CN201519474U - External circulating evaporator - Google Patents
External circulating evaporator Download PDFInfo
- Publication number
- CN201519474U CN201519474U CN2009202101904U CN200920210190U CN201519474U CN 201519474 U CN201519474 U CN 201519474U CN 2009202101904 U CN2009202101904 U CN 2009202101904U CN 200920210190 U CN200920210190 U CN 200920210190U CN 201519474 U CN201519474 U CN 201519474U
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- CN
- China
- Prior art keywords
- pipeline
- pump
- heater
- circulation type
- inner bag
- 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
- 239000000463 material Substances 0.000 claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 238000009834 vaporization Methods 0.000 claims description 19
- 230000008016 vaporization Effects 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 238000007599 discharging Methods 0.000 claims description 8
- 230000008020 evaporation Effects 0.000 abstract 5
- 238000001704 evaporation Methods 0.000 abstract 5
- 239000011344 liquid material Substances 0.000 description 4
- 238000004821 distillation Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000021715 photosynthesis, light harvesting Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to an external circulating evaporator. The external circulating evaporator comprises vapor generating equipment, a material temporary storage tank, an evaporation chamber and a heater; an inner container is arranged in the heater; the inner container of the heater is communicated with the side wall of the evaporation chamber through a first pipeline; the material temporary storage tank is communicated with the first pipeline through a feed pump and a feed pipeline; the bottom of the inner container of the heater is connected with a storage tank through a discharge rotor pump and a discharge pipeline; the side wall of the inner container of the heater and the bottom of the evaporation chamber are connected with an evaporation circulating pump through a second pipeline and a third pipeline respectively; the top part of the evaporation chamber is connected with a condenser through a fourth pipeline; and the bottom of the condenser is communicated with a gas-liquid buffer tank through a fifth pipeline. The utility model utilizes two sets of circulating systems and can carry out continuous operation, thereby saving manpower and material resources, and can fully utilize heat quantity.
Description
Technical field
The utility model relates to a kind of evaporimeter, particularly a kind of outer circulation type evaporimeter.
Background technology
In food production and medicine process, the distillation of fluid or processed often will be with the material batch processings, and can not handle continuously.Such distillation equipment troublesome poeration, energy dissipation is serious, can not work continuously, and operating efficiency is low.
The utility model content
The purpose of this utility model provides a kind of outer circulation type evaporimeter, can effectively solve serious, the inferior problem of inefficiency of troublesome poeration, energy dissipation that prior art exists.The utility model relates to a kind of outer circulation type evaporimeter, comprise steam generating equipment, temporary jar of material, vaporization chamber and heater, be provided with inner bag in the described heater, described heater inner bag is communicated with the sidewall of vaporization chamber by first pipeline, the temporary jar of material passes through feed pump, feed pipe is connected with first pipeline, the bottom of described heater inner bag is by the discharging impeller pump, discharge pipe is connected with holding vessel, the sidewall of described heater inner bag is connected with the vaporization cycle pump with the 3rd pipeline by second pipeline respectively with the bottom of vaporization chamber, described vaporization chamber top is connected with condenser by the 4th pipeline, the condenser bottom is communicated with the gas-liquid surge tank by the 5th pipeline, the top of gas-liquid surge tank is connected with vavuum pump, the bottom of gas-liquid surge tank is connected with the condensed water suction pump, the condenser bottom is connected with the indirect steam condensate pump, described steam generating equipment passes through steam channel, heat pump is connected with the outer wall of heater, the air admission hole of described heat pump is connected with the 4th pipeline by the 6th pipeline, and described heater outer wall is connected with the 4th pipeline by the 7th pipeline.Be provided with vapor filter, Pressure gauge, control valve and stop valve on the steam channel between described steam generating equipment and the heat pump successively.Described feed pipe is provided with the charging switch, and described discharge pipe is provided with the discharging switch, and described the 7th pipeline is provided with control valve.The utility model utilizes the two cover circulatory systems, can work continuously, and uses manpower and material resources sparingly, and can make full use of heat.
Description of drawings
Accompanying drawing 1 is a structural representation of the present utility model.
The specific embodiment
Comprise steam generating equipment 1, temporary jar 2 of material, vaporization chamber 3 and heater 4 among the figure, be provided with inner bag 5 in the described heater 4, described heater inner bag 5 is communicated with the sidewall of vaporization chamber 3 by first pipeline 6, temporary jar 2 of material is connected with first pipeline 6 by feed pump 7, feed pipe 8, the bottom of described heater inner bag 5 is connected with holding vessel 11 by discharging impeller pump 9, discharge pipe 10, and the bottom of the sidewall of described heater inner bag 5 and vaporization chamber 3 is connected with vaporization cycle pump 14 with the 3rd pipeline 13 by second pipeline 12 respectively.First pipeline 6, heater 4, second pipeline 12, vaporization cycle pump 14, the 3rd pipeline 13, vaporization chamber 3 form one for the hydronic circular passage of material.
Described feed pipe 8 is provided with charging switch 15, described discharge pipe 10 is provided with discharging switch 16, after the utility model starts, at first open charging switch 15 and close discharging switch 16, liquid material in the temporary jar 2 of material enters first pipeline 6 by feed pipe 8 under the effect of feed pump 7, and one after another by heater 4 heating.
Described vaporization chamber 3 tops are connected with condenser 18 by the 4th pipeline 17, the condenser bottom is communicated with gas-liquid surge tank 20 by the 5th pipeline 19, the top of gas-liquid surge tank 20 is connected with vavuum pump 21, the bottom of gas-liquid surge tank 20 is connected with condensed water suction pump 22, and condenser 18 bottoms are connected with indirect steam condensate pump 23.In the utility model work, vavuum pump 21 continuous operations make gas flow condenser 18 and gas-liquid surge tank 20 in the vaporization chamber.Liquid material after the heating evaporates a large amount of steam in vaporization chamber, steam flows to condenser 18 with hot-air by four-way 17, liquefy water flows out through indirect steam condensate pump 23 behind a large amount of water vapor condensations, a small amount of water vapor and hot-air flow into gas-liquid surge tank 20, steam liquefaction is after by 22 outflows of condensed water suction pump, hot-air is discharged through vavuum pump 21.
Described steam generating equipment 1 is connected with the outer wall of heater 4 by steam channel 24, heat pump 25.Described heater 4 outer walls are connected with the 4th pipeline 17 by the 7th pipeline 26, and described the 7th pipeline 26 is provided with control valve 27.
Under the normal condition, control valve 27 cuts out, and heat pump 25 pushes heater 4 with steam, in heater 4, liquid material in high-temperature water vapor and the inner bag 5 carries out heat exchange, and liquid material is heated, and steam can flow out by indirect steam condensate pump 23 by liquefy water after finishing heat exchange.After heat exchange a period of time, residual water vapor can not satisfy the heat exchange demand, therefore, need open the control valve 28 on the steam channel 24, replenish high-temperature vapor to heater 4, open the control valve 27 on the 7th pipeline 26 simultaneously, it is unimpeded to guarantee that gas can flow.
The air admission hole of described heat pump 25 is connected with the 4th pipeline 17 by the 6th pipeline 29, and the vapours in the 4th pipeline 17 can be extracted out a part by heat pump 25 and be participated in heat exchange, reduces the waste of heat energy.
Be provided with vapor filter 30, pressure-reducing valve 31, Pressure gauge 32, safety valve 33, control valve 28 and stop valve 34 on the steam channel 24 between described steam generating equipment 1 and the heat pump 25 successively, vapor filter can prevent that impurity such as airborne dust from sneaking into, Pressure gauge 32 and control valve 28 are used, be used for controlling the input quantity of the high-temperature steam of whole utility model, pressure-reducing valve 31 and safety valve 33 are used, can be used for discharging too much steam, the control steam generating amount, stop valve is used for steam off, prevents that steam input is out of control and causes production accident.
Claims (5)
1. outer circulation type evaporimeter, comprise steam generating equipment, temporary jar of material, vaporization chamber and heater, it is characterized in that: be provided with inner bag in the described heater, described heater inner bag is communicated with the sidewall of vaporization chamber by first pipeline, the temporary jar of material passes through feed pump, feed pipe is connected with first pipeline, the bottom of described heater inner bag is by the discharging impeller pump, discharge pipe is connected with holding vessel, the sidewall of described heater inner bag is connected with the vaporization cycle pump with the 3rd pipeline by second pipeline respectively with the bottom of vaporization chamber, described vaporization chamber top is connected with condenser by the 4th pipeline, the condenser bottom is communicated with the gas-liquid surge tank by the 5th pipeline, the top of gas-liquid surge tank is connected with vavuum pump, the bottom of gas-liquid surge tank is connected with the condensed water suction pump, the condenser bottom is connected with the indirect steam condensate pump, described steam generating equipment passes through steam channel, heat pump is connected with the outer wall of heater, the air admission hole of described heat pump is connected with the 4th pipeline by the 6th pipeline, and described heater outer wall is connected with the 4th pipeline by the 7th pipeline.
2. outer circulation type evaporimeter as claimed in claim 1 is characterized in that: be provided with vapor filter, Pressure gauge, control valve and stop valve on the steam channel between described steam generating equipment and the heat pump successively.
3. outer circulation type evaporimeter as claimed in claim 1 is characterized in that: described feed pipe is provided with the charging switch.
4. outer circulation type evaporimeter as claimed in claim 1 is characterized in that: described discharge pipe is provided with the discharging switch.
5. outer circulation type evaporimeter as claimed in claim 1 is characterized in that: described the 7th pipeline is provided with control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202101904U CN201519474U (en) | 2009-09-25 | 2009-09-25 | External circulating evaporator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202101904U CN201519474U (en) | 2009-09-25 | 2009-09-25 | External circulating evaporator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201519474U true CN201519474U (en) | 2010-07-07 |
Family
ID=42505653
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202101904U Expired - Fee Related CN201519474U (en) | 2009-09-25 | 2009-09-25 | External circulating evaporator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201519474U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101966396A (en) * | 2010-09-21 | 2011-02-09 | 广州市心德实业有限公司 | Evaporation device |
| CN103505895A (en) * | 2012-06-15 | 2014-01-15 | 苏州市金翔钛设备有限公司 | Outer circulation condensation device |
| CN103505891A (en) * | 2012-06-15 | 2014-01-15 | 苏州市金翔钛设备有限公司 | Evaporator |
| CN103537104A (en) * | 2013-10-25 | 2014-01-29 | 昆山市盛兴设备安装有限公司 | Fructose-glucose syrup evaporating system |
| CN109731358A (en) * | 2019-02-15 | 2019-05-10 | 陕西陕化煤化工集团有限公司 | A kind of evaporation concentration system |
-
2009
- 2009-09-25 CN CN2009202101904U patent/CN201519474U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101966396A (en) * | 2010-09-21 | 2011-02-09 | 广州市心德实业有限公司 | Evaporation device |
| CN101966396B (en) * | 2010-09-21 | 2012-07-25 | 广州市心德实业有限公司 | Evaporation device |
| CN103505895A (en) * | 2012-06-15 | 2014-01-15 | 苏州市金翔钛设备有限公司 | Outer circulation condensation device |
| CN103505891A (en) * | 2012-06-15 | 2014-01-15 | 苏州市金翔钛设备有限公司 | Evaporator |
| CN103537104A (en) * | 2013-10-25 | 2014-01-29 | 昆山市盛兴设备安装有限公司 | Fructose-glucose syrup evaporating system |
| CN109731358A (en) * | 2019-02-15 | 2019-05-10 | 陕西陕化煤化工集团有限公司 | A kind of evaporation concentration system |
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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: 20100707 Termination date: 20140925 |
|
| EXPY | Termination of patent right or utility model |