CN2705219Y - Double section type screen separating evaporator - Google Patents
Double section type screen separating evaporator Download PDFInfo
- Publication number
- CN2705219Y CN2705219Y CN 200420040649 CN200420040649U CN2705219Y CN 2705219 Y CN2705219 Y CN 2705219Y CN 200420040649 CN200420040649 CN 200420040649 CN 200420040649 U CN200420040649 U CN 200420040649U CN 2705219 Y CN2705219 Y CN 2705219Y
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- water
- section
- carbonated drink
- evaporator
- steam
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Abstract
A kind of two section type silk screen separating evaporator relates to water distillation equipment field.Comprise vaporiser body and the tubulation that matches, the turnover mouth of pipe, it is characterized in that vaporiser body is made up of the evaporator section (3) on top and the carbonated drink segregation section (8) of bottom, the bottom of evaporator section (3) is evaporation tubulation group (4), top is cloth water chamber (13), water inlet pipe (10) is set in the cloth water chamber (13), this water inlet pipe (10) runs through evaporator section (3) and carbonated drink segregation section (8) downwards, water inlet pipe mouth is visited the outside that reaches carbonated drink segregation section (8), in the carbonated drink segregation section (8) steam-water separator (7) is set in addition.The utility model exposes pipeline owing to having shortened, and not only reduces scattering and disappearing of heat, also can raw water is preheated, and improves the utilization rate of heat.
Description
Technical field
The utility model relates to water distillation equipment field, specifically is a kind of two section type silk screen separating evaporator.
Background technology
At present, the equipment of producing medical distilled water generally adopts multi-effect water distillator.This distillation machine is serially connected by multi-effect evaporator, its structure of evaporimeter that the prior art distillation machine adopts mostly is external inlet channel, and evaporimeter is the top water inlet, like this when each single-effect evaporator connects successively, because its water inlet pipe mouth is at the top of evaporimeter, the water inlet pipe of each single-effect evaporator all prolongs on the bottom to the top, must will extending so make use of momentum, each exposes tube side at the water inlet pipe of device external, the device external pipeline is barish many more, scattering and disappearing of heat is just big more, the utilization rate of heat is just low more, the most directly cause the reduction greatly of energy waste and distilled water productive rate, how can solve similar problem, to become industry technical staff's a problem.
The utility model content
The purpose of this utility model is to overcome above-mentioned deficiency of the prior art, and provide a kind of and shortened the equipment tube side of exposed pipeline outward, and simple and compact for structure, heat utilization ratio height, the two section type silk screen separating evaporator that the distilled water yield is high.
The utility model is achieved through the following technical solutions:
It is a kind of two section type silk screen separating evaporator, comprise vaporiser body and the tubulation that matches, the turnover mouth of pipe, it is characterized in that vaporiser body is made up of the evaporator section 3 on top and the carbonated drink segregation section 8 of bottom, the bottom of evaporator section 3 is evaporation tubulation group 4, and top is cloth water chamber 13, water inlet pipe 10 is set in the cloth water chamber 13, this water inlet pipe 10 runs through evaporator section 3 and carbonated drink segregation section 8 downwards, and water inlet pipe mouth is visited the outside that reaches carbonated drink segregation section 8, in the carbonated drink segregation section 8 steam-water separator 7 is set in addition.
Described water inlet pipe 10 is positioned at the center of vaporiser body, and its top can be higher than water distributing plate 1 upper surface of each tubulation group 4 top.For making water distribution even, also the water distributing plate 1 that all plants the water through hole can be set in the bottom in the cloth water chamber 13.
The steam-water separator 7 that is provided with in the described carbonated drink segregation section 8 is a funnel-shaped structure, the top of steam-water separator 7 is positioned at the below of evaporation tubulation group 4, constitute steam-water separation chamber between the intracavity bottom of the bottom of steam-water separator 7 and carbonated drink segregation section 8, in carbonated drink segregation section 8 inner chambers of ring steam-water separator 7 outer wall bottoms carbonated drink separate mesh 9 is set, after the high temperature steam water interface carries out first separation in steam-water separation chamber like this, high-temperature steam is quilt carbonated drink separation once more through carbonated drink separate mesh 9 time, steam after separating is once more discharged along indirect steam outlet 6, and raw material coagulates water and then discharges from raw water outlet 11.
The utility model is owing to make water inlet pipe enter vaporiser body from the bottom, not only shortened the equipment tube side of exposed pipeline outward, reduced scattering and disappearing of heat, also can raw water has been preheated, improve the utilization rate of heat, so can finally improve producing effects of distilled water greatly.
Description of drawings
Below in conjunction with Figure of description the utility model is described in further detail:
Fig. 1: the utility model embodiment 1 structural representation.
The specific embodiment
Before use, the utility model shown in Figure 1 can be used according to the connecting mode multiple-effect series connection of prior art, to improve the production efficiency of distilled water.
In use, throw hot industry steam by air intake 12 into in the evaporation cavity 2 of first evaporator evaporator section 3, the industrial steam of high temperature heats up for tubulation group 4 Fast Heating in the evaporator section 3, raw water enters into cloth water chamber 13 through the water inlet pipe 10 of vaporiser body bottom simultaneously, raw water is evaporated the high-temperature steam preheating in the body in up along water inlet pipe 10, like this at raw water after the water distribution through hole of water distributing plate 1 flows down, accelerated raw water vaporization rate in the unit interval in tubulation group 4, the steam water interface of the raw water after being vaporized is discharged from the bottom of tubulation group 4, and enter the steam-water separation chamber of carbonated drink segregation section 8 along steam-water separator 7, after steam water interface is separated in steam-water separation chamber for the first time, raw material water-setting water is discharged from raw water outlet 11, enter lower effective evaporator, follow-up each effect connects successively, clean distilled water steam is through carbonated drink separate mesh 9 after carbonated drink is separated once more, enter lower effective evaporator through indirect steam outlet 6 discharges, follow-up each single-effect evaporator connects successively, and condensed Industrial Boiler steam condensation water is discharged from floss hole 5.
The utility model is owing to make water inlet pipe enter vaporiser body from the bottom, not only shortened the equipment tube side of exposed pipeline outward, reduced scattering and disappearing of heat, also can raw water has been preheated, improve the utilization rate of heat, so can finally improve producing effects of distilled water greatly.
Claims (5)
1, a kind of two section type silk screen separating evaporator, comprise vaporiser body and the tubulation that matches, the turnover mouth of pipe, it is characterized in that vaporiser body is made up of the evaporator section (3) on top and the carbonated drink segregation section (8) of bottom, the bottom of evaporator section (3) is evaporation tubulation group (4), top is cloth water chamber (13), water inlet pipe (10) is set in the cloth water chamber (13), this water inlet pipe (10) runs through evaporator section (3) and carbonated drink segregation section (8) downwards, water inlet pipe mouth is visited the outside that reaches carbonated drink segregation section (8), in the carbonated drink segregation section (8) steam-water separator (7) is set in addition.
2, two section type silk screen separating evaporator according to claim 1 is characterized in that water inlet pipe (10) is positioned at the center of vaporiser body.
3, two section type silk screen separating evaporator according to claim 1 is characterized in that the bottom in the cloth water chamber (13) is provided with the water distributing plate (1) that all plants the water through hole.
4, two section type silk screen separating evaporator according to claim 1, it is characterized in that the steam-water separator (7) that is provided with in the carbonated drink segregation section (8) is a funnel-shaped structure, the top of steam-water separator (7) is positioned at the below of evaporation tubulation group (4), constitute steam-water separation chamber between the intracavity bottom of the bottom of steam-water separator (7) and carbonated drink segregation section (8), in carbonated drink segregation section (8) inner chamber of ring steam-water separator (7) outer wall bottom carbonated drink separate mesh (9) is set.
5,, it is characterized in that water inlet pipe (10) top of evaporator section (3) is higher than water distributing plate (1) upper surface of each tubulation group (4) top according to claim 1,2 described two section type silk screen separating evaporators.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420040649 CN2705219Y (en) | 2004-05-20 | 2004-05-20 | Double section type screen separating evaporator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420040649 CN2705219Y (en) | 2004-05-20 | 2004-05-20 | Double section type screen separating evaporator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2705219Y true CN2705219Y (en) | 2005-06-22 |
Family
ID=34850637
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200420040649 Expired - Fee Related CN2705219Y (en) | 2004-05-20 | 2004-05-20 | Double section type screen separating evaporator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2705219Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103223254A (en) * | 2013-02-01 | 2013-07-31 | 杨家华 | Solution concentrating apparatus |
| CN105327518A (en) * | 2014-08-12 | 2016-02-17 | 上海凯赛生物技术研发中心有限公司 | Pentanediamine concentration system and method thereof |
| CN111285422A (en) * | 2020-02-15 | 2020-06-16 | 青岛科技大学 | Integrated form MVR evaporation concentration device |
-
2004
- 2004-05-20 CN CN 200420040649 patent/CN2705219Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103223254A (en) * | 2013-02-01 | 2013-07-31 | 杨家华 | Solution concentrating apparatus |
| CN103223254B (en) * | 2013-02-01 | 2016-03-30 | 江苏河海新能源股份有限公司 | A kind of solution condensing device |
| CN105327518A (en) * | 2014-08-12 | 2016-02-17 | 上海凯赛生物技术研发中心有限公司 | Pentanediamine concentration system and method thereof |
| CN105327518B (en) * | 2014-08-12 | 2018-01-23 | 上海凯赛生物技术研发中心有限公司 | The concentration systems and method of a kind of pentanediamine |
| CN111285422A (en) * | 2020-02-15 | 2020-06-16 | 青岛科技大学 | Integrated form MVR evaporation concentration device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20050622 Termination date: 20130520 |