CN103130290A - Stripping system based on internal screw multi-effect water distillatory - Google Patents
Stripping system based on internal screw multi-effect water distillatory Download PDFInfo
- Publication number
- CN103130290A CN103130290A CN2012101727461A CN201210172746A CN103130290A CN 103130290 A CN103130290 A CN 103130290A CN 2012101727461 A CN2012101727461 A CN 2012101727461A CN 201210172746 A CN201210172746 A CN 201210172746A CN 103130290 A CN103130290 A CN 103130290A
- Authority
- CN
- China
- Prior art keywords
- steam
- water
- internal screw
- chamber
- effect
- 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.)
- Pending
Links
Images
Abstract
The invention discloses a stripping system based on an internal screw multi-effect water distillatory. The stripping system based on the internal screw multi-effect water distillatory mainly comprises the internal screw multi-effect water distillatory, an industrial steam system, a purified water system and a condenser, wherein the industrial steam system, the purified water system and the condenser are connected with the internal screw multi-effect water distillatory, and the condenser is further connected with a condensate water system. The stripping system based on the internal screw multi-effect water distillatory has the advantages that due to the fact that a mode of internal screw three-level separation is adopted, purify and drying of steam separation are guaranteed, bacterium endomycin is completely separated, water quality of distilled water can be improved, and an ideal energy-saving effect can be achieved.
Description
Technical field
The present invention relates to the generation equipment of distilled water, specifically refer to the system of heating up in a steamer of putting forward based on the internal screw multi-effect water distillator.
Background technology
Distilled water refers to the pure water with the distillating method preparation.Can divide once and distilled water repeatedly.Be widely used in medical treatment, scientific research, productive life.
Equipment for the production of distilled water is referred to as distillation machine, and existing distilled water equipment is varied, according to the purity of the water after distillation, divides the grade of distillation machine with this.
In existing first water, general employing directly adds evaporates water, gets final product after the water that obtains condensing.For this type of distillation machine, owing to there is no follow-up treatment measures, the distilled water purity that therefore obtains is not high.And to obtain highly purified distilled water, and its equipment cost and the cost that puts into production are all higher, and this is the multistage mode of production that adopts due to existing high purity distilled water production unit, and the distilled water that soon obtains for the first time distills again as former water.The initial stage of its energy consumption, and production unit for this reason drops into all higher.
For this reason, we are in order to reduce the production cost of distilled water, and we need to improve in one-level distilled water equipment, just can obtain the higher distilled water of purity after one-level is produced.
Summary of the invention
The purpose of this invention is to provide simple in structure, cost is low, produce the distilled water purity high system of heating up in a steamer of putting forward based on the internal screw multi-effect water distillator.
To achieve these goals, the technical solution used in the present invention is: based on the system of heating up in a steamer of carrying of internal screw multi-effect water distillator, mainly be made of internal screw multi-effect water distillator and the industrial steam system, water purification system, the condenser that are connected with the internal screw multi-effect water distillator, described condenser also is connected with condensate system; Described internal screw multi-effect water distillator is mainly by the steam gravity separator, and the steam generation chamber that is arranged on steam gravity separator top, and the pure water vapour outlet and the liquid water that are arranged on top, steam generation chamber are imported and exported formation, described steam generates the indoor centrifugal steam separate chamber of also being provided with, described centrifugal steam separate chamber is connected with the conducting of steam gravity separator, described liquid water is imported and exported with steam generation chamber conducting and is connected, and described pure water vapour outlet is connected with the separate chamber's conducting of centrifugal steam; Described pure water vapour outlet is connected with condenser, and water purification system is imported and exported with liquid water and is connected, and described industrial steam system and steam generate the chamber interior conducting.
Described steam generates the indoor two ends that are provided with and is connected respectively the generating tube that is connected with the steam gravity separator with liquid water.
Be provided with roughing out chamber, the indoor undergauge helical cavity that is provided with of described roughing out in described centrifugal steam separate chamber; The described centrifugal steam Huo of separate chamber and roughing out chamber Huo and undergauge helical cavity have the whirlwind mouth.
Centrifugal steam separate chamber is connected with the steam gravity separator by the gravity water pipe.
Described steam generates the indoor high-temperature steam that is full of.
based on foregoing, the vaporizer that the present invention adopts is to use the Boiler Steam of industrial steam system the inside to calorify generating tube, the raw water of water purification system the inside enters generating tube from liquid water, generate under the indoor effect that is full of high-temperature steam at steam, raw water changes water vapor into, and formation film falling film evaporation, vapour stream after collecting and separating at steam gravity separator place for the raw water of evaporation, vapour stream forms 180 ° turning to simultaneously, enter into centrifugal steam separate chamber, vapour stream carries out the low speed roughing out in the roughing out chamber near the bottom of steam gravity separator one end in centrifugal steam separate chamber, and the large drop in steam water interface is thrown into the inwall of centrifugal steam separate chamber under the effect of centrifugal force, make large drop along the downward landing of inwall of steam separate chamber.Vapour stream after roughing out simultaneously begins to continue to rise, and arrives in centrifugal steam separate chamber's medium position arrival undergauge helical cavity, under the effect of cyclone, has accelerated the rotation flow velocity of vapour stream, and centrifugal motion at a high speed continues to remove water droplet and impurity.Vapour stream continues to rise, when arriving the top of undergauge helical cavity, be in the air intake position of whirlwind mouth due to the top of undergauge helical cavity, so the vapour stream in the undergauge helical cavity forms the high-speed motion whirlpool, centripetal acceleration is faster, and water droplet is given the inwall that is thrown to the undergauge helical cavity by powerful centripetal force.And fall, enter the gravity water pipe and arrive the steam gravity separator.
Then, pure steam is transported to condenser inside, and under the effect of condensate system, water coolant also is injected into condenser inside, makes pure steam be condensed and is converted into pure distilled water.
With this, the invention has the advantages that the present invention adopts the mode of three grades of separation of internal screw, guaranteed the clean dry of vapor removal, the bacterium endomycin separates thoroughly, can improve the water quality of distilled water.And can obtain desirable energy-saving effect.
Description of drawings
Fig. 1 is the structural representation of internal screw multi-effect water distillator in the present invention.
Fig. 2 is system construction drawing of the present invention.
Label in figure is expressed as respectively: 1, pure water vapour outlet; 2, liquid water is imported and exported; 4, generating tube; 5, whirlwind mouth; 6, undergauge helical cavity; 7, steam gravity separator; 8, gravity water pipe; 9, roughing out chamber; 11, centrifugal steam separate chamber; 12, steam generates the chamber.
Embodiment
Below in conjunction with embodiment, the present invention is described in further detail, but embodiment of the present invention is not limited to this.
As shown in Figure 1, 2, the present invention adopts the mode of three grades of separation of internal screw, has guaranteed the clean dry of vapor removal, and the bacterium endomycin separates thoroughly, can improve the water quality of distilled water.And can obtain desirable energy-saving effect.Based on the system of heating up in a steamer of carrying of internal screw multi-effect water distillator, mainly consisted of by internal screw multi-effect water distillator and the industrial steam system, water purification system, the condenser that are connected with the internal screw multi-effect water distillator, described condenser also is connected with condensate system;
Described internal screw multi-effect water distillator is mainly by steam gravity separator 7, and the steam generation chamber 12 that is arranged on steam gravity separator 7 tops, and the pure water vapour outlet 1 and liquid water import and export 2 formations that are arranged on steam generation 12 tops, chamber, described steam generates and also is provided with centrifugal steam separate chamber 11 in chamber 12, described centrifugal steam separate chamber 11 is connected with 7 conductings of steam gravity separator, described liquid water is imported and exported 2 and is connected with steam generation chamber 12 conductings, and described pure water vapour outlet 1 is connected with separate chamber's 11 conductings of centrifugal steam.
Described pure water vapour outlet 1 is connected with condenser, and water purification system is imported and exported 2 with liquid water and is connected, and described industrial steam system and steam generate the inner conducting in chamber 12.
Described steam generates in chamber 12 and is provided with generating tube 4, and the two ends of described generating tube 4 are are connected 2 with steam gravity separator 7 with liquid water respectively and are connected.
Be provided with roughing out chamber 9 in described centrifugal steam separate chamber 11, be provided with undergauge helical cavity 6 in described roughing out chamber 9.
The 11 Huo of described centrifugal steam separate chamber and roughing out chamber 9 Huo and undergauge helical cavity 6 have whirlwind mouth 5.
Centrifugal steam separate chamber 11 is connected with steam gravity separator 7 by gravity water pipe 8.
Described steam generates in chamber 12 and is full of high-temperature steam.
based on foregoing, the vaporizer that the present invention adopts is to use Boiler Steam to calorify generating tube 4, raw water is imported and exported 2 from liquid water and is entered generating tube 4, in generating chamber 12, steam is full of under the effect of high-temperature steam, raw water changes water vapor into, and formation film falling film evaporation, vapour stream after collecting and separating at steam gravity separator 7 places for the raw water of evaporation, vapour stream forms 180 ° turning to simultaneously, enter into centrifugal steam separate chamber 11, vapour stream 11 carries out the low speed roughing out near the roughing out chamber 9 of the bottom of steam gravity separator 7 one ends in centrifugal steam separate chamber, and the large drop in steam water interface is thrown into the inwall of centrifugal steam separate chamber 11 under the effect of centrifugal force, make 11 the downward landing of inwall along the steam separate chamber of large drop.Simultaneously the vapour stream after roughing out begins to continue to rise, and arrives centrifugal steam separate chamber 11 medium positions and arrives in undergauge helical cavity 6, under the effect of cyclone, has accelerated the rotation flow velocity of vapour stream, and centrifugal motion at a high speed continues removal water droplet and impurity.Vapour stream continues to rise, when arriving the top of undergauge helical cavity 6, be in the air intake position of whirlwind mouth 5 due to the top of undergauge helical cavity 6, therefore the vapour stream in undergauge helical cavity 6 forms the high-speed motion whirlpool, centripetal acceleration is faster, and water droplet is given the inwall that is thrown to undergauge helical cavity 6 by powerful centripetal force.And fall, enter gravity water pipe 8 and arrive steam gravity separator 7.
Just can better realize the present invention as mentioned above.
Claims (5)
1. based on the system of heating up in a steamer of carrying of internal screw multi-effect water distillator, it is characterized in that: mainly be made of internal screw multi-effect water distillator and the industrial steam system, water purification system, the condenser that are connected with the internal screw multi-effect water distillator, described condenser also is connected with condensate system, described internal screw multi-effect water distillator is mainly by steam gravity separator (7), and the steam generation chamber (12) that is arranged on steam gravity separator (7) top, and the pure water vapour outlet (1) and the liquid water that are arranged on top, steam generation chamber (12) are imported and exported (2) formation, described steam generates in chamber (12) and also is provided with centrifugal steam separate chamber (11), described centrifugal steam separate chamber (11) is connected with steam gravity separator (7) conducting, described liquid water is imported and exported (2) and is connected with steam generation chamber (12) conducting, described pure water vapour outlet (1) is connected with centrifugal steam separate chamber (11) conducting, described pure water vapour outlet (1) is connected with condenser, and water purification system is imported and exported (2) with liquid water and is connected, and described industrial steam system and steam generate the inner conducting in chamber (12).
2. the system of heating up in a steamer of carrying based on the internal screw multi-effect water distillator according to claim 1, is characterized in that: be provided with two ends in described steam generation chamber (12) and be connected with steam gravity separator (7) generating tube (4) that (2) are connected with liquid water respectively.
3. the system of heating up in a steamer of carrying based on the internal screw multi-effect water distillator according to claim 1, is characterized in that: be provided with roughing out chamber (9) in described centrifugal steam separate chamber (11), be provided with undergauge helical cavity (6) in described roughing out chamber (9); The Huo of described centrifugal steam separate chamber (11) and roughing out chamber (9) Huo and undergauge helical cavity (6) have whirlwind mouth (5).
4. any one described system of heating up in a steamer of carrying based on the internal screw multi-effect water distillator according to claim 1-3, it is characterized in that: centrifugal steam separate chamber (11) is connected with steam gravity separator (7) by gravity water pipe (8).
5. any one described system of heating up in a steamer of carrying based on the internal screw multi-effect water distillator according to claim 1-3, it is characterized in that: described steam generates in chamber (12) and is full of high-temperature steam.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2012101727461A CN103130290A (en) | 2011-11-23 | 2012-05-30 | Stripping system based on internal screw multi-effect water distillatory |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201110376011 | 2011-11-23 | ||
CN201110376011.6 | 2011-11-23 | ||
CN2012101727461A CN103130290A (en) | 2011-11-23 | 2012-05-30 | Stripping system based on internal screw multi-effect water distillatory |
Publications (1)
Publication Number | Publication Date |
---|---|
CN103130290A true CN103130290A (en) | 2013-06-05 |
Family
ID=48490811
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2012101727461A Pending CN103130290A (en) | 2011-11-23 | 2012-05-30 | Stripping system based on internal screw multi-effect water distillatory |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103130290A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106608663A (en) * | 2016-10-17 | 2017-05-03 | 湘潭大学 | Electric multi-effect water distiller |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3499827A (en) * | 1967-04-12 | 1970-03-10 | Us Interior | Distillation plant |
CN2496529Y (en) * | 2001-07-18 | 2002-06-26 | 南松贵 | Evaporator water-steam three-stage separation apparatus of multiple-effect water-distilling machine |
CN2758240Y (en) * | 2004-11-14 | 2006-02-15 | 曲景春 | Electric multieffect distilled water machine |
CN1792827A (en) * | 2005-12-02 | 2006-06-28 | 宁波振国制药设备制造有限公司 | Vapor, water four-grade separating water distilling machine |
CN202558665U (en) * | 2012-05-30 | 2012-11-28 | 四川制药制剂有限公司 | Stripping system based on internal screw multi-effect water distiller |
-
2012
- 2012-05-30 CN CN2012101727461A patent/CN103130290A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3499827A (en) * | 1967-04-12 | 1970-03-10 | Us Interior | Distillation plant |
CN2496529Y (en) * | 2001-07-18 | 2002-06-26 | 南松贵 | Evaporator water-steam three-stage separation apparatus of multiple-effect water-distilling machine |
CN2758240Y (en) * | 2004-11-14 | 2006-02-15 | 曲景春 | Electric multieffect distilled water machine |
CN1792827A (en) * | 2005-12-02 | 2006-06-28 | 宁波振国制药设备制造有限公司 | Vapor, water four-grade separating water distilling machine |
CN202558665U (en) * | 2012-05-30 | 2012-11-28 | 四川制药制剂有限公司 | Stripping system based on internal screw multi-effect water distiller |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106608663A (en) * | 2016-10-17 | 2017-05-03 | 湘潭大学 | Electric multi-effect water distiller |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US11779858B2 (en) | Process and system for dehydrating a product stream in ethanol production | |
CN104926676B (en) | A kind of solvent recovering system of low concentration DMF brine waste | |
CN104961783A (en) | Method for effectively extracting anthocyanidin and anthocyanin | |
JP2005536710A (en) | Method and apparatus for producing clean steam | |
CN205528218U (en) | One imitates useless water separator of limbs MVR mixed salt | |
CN202558665U (en) | Stripping system based on internal screw multi-effect water distiller | |
CN103130290A (en) | Stripping system based on internal screw multi-effect water distillatory | |
CN202440336U (en) | Internally-spiral multi-effect water distillator | |
CN208097426U (en) | A kind of sodium aluminate solution mixing concentration systems | |
CN2496529Y (en) | Evaporator water-steam three-stage separation apparatus of multiple-effect water-distilling machine | |
CN203823716U (en) | Four-step type liquid droplet separating device | |
CN104045519B (en) | High-purity Delta terpilenol separation and purification method | |
CN206910972U (en) | A kind of double-screw type pure steam separator | |
WO2016088134A2 (en) | Integrated ethanol separation and vinasse/ slop concentration using mechanical vapour recompression | |
CN203990963U (en) | A kind of cyclone separator | |
CN207980454U (en) | A kind of production potassium nitrate multi-effect evaporating device | |
CN107162297A (en) | One kind one imitates four body MVR mixed salts waste water separators and separation method | |
CN206295623U (en) | A kind of ethanol distillation purifying plant | |
CN203683159U (en) | Medicinal tubular multi-effect water distillator | |
CN102942452B (en) | Preparation method of natural borneol | |
CN1046723A (en) | Efficient distilled water production technique and device | |
CN207734632U (en) | Device for recovering tail gas | |
CN100395190C (en) | Method and device for treating water | |
CN206172995U (en) | Device that pure lithium chloride solution was prepared to sodium is analysed in evaporation of lithium chloride sodium chloride mixing water solution | |
CN206027147U (en) | Installation hydrocyclone's MVR crystallizer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C12 | Rejection of a patent application after its publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20130605 |