CN202199132U - Coil condensation intermittent vacuum concentration evaporator - Google Patents
Coil condensation intermittent vacuum concentration evaporator Download PDFInfo
- Publication number
- CN202199132U CN202199132U CN2011202928971U CN201120292897U CN202199132U CN 202199132 U CN202199132 U CN 202199132U CN 2011202928971 U CN2011202928971 U CN 2011202928971U CN 201120292897 U CN201120292897 U CN 201120292897U CN 202199132 U CN202199132 U CN 202199132U
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- vacuum concentration
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- condenser
- concentration evaporator
- sterilizer
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Abstract
The utility model relates to the field of concentration equipment, in particular to an evaporator. A coil condensation intermittent vacuum concentration evaporator comprises an evaporator main body, wherein the evaporator main body comprises a heating chamber and a separation chamber connected with the heating chamber; a heating coil is arranged in the heating chamber; and a condenser is arranged at a secondary steam outlet of the separation chamber and is a coil condenser. By the evaporator, cooling water can be recycled, and water consumption is greatly reduced.
Description
Technical field
The utility model relates to the concentrator field, is specifically related to a kind of vacuum concentration evaporator.
Background technology
The vacuum concentration evaporator has a series of advantage to adopt under the negative pressure with the concentrated mode of lower temperature, and low like the feed liquid boiling point, the speed that concentrates is fast, is beneficial to the maintenance food nutrient composition, the characteristics that energy consumption is little.Yet as the nucleus equipment of system, the vacuum system of coil pipe condensation batch (-type) vacuum concentration evaporator adopts Water Jet Condenser to add the form of multistage water pump more, has the big shortcoming of power consumption.
The utility model content
The purpose of the utility model is, a kind of coil pipe condensation batch (-type) vacuum concentration evaporator is provided, and solves the problems of the technologies described above.
The technical problem that the utility model solved can adopt following technical scheme to realize:
Coil pipe condensation batch (-type) vacuum concentration evaporator; Comprise a vaporizer body; Said vaporizer body comprise heating clamber, with the separation chamber that said heating clamber is connected, it is characterized in that said heating clamber adopts heat(ing) coil; The exit of said separation chamber indirect steam is provided with condenser, and said condenser adopts coiled tube condenser.
Coiled tube condenser is indirect type cooling, and cooling water can cycle applications, greatly reduces the consumption of water.
The outlet of said condenser connects a water ring vacuum pump, and indirect steam is cooled to condensed water through coiled tube condenser, when being cooled to condensed water to indirect steam, emits incoagulable gas.Vacuum when working with maintenance equipment through the suction of water ring vacuum pump is carried out evaporation smoothly.
Comprise that also one is used for the sterilizer of kill bacteria, said sterilizer is positioned at the charging aperture place of said vaporizer body.Said sterilizer adopts the direct-type sterilizer.Directly pass to steam in the direct-type sterilizer employing material and heat, be difficult for producing coking, the sterilization temperature retention time is long.
Also comprise a heating control system, said vaporization chamber indirect steam exit is provided with a temperature sensor, and the signal output part of said temperature sensor connects said heating control system.Temperature through said heating control system steam regulation.The temperature sensor that said temperature sensor adopts RTD to process.
The top of said separation chamber is provided with the cleaning shower nozzle, and said cleaning shower nozzle connects an automatic flushing device, and said automatic flushing device connects an automatic program control system, controls lotion and hot water temperature automatically.
Said vaporizer body connects a switch board, and the control end of said heating control system, automatic program control system is positioned at said switch board, and said switch board is provided with Ethernet interface.
Said vaporizer body and material contact portion adopt stainless steel material to process.Said stainless steel adopts austenitic stainless steel.
Said vaporizer body also is provided with one and is used to observe the observation window of evaporation situation, the observation window that said observation window adopts heat resistant glass to process.
Beneficial effect: owing to adopted technique scheme, cooling water can cycle applications, greatly reduces the consumption of water.
Description of drawings
Fig. 1 is that the structure of the utility model connects sketch map.
The specific embodiment
For technological means, creation characteristic that the utility model is realized, reach purpose and be easy to understand with effect and understand, below in conjunction with the further elaboration the utility model of concrete diagram.
With reference to Fig. 1; Coil pipe condensation batch (-type) vacuum concentration evaporator; Comprise a vaporizer body, vaporizer body comprises heating clamber 1, the separation chamber 2 that is connected with heating clamber 1, and heating clamber 1 adopts heat(ing) coil; The exit of separation chamber's 2 indirect steams is provided with condenser 3, and condenser 3 adopts coiled tube condenser.Coiled tube condenser is indirect type cooling, and cooling water can cycle applications, greatly reduces the consumption of water.The outlet of condenser 3 connects a water ring vacuum pump, and indirect steam is cooled to condensed water through coiled tube condenser, when being cooled to condensed water to indirect steam, emits incoagulable gas.Vacuum when working with maintenance equipment through the suction of water ring vacuum pump is carried out evaporation smoothly.
Comprise that also one is used for the sterilizer of kill bacteria, sterilizer is positioned at the charging aperture place of vaporizer body.Sterilizer adopts the direct-type sterilizer.Directly pass to steam in the direct-type sterilizer employing material and heat, be difficult for producing coking, the sterilization temperature retention time is long.
Also comprise a heating control system, vaporization chamber indirect steam exit is provided with a temperature sensor, and the signal output part of temperature sensor connects heating control system.Temperature through the heating control system steam regulation.The temperature sensor that temperature sensor adopts RTD to process.The top of separation chamber 2 is provided with the cleaning shower nozzle, cleans shower nozzle and connects an automatic flushing device, and automatic flushing device connects an automatic program control system, controls lotion and hot water temperature automatically.Vaporizer body connects a switch board, and the control end of heating control system, automatic program control system is positioned at switch board, and switch board is provided with Ethernet interface.
Vaporizer body and material contact portion adopt stainless steel material to process.Stainless steel adopts austenitic stainless steel.Vaporizer body also is provided with one and is used to observe the observation window of evaporation situation, the observation window that observation window adopts heat resistant glass to process.
More than show and described basic principle of the utility model and the advantage of principal character and the utility model.The technical staff of the industry should understand; The utility model is not restricted to the described embodiments; The principle of describing in the foregoing description and the specification that the utility model just is described; Under the prerequisite that does not break away from the utility model spirit and scope, the utility model also has various changes and modifications, and these variations and improvement all fall in the utility model scope that requires protection.The utility model requires protection domain to be defined by appending claims and equivalent thereof.
Claims (5)
1. coil pipe condensation batch (-type) vacuum concentration evaporator; Comprise a vaporizer body; Said vaporizer body comprise heating clamber, with the separation chamber that said heating clamber is connected, it is characterized in that said heating clamber adopts heat(ing) coil; The exit of said separation chamber indirect steam is provided with condenser, and said condenser adopts coiled tube condenser.
2. coil pipe condensation batch (-type) vacuum concentration evaporator according to claim 1, it is characterized in that: the outlet of said condenser connects a water ring vacuum pump.
3. coil pipe condensation batch (-type) vacuum concentration evaporator according to claim 2, it is characterized in that: comprise that also one is used for the sterilizer of kill bacteria, said sterilizer is positioned at the charging aperture place of said vaporizer body; Said sterilizer adopts the direct-type sterilizer.
4. coil pipe condensation batch (-type) vacuum concentration evaporator according to claim 3; It is characterized in that: the top of said separation chamber is provided with the cleaning shower nozzle; Said cleaning shower nozzle connects an automatic flushing device, and said automatic flushing device connects an automatic program control system.
5. coil pipe condensation batch (-type) vacuum concentration evaporator according to claim 4, it is characterized in that: said vaporizer body connects a switch board, and said switch board is provided with Ethernet interface.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202928971U CN202199132U (en) | 2011-08-12 | 2011-08-12 | Coil condensation intermittent vacuum concentration evaporator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202928971U CN202199132U (en) | 2011-08-12 | 2011-08-12 | Coil condensation intermittent vacuum concentration evaporator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202199132U true CN202199132U (en) | 2012-04-25 |
Family
ID=45963270
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011202928971U Expired - Fee Related CN202199132U (en) | 2011-08-12 | 2011-08-12 | Coil condensation intermittent vacuum concentration evaporator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202199132U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104645657A (en) * | 2013-11-15 | 2015-05-27 | 嘉兴市南洋塑料化工有限公司 | System of reducing heating loss of methyl tetrahydrophthalic anhydride and method thereof |
| CN105413209A (en) * | 2015-12-30 | 2016-03-23 | 天津横天生物科技有限公司 | Efficient concentrator for powder production |
-
2011
- 2011-08-12 CN CN2011202928971U patent/CN202199132U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104645657A (en) * | 2013-11-15 | 2015-05-27 | 嘉兴市南洋塑料化工有限公司 | System of reducing heating loss of methyl tetrahydrophthalic anhydride and method thereof |
| CN105413209A (en) * | 2015-12-30 | 2016-03-23 | 天津横天生物科技有限公司 | Efficient concentrator for powder production |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120425 Termination date: 20140812 |
|
| EXPY | Termination of patent right or utility model |