CN2463019Y - High-efficiency tower distilling apparatus - Google Patents
High-efficiency tower distilling apparatus Download PDFInfo
- Publication number
- CN2463019Y CN2463019Y CN 00261419 CN00261419U CN2463019Y CN 2463019 Y CN2463019 Y CN 2463019Y CN 00261419 CN00261419 CN 00261419 CN 00261419 U CN00261419 U CN 00261419U CN 2463019 Y CN2463019 Y CN 2463019Y
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- condenser
- utility
- pipe
- evaporator
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a high efficient tower type sub-boiling distilling device. An evaporator and a condenser adopt inwards concave opening types and are directly in a butt joint mode through a connecting piece, and a guide pipe is arranged between a distilling bottle and an outer part which is provided with a heat insulating and temperature regulating type heater. A condensing tank is arranged in the condenser on which a water inlet pipe and a water outlet pipe are arranged, and the bottom of the inner side of the condenser is provided with a liquid collecting tank communicated with a collecting pipe of the outer part. The utility model enlarges a steam passage so as to prevent evaporating liquid from flowing back and respectively heats the upper part and the lower part of the evaporator so as to thoroughly prevent the evaporating liquid from flowing upwards. The utility model enlarges the area of a condensing surface and enhances condensing efficiency. The evaporator and the condenser adopt the inwards concave opening types, so that people can sufficiently clean the evaporator and the condenser. The utility model adopts different types of condensing matter so as to ensure that evaporating matter can be sufficiently condensed, and has the advantages of simple structure, easy installation and small occupation area.
Description
The utility model relates to a kind of efficient tower type sub-boiling distillation device.
Distillation is a kind of method for preparing pure water comparatively commonly used, normally carries out under the situation of quilt steaming liquid boiling.And in order to improve the purity of product, usually adopt the method for sub-boiling distillation, promptly to distilling under the situation of not seethed with excitement by steaming liquid, owing to steamed not boiling of liquid, therefore not having bubble in by steaming liquid produces, steamed that liquid will can not produce like this because collapse of bubbles and situation in the form steam that drips with mist, thereby can be reduced the contained impurity of steam widely.But no matter seethe with excitement distillation or sub-boiling distillation, the distiller that is adopted in the dual mode all has common problem, be that its steam circulation is narrow, the condenser condenses area is less, it is serious to be repeated once more Evaporation Phenomenon after the backflow, make distillation efficiency lower, and, condenser and cucurbit inside are difficult to clean through after the long period use; No matter traditional distiller is which kind of is steamed liquid, all can only adopt the mode of water condensation, has limitation, and its condensation effect is subjected to bigger restriction.
The purpose of this utility model be to provide a kind of steam passages spaciousness, condensation area big, can avoid after the liquid evaporation backflow, can select condensed material, be convenient to clean, efficient tower type sub-boiling distillation device simple in structure.
The purpose of this utility model can realize by following measure:
A kind of efficient lid formula distilling apparatus comprises evaporimeter and condenser, and evaporimeter and condenser all adopt the indent open type and directly dock by connector, are provided with conduit between cucurbit and the outside, and the cucurbit outside is provided with the temp .-regulating type heater; Establish condensate tank(trap) in the condenser, condenser is provided with water inlet pipe, and top is provided with outlet pipe, and the condenser inside bottom is provided with collecting tank, and collecting tank is connected with the collected outside pipe.
The purpose of this utility model can also realize by following measure:
The inlet place of described conduit is provided with and the corresponding overflow pipe of liquid level; Evaporimeter is provided with the thermowell of measuring the liquid evaporating temperature; The condenser outer surface is provided with heat-insulation layer; The condenser napex is provided with openable spiral cover and links to each other with outlet pipe.
The utility model has following advantage compared to existing technology:
The utility model condenser directly docks with evaporimeter, vapor stream leads to the same size of bore with evaporimeter, has increased steam passages, has reduced the backflow that adds of condensed fluid, be to evaporimeter separately heating of two parts up and down, thoroughly avoided swashing of vapour liq; Increase the condensing surface area, improved condensation efficiency; Evaporimeter and condenser are open type, therefore can clean fully both; Can adopt dissimilar condensed materials according to the characteristics that are distilled liquid, guarantee evaporated material condensation fully; Adopted muff heater, can prevent too much the scattering and disappearing of heat in the heating process, raised the efficiency, the utility model is simple in structure, installs easily, and floor space is little.
Structure of the present utility model is provided by accompanying drawing:
1-cucurbit 2-conduit 3-temp .-regulating type heater 4-overfall 5-inlet
6-temp .-regulating type heater 7-collecting pipe 8-collecting tank 9-heat-insulation layer 10-condensate tank(trap)
11-outlet pipe 12-spiral cover 13-connector 14-water inlet pipe 15-thermowell
The utility model is also incited somebody to action in conjunction with the accompanying drawings, and embodiment is described in further detail:
A kind of efficient tower type sub-boiling distillation device, comprise evaporimeter and condenser, evaporimeter and condenser all adopt the indent open type and directly dock by connector 13, are provided with conduit 2 between cucurbit 1 and the outside, and cucurbit 1 outside is provided with insulation temp .-regulating type heater 3,6; Establish condensate tank(trap) 10 in the condenser, water inlet pipe 14 and outlet pipe 11 lay respectively at condenser and top, and the condenser inside bottom is provided with collecting tank 8, collecting tank 8 is connected with collected outside pipe 7, inlet 5 places of conduit 2 are provided with and the corresponding overflow pipe 4 of liquid level, evaporimeter is provided with the thermowell 15 of measuring the liquid level temperature, and the condenser outer surface is provided with heat-insulation layer 9, and condenser overhead is provided with openable spiral cover 12 and links to each other with outlet pipe 11.
The course of work of the utility model is as follows:
The utility model is when work, evaporating liquid is added in the cucurbit 1 to liquid level by conduit 2 from inlet 5, open and regulate insulation temp .-regulating type heater 3,6, under normal conditions, the temperature of temp .-regulating type heater 6 is higher than the temperature of temp .-regulating type heater 3, thereby to keep distiller top inwall to be drying regime, prevent to be evaporated liquid and climb the notes condenser by inwall, liquid is evaporated to steam in the vaporization chamber II, after steam rises to condenser, effect owing to condensation in the condensation chamber I will be flowed back to collecting tank 8 by the condenser inwall, again by confluxing into collecting pipe 7.Constantly evaporate along with being evaporated liquid, can replenish from the inlet 5 of conduit 2 and add, and by set overflow pipe 4 controls and keep inner liquid level stabilizing, the temperature of liquid can be measured demonstration by the thermometer in the thermowell 15.The utility model can be selected dissimilar condensation speciality according to being distilled the liquid characteristics, when for example needing solid-state condensate ice or dry ice sometimes, can open spiral cover and add condensation chamber and get final product, at this moment with condensation flow to mutually; Evaporating liquid adopts the heater heating that separates up and down, can regulate heating-up temperature, according to select to make liquid boil situation in boiling or Asia under evaporation use, can also be used to carrying out experimental study to vapor phase.
Claims (5)
1, a kind of efficient tower type sub-boiling distillation device, comprise evaporimeter and condenser, it is characterized in that evaporimeter and condenser all adopt the indent open type and pass through directly butt joint of connector (13), be provided with conduit (2) between cucurbit (1) and the outside, cucurbit (1) outside is provided with insulation temp .-regulating type heater (3), (6); Establish condensate tank(trap) (10) in the condenser, condenser is provided with water inlet pipe (14), and top is provided with outlet pipe (11), and the condenser inside bottom is provided with collecting tank (8), and collecting tank (8) is connected with collected outside pipe (7).
2, efficient tower type sub-boiling distillation device as claimed in claim 1 is characterized in that the inlet (5) of conduit (2) is located to be provided with and the corresponding overflow pipe of liquid level (4).
3, efficient tower type sub-boiling distillation device as claimed in claim 1 is characterized in that evaporimeter is provided with the thermowell (15) of measuring the liquid surface evaporating temperature.
4, efficient tower type sub-boiling distillation device as claimed in claim 1 is characterized in that the condenser outer surface is provided with heat-insulation layer (9).
5, efficient tower type sub-boiling distillation device as claimed in claim 1 is characterized in that condenser overhead is provided with openable spiral cover (12) and links to each other with outlet pipe (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00261419 CN2463019Y (en) | 2000-12-08 | 2000-12-08 | High-efficiency tower distilling apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00261419 CN2463019Y (en) | 2000-12-08 | 2000-12-08 | High-efficiency tower distilling apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2463019Y true CN2463019Y (en) | 2001-12-05 |
Family
ID=33616933
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00261419 Expired - Fee Related CN2463019Y (en) | 2000-12-08 | 2000-12-08 | High-efficiency tower distilling apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2463019Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102465209A (en) * | 2010-11-02 | 2012-05-23 | 北京有色金属研究总院 | Method and vacuum distillation device for preparing high-purity neodymium |
| CN103143184A (en) * | 2013-02-07 | 2013-06-12 | 中国科学院上海应用物理研究所 | Distillation apparatus |
| CN106892473A (en) * | 2017-03-23 | 2017-06-27 | 重庆大学 | A kind of geothermal energy fresh water preparation system and geothermal energy fresh water preparation method |
| CN114292720A (en) * | 2021-12-21 | 2022-04-08 | 孝感麻糖米酒有限责任公司 | Rice wine production is with high-efficient boiling device |
| CN116199292A (en) * | 2023-04-20 | 2023-06-02 | 桂林理工大学 | Surface super-hydrophilic modified sea water desalinator |
-
2000
- 2000-12-08 CN CN 00261419 patent/CN2463019Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102465209A (en) * | 2010-11-02 | 2012-05-23 | 北京有色金属研究总院 | Method and vacuum distillation device for preparing high-purity neodymium |
| CN102465209B (en) * | 2010-11-02 | 2014-08-27 | 有研稀土新材料股份有限公司 | Method and vacuum distillation device for preparing high-purity neodymium |
| CN103143184A (en) * | 2013-02-07 | 2013-06-12 | 中国科学院上海应用物理研究所 | Distillation apparatus |
| CN103143184B (en) * | 2013-02-07 | 2014-12-24 | 中国科学院上海应用物理研究所 | Distillation apparatus |
| CN106892473A (en) * | 2017-03-23 | 2017-06-27 | 重庆大学 | A kind of geothermal energy fresh water preparation system and geothermal energy fresh water preparation method |
| CN114292720A (en) * | 2021-12-21 | 2022-04-08 | 孝感麻糖米酒有限责任公司 | Rice wine production is with high-efficient boiling device |
| CN116199292A (en) * | 2023-04-20 | 2023-06-02 | 桂林理工大学 | Surface super-hydrophilic modified sea water desalinator |
| CN116199292B (en) * | 2023-04-20 | 2024-05-28 | 桂林理工大学 | Surface super-hydrophilic modified sea water desalinator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |