | Industrial prefabricated distilled water preparation device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104759108B (en) | Three grades of continuous falling liquid film circulating and evaporating concentration systems with function of mechanical steam recompression | |
CN202590405U (en) | Triple effect concentration evaporator | |
CN104591327A (en) | Loop heat pipe-type cylindrical solar seawater desalination device | |
CN205035108U (en) | A light water condenser for sea water desalination device | |
JP5971177B2 (en) | Evaporation and concentration equipment for aqueous caustic soda | |
CN202983245U (en) | MVR (Mechanical Vapor Recompression) evaporator applicable to concentration of magnesium sulfate solution | |
CN206051602U (en) | A kind of efficient tower type distills Water generator | |
CN209033781U (en) | A kind of energy-efficient MVR crystallization enrichment facility | |
CN205145636U (en) | Novel distillation device | |
CN204404134U (en) | Pure steam generator | |
CN212700588U (en) | Multi-effect falling film evaporation concentrator unit system | |
CN206027123U (en) | Waste solvent recoverer suitable for coating processing | |
CN101525196A (en) | Multi-effect distilled seawater desalting plant with pre-heater | |
CN217961331U (en) | Novel negative pressure MVR evaporation equipment | |
CN203699954U (en) | Recovery system of ammonia steam waste heat generated in ammonia steaming process | |
CN103553164B (en) | High-salt wastewater treatment system for horizontal-vertical tube falling film multiple-effect evaporation | |
CN105692744B (en) | A kind of medical multi-effect water distillator | |
CN205917042U (en) | Concentrated system of high salt waste water MVR of separable low boiling difficult degradation organic matter | |
CN207527540U (en) | A kind of Steam Recovery boiler plant and energy saver containing frequency conversion fan | |
CN205722825U (en) | A kind of uranium-containing waste water enrichment facility | |
CN205164164U (en) | Tape unit tool vapor recompression's tertiary concentrated system of falling liquid film circulation evaporating in succession | |
CN206184013U (en) | System for utilize air heat pump low temperature evaporative concentration alcohol waste liquid | |
CN105169734A (en) | Vacuum rectification device and rectification method thereof | |
RU65395U1 (en) | Desalination plant | |
JP6015507B2 (en) | Evaporation concentration equipment for caustic soda aqueous solution and method for concentrating caustic soda aqueous solution using the equipment |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170329 Termination date: 20170928 |
|
CF01 | Termination of patent right due to non-payment of annual fee |