CN2705220Y - Double section screw separating evaporator - Google Patents
Double section screw separating evaporator Download PDFInfo
- Publication number
- CN2705220Y CN2705220Y CN 200420040650 CN200420040650U CN2705220Y CN 2705220 Y CN2705220 Y CN 2705220Y CN 200420040650 CN200420040650 CN 200420040650 CN 200420040650 U CN200420040650 U CN 200420040650U CN 2705220 Y CN2705220 Y CN 2705220Y
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- CN
- China
- Prior art keywords
- water
- section
- carbonated drink
- steam
- inlet pipe
- 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 - Lifetime
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Abstract
A kind of two section type spiral separation evaporimeter relates to water distillation equipment field.Comprise vaporiser body, the tubulation that matches and the turnover mouth of pipe, the top that it is characterized in that vaporiser body is that evaporator section (3), bottom are carbonated drink segregation section (10), the bottom of evaporator section (3) is evaporation tubulation group (4), top is cloth water chamber (17), water inlet pipe (2) is set in the cloth water chamber (17), this water inlet pipe (2) runs through evaporator section (3) and carbonated drink segregation section (10) downwards, water inlet pipe mouth is visited the outside that reaches carbonated drink segregation section (10), in the carbonated drink segregation section (10) steam-water separator (7) is set in addition.The utility model has not only shortened the equipment tube side of exposed pipeline outward, has reduced scattering and disappearing of heat, and raw water also can be preheated in vaporiser body in addition, 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 spiral separation evaporimeter.
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, provides a kind of simple and compact for structure, heat utilization ratio height, the two section type spiral separation evaporimeter 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 spiral separation evaporimeter, comprise vaporiser body, the tubulation that matches and the turnover mouth of pipe, the top that it is characterized in that vaporiser body is that evaporator section 3, bottom are carbonated drink segregation section 10, and the bottom of evaporator section 3 is evaporation tubulation group 4, and top is cloth water chamber 17, water inlet pipe 2 is set in the cloth water chamber 17, this water inlet pipe 2 runs through evaporator section 3 and carbonated drink segregation section 10 downwards, and water inlet pipe mouth is visited the outside that reaches carbonated drink segregation section 10, in the carbonated drink segregation section 10 steam-water separator 7 is set in addition.
Described water inlet pipe 2 is positioned at the center of vaporiser body.For making the raw water water distribution even, the water distributing plate 1 that all plants the water through hole can be set in the bottom in the cloth water chamber 17.
The steam-water separator 7 that is provided with in the described carbonated drink segregation section 10 is a funnel-shaped structure, ring steam-water separator 7 outer setting spiral separators 15, the top of steam-water separator 7 is positioned at the below of evaporation tubulation group 4, constitute steam-water separation chamber 13 between the intracavity bottom of bottom and carbonated drink segregation section 10, the carbonated drink cylinder 9 of the uniform through hole that the carbonated drink segregation section 10 inwall settings of corresponding steam-water separator 7 match, leave the water outlet opening between the bottom of carbonated drink cylinder 9 and carbonated drink segregation section 10 inwalls, and the bottom between carbonated drink cylinder 9 and steam-water separator 7 is provided with carbonated drink separate mesh 9, the section of this carbonated drink cylinder (9) can be trapezium structure, also can be other structure.
For guaranteeing the mobile smooth and easy of raw water, can make water inlet pipe 2 tops of evaporator section 3 be higher than water distributing plate 1 upper surface of each tubulation group 4 top.
The utility model is owing to make water inlet pipe enter vaporiser body inside from base of evaporator, 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 16 into in the evaporation cavity 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 17 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 13 of carbonated drink segregation section 10 along steam-water separator 7, steam water interface is separated in steam-water separation chamber 13 for the first time, clean distilled water steam rises through carbonated drink separate mesh 9 after carbonated drink is separated once more, clean distilled water steam is along helical duct 8 rotation at a high speed of spiral separator 15, by carbonated drink separation once more, distilled water steam clean after separating rises along helical duct 8,, indirect steam outlet 6 enters lower effective evaporator after discharging, follow-up each effect connects successively, raw material water-setting water is then wandered in the steam-water separation chamber 13 along coagulating water opening 12, last raw material water-setting water is discharged from raw water outlet 14, 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 base of evaporator, not only shortened the equipment tube side of exposed pipeline outward, reduced scattering and disappearing of heat, raw water also can be preheated in vaporiser body, improved the utilization rate of heat, so can finally improve producing effects of distilled water greatly.
Claims (6)
1, a kind of two section type spiral separation evaporimeter, comprise vaporiser body, the tubulation that matches and the turnover mouth of pipe, the top that it is characterized in that vaporiser body is that evaporator section (3), bottom are carbonated drink segregation section (10), the bottom of evaporator section (3) is evaporation tubulation group (4), top is cloth water chamber (17), water inlet pipe (2) is set in the cloth water chamber (17), this water inlet pipe (2) runs through evaporator section (3) and carbonated drink segregation section (10) downwards, water inlet pipe mouth is visited the outside that reaches carbonated drink segregation section (10), in the carbonated drink segregation section (10) steam-water separator (7) is set in addition.
2, two section type spiral separation evaporimeter according to claim 1 is characterized in that water inlet pipe (2) is positioned at the center of vaporiser body.
3, two section type spiral separation evaporimeter according to claim 1 is characterized in that the bottom in the cloth water chamber (17) is provided with the water distributing plate (1) that all plants the water through hole.
4, two section type spiral separation evaporimeter according to claim 1, it is characterized in that the steam-water separator (7) that is provided with in the carbonated drink segregation section (10) is a funnel-shaped structure, ring steam-water separator (7) outer setting spiral separator (15), the top of steam-water separator (7) is positioned at the below of evaporation tubulation group (4), constitute steam-water separation chamber (13) between the intracavity bottom of bottom and carbonated drink segregation section (10), the carbonated drink cylinder (9) of the uniform through hole that carbonated drink segregation section (10) the inwall setting of corresponding steam-water separator (7) matches, leave the water outlet opening between the bottom of carbonated drink cylinder (9) and carbonated drink segregation section (10) inwall, and the bottom between carbonated drink cylinder (9) and steam-water separator (7) is provided with carbonated drink separate mesh (9).
5, two section type spiral separation evaporimeter according to claim 4, the section that it is characterized in that carbonated drink cylinder (9) is a trapezium structure.
6,, it is characterized in that water inlet pipe (2) 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 spiral separation evaporimeters.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200420040650 CN2705220Y (en) | 2004-05-20 | 2004-05-20 | Double section screw separating evaporator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200420040650 CN2705220Y (en) | 2004-05-20 | 2004-05-20 | Double section screw separating evaporator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2705220Y true CN2705220Y (en) | 2005-06-22 |
Family
ID=34850638
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200420040650 Expired - Lifetime CN2705220Y (en) | 2004-05-20 | 2004-05-20 | Double section screw separating evaporator |
Country Status (1)
Country | Link |
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CN (1) | CN2705220Y (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100390073C (en) * | 2005-12-02 | 2008-05-28 | 宁波振国制药设备制造有限公司 | Vapor, water four-grade separating water distilling machine |
-
2004
- 2004-05-20 CN CN 200420040650 patent/CN2705220Y/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100390073C (en) * | 2005-12-02 | 2008-05-28 | 宁波振国制药设备制造有限公司 | Vapor, water four-grade separating water distilling machine |
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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 | ||
CX01 | Expiry of patent term |
Expiration termination date: 20140520 Granted publication date: 20050622 |