CN207187150U - A kind of energy-saving distillation recovery device - Google Patents
A kind of energy-saving distillation recovery device Download PDFInfo
- Publication number
- CN207187150U CN207187150U CN201720075352.2U CN201720075352U CN207187150U CN 207187150 U CN207187150 U CN 207187150U CN 201720075352 U CN201720075352 U CN 201720075352U CN 207187150 U CN207187150 U CN 207187150U
- Authority
- CN
- China
- Prior art keywords
- steam
- distilled
- waste heat
- distillation
- energy
- 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
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a kind of energy-saving distillation recovery device, including distillation still, condenser and waste heat using device, the waste heat using device includes steam channel inner tube, the outside of steam channel inner tube, which is provided with, preheats liquid outer tube to be distilled, the steam channel inner tube both ends are respectively steam inlet and steam (vapor) outlet, and the preheating liquid outer tube side wall to be distilled is provided with liquid import to be distilled and liquid to be distilled exports；The distillation still connects the steam inlet of waste heat using device by pipeline one, and the steam (vapor) outlet of the waste heat using device connects condenser by pipeline two.The utility model compared with prior art the advantages of be：The utility model can be applicable all systems that separated is carried out by boiling point different solutions, and by cold and hot exchange, energy is fully utilized so that distillation warm-up time shortens, condensing gas temperature reduction, hence it is evident that can lift the efficiency of distillation recovery.Take this mode that distillation efficiency can be made to lift 5%, the energy reduces by 8% or so.
Description
Technical field
It the utility model is related to residual heat using device, more particularly to a kind of energy-saving distillation recovery device.
Background technology
Former Distallation systm does not install waste heat using device additional so that cannot cool down into the steam before condenser, enter simultaneously
The mixed liquor of distillation still cannot preheat so that energy is not fully utilized, it is impossible to improve the efficiency of cleaning distillation, waste one
A little energy resource consumptions.
Utility model content
The utility model is to solve above-mentioned deficiency, there is provided a kind of energy-saving distillation recovery device.
Above-mentioned purpose of the present utility model is realized by following technical scheme：A kind of energy-saving distillation recovery device,
Including distillation still, condenser and waste heat using device, the waste heat using device includes steam channel inner tube, steam channel inner tube
Outside be provided with and preheat liquid outer tube to be distilled, the steam channel inner tube both ends are respectively steam inlet and steam (vapor) outlet,
The preheating liquid outer tube side wall to be distilled is provided with liquid import to be distilled and liquid to be distilled exports；The distillation still passes through pipeline one
The steam inlet of waste heat using device is connected, the steam (vapor) outlet of the waste heat using device connects condenser by pipeline two.
The diameter of the steam inlet is 2-4 times of steam (vapor) outlet diameter.
Waste heat using device of the present utility model causes steam from internal layer by the way that the liquid with distillation is from outer layer by one
High temperature, one is low temperature, will carry out cold and hot exchange, reduces the temperature of steam, lifts the temperature of liquid to be distilled.
The utility model compared with prior art the advantages of be：The utility model can be applicable all by boiling point different solutions
The system for carrying out separated, by cold and hot exchange, energy is fully utilized so that distillation warm-up time shortens, condensation
Gas temperature reduces, hence it is evident that can lift the efficiency of distillation recovery.Take this mode that distillation efficiency can be made to lift 5%, energy drop
Low 8% or so.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation of waste heat using device in the utility model.
Embodiment
The utility model is described in further detail below in conjunction with the accompanying drawings.
As shown in Figure 1 and Figure 2, a kind of energy-saving distillation recovery device, including distillation still 1, condenser 2 and waste heat using device
3, the waste heat using device 3 includes steam channel inner tube 3-1, and steam channel inner tube 3-1 outside is to be distilled provided with preheating
Liquid outer tube 3-2, the steam channel inner tube 3-1 both ends are respectively steam inlet 3-3 and steam (vapor) outlet 3-4, the preheating
Liquid outer tube 3-2 side walls to be distilled are provided with liquid import 3-5 to be distilled and liquid to be distilled outlet 3-6；The distillation still 1 passes through pipeline
The steam inlet 3-3 of one 4 connection waste heat using devices 3, the steam (vapor) outlet 3-4 of the waste heat using device 3 are connected by pipeline 25
Condenser 2.
The diameter of the steam inlet 3-3 is 2-4 times of steam (vapor) outlet 3-4 diameters.
Waste heat using device of the present utility model causes steam from internal layer by the way that the liquid with distillation is from outer layer by one
High temperature, one is low temperature, will carry out cold and hot exchange, reduces the temperature of steam, lifts the temperature of liquid to be distilled.
Embodiment of the present utility model is the foregoing is only, not thereby limits the scope of the claims of the present utility model, it is every
The equivalent structure or equivalent flow conversion made using the utility model specification and accompanying drawing content, or be directly or indirectly used in
Other related technical areas, similarly it is included in scope of patent protection of the present utility model.
Claims (2)
- A kind of 1. energy-saving distillation recovery device, it is characterised in that：It is described remaining including distillation still, condenser and waste heat using device Heat utilization device includes steam channel inner tube, and the outside of steam channel inner tube, which is provided with, preheats liquid outer tube to be distilled, the steaming Vapour passage inner tube both ends are respectively steam inlet and steam (vapor) outlet, and the preheating liquid outer tube side wall to be distilled is provided with to be distilled Liquid import and liquid to be distilled outlet；The distillation still connects the steam inlet of waste heat using device, the waste heat profit by pipeline one Condenser is connected by pipeline two with the steam (vapor) outlet of device.
- A kind of 2. energy-saving distillation recovery device according to claim 1, it is characterised in that：The diameter of the steam inlet It is 2-4 times of steam (vapor) outlet diameter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720075352.2U CN207187150U (en) | 2017-01-21 | 2017-01-21 | A kind of energy-saving distillation recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720075352.2U CN207187150U (en) | 2017-01-21 | 2017-01-21 | A kind of energy-saving distillation recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207187150U true CN207187150U (en) | 2018-04-06 |
Family
ID=61792318
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720075352.2U Expired - Fee Related CN207187150U (en) | 2017-01-21 | 2017-01-21 | A kind of energy-saving distillation recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207187150U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108704328A (en) * | 2018-06-01 | 2018-10-26 | 袁锟 | A kind of novel flash distillation device and its distillating method |
| CN109364508A (en) * | 2018-12-07 | 2019-02-22 | 威海天宇新材料科技有限公司 | A kind of energy saving and environment friendly distillation still |
| CN109966768A (en) * | 2019-05-28 | 2019-07-05 | 蓬莱禄昊化工机械有限公司 | A kind of separator for mixing liquid |
| CN112403012A (en) * | 2020-12-09 | 2021-02-26 | 安徽金禾实业股份有限公司 | Circulation accuse temperature formula molecular distillation equipment |
| CN114949897A (en) * | 2022-06-22 | 2022-08-30 | 安徽佳先功能助剂股份有限公司 | Continuous dehydration distillation plant of nylon acid diisobutyl ester |
| CN117264713A (en) * | 2023-11-22 | 2023-12-22 | 汕头市黄姥爷酒业有限责任公司 | Environment-friendly and efficient brewing device |
-
2017
- 2017-01-21 CN CN201720075352.2U patent/CN207187150U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108704328A (en) * | 2018-06-01 | 2018-10-26 | 袁锟 | A kind of novel flash distillation device and its distillating method |
| CN109364508A (en) * | 2018-12-07 | 2019-02-22 | 威海天宇新材料科技有限公司 | A kind of energy saving and environment friendly distillation still |
| CN109966768A (en) * | 2019-05-28 | 2019-07-05 | 蓬莱禄昊化工机械有限公司 | A kind of separator for mixing liquid |
| CN112403012A (en) * | 2020-12-09 | 2021-02-26 | 安徽金禾实业股份有限公司 | Circulation accuse temperature formula molecular distillation equipment |
| CN114949897A (en) * | 2022-06-22 | 2022-08-30 | 安徽佳先功能助剂股份有限公司 | Continuous dehydration distillation plant of nylon acid diisobutyl ester |
| CN117264713A (en) * | 2023-11-22 | 2023-12-22 | 汕头市黄姥爷酒业有限责任公司 | Environment-friendly and efficient brewing device |
| CN117264713B (en) * | 2023-11-22 | 2024-05-10 | 汕头市黄姥爷酒业有限责任公司 | Environment-friendly and efficient brewing device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN207187150U (en) | A kind of energy-saving distillation recovery device | |
| CN203904327U (en) | White liquor distilling apparatus | |
| CN206352906U (en) | A kind of exhaust steam direct-absorption type lithium bromide heat pump system | |
| CN106369866A (en) | Waste steam directly absorbed type double-effect lithium bromide heat pump system and working method thereof | |
| CN206310525U (en) | Wet desulphurization neat stress recuperative system | |
| CN104406143B (en) | A kind of vacuum compression high-temperature boiler and the method allowing steam heat up | |
| CN204665333U (en) | Smoke waste heat utilization system | |
| CN206832073U (en) | A kind of steam cooling recovery system | |
| CN202793091U (en) | Vapor condensed water one-effect flash utilization system of air heating coil device | |
| CN106120222B (en) | A kind of waste-heat recovery device of steaming silk system | |
| CN205980854U (en) | Adopt direct combustion formula to absorb bathroom waste heat recovery system of heat pump | |
| CN104653242A (en) | Waste heat recovery device for direct air-cooling unit | |
| CN203183716U (en) | Alcohol distillation device with heat recovery device | |
| CN208741956U (en) | Catalyst solution enrichment facility | |
| CN203842338U (en) | Heat gradient utilization device in methanol rectification process | |
| CN210069822U (en) | High-pressure high-temperature condensed water flash evaporation recovery system | |
| CN204176663U (en) | A kind of process waste reclaims energy conserving system | |
| CN105953424A (en) | Waste heat recovery and heat supply system for power plant | |
| CN208186318U (en) | Thick oil heat-collecting steam boiler device | |
| CN207850110U (en) | A kind of steam condensate recovering device | |
| CN105327520B (en) | Feeding and heating system of alcohol recovery tower | |
| CN207050490U (en) | A kind of ammonia vaporizer | |
| CN206257651U (en) | Oxygen-eliminating device discharged steam recovering device | |
| CN218130047U (en) | Rectifying tower with cooling and recycling functions for rectifying process | |
| CN202733867U (en) | Energy-saving heat-pump steam generation device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180406 Termination date: 20200121 |