CN2520494Y - Empty tower spray condenser - Google Patents
Empty tower spray condenser Download PDFInfo
- Publication number
- CN2520494Y CN2520494Y CN 02221331 CN02221331U CN2520494Y CN 2520494 Y CN2520494 Y CN 2520494Y CN 02221331 CN02221331 CN 02221331 CN 02221331 U CN02221331 U CN 02221331U CN 2520494 Y CN2520494 Y CN 2520494Y
- Authority
- CN
- China
- Prior art keywords
- atomising device
- cylindrical shell
- spraying
- hollow
- water tank
- 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
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model provides a superficial spray cooler, which comprises a tube body, a supporting foot, a water inlet main pipe, an air inlet pipe, an air outlet pipe, a water outlet pipe, condensation elements which are composed of an atomising device and a trickle plate are arranged in the tube body, and a ring-shaped water tank which is respectively communicated with the water inlet main pipe and the atomising device and the ring-shaped water tank is arranged on the outer wall of the tube body. The utility model has the advantages that cooling water can be evenly sprayed downwards by the atomising device, and cooling surface area is large, which can largely reduce cooling water quantity, can lower fluid resistance, can improve vacuum degree, and has distinctive energy saving effect.
Description
Technical field
The utility model relates to a kind of high vacuum system equipment, particularly a kind of hollow-spraying-tower condenser that is used for the multiple-effect evaporation production technology.
Background technology
The condensation element of existing hollow-spraying-tower condenser generally is made up of drip water plate and cooling tubulation, having pipeline easily stops up, cooling water shortcoming pockety, make the gas that is condensed to carry out heat exchange with cooling water fully, thereby fully condensation condensable gas, so cooling effect is poor, the system energy consumption height, yield poorly, the production cost height.
The utility model content
The purpose of this utility model is to provide a kind of hollow-spraying-tower condenser, adopts centrifugal atomization apparatus and drip water plate as the condensation element, the purpose that improve cooling effect to reach, reduces the cooling energy consumption.
Solution of the present utility model is that this kind hollow-spraying-tower condenser comprises cylindrical shell, feet, be located at the outer water inlet manifold of cylindrical shell, the indirect steam air inlet pipe that is communicated with the cylindrical shell bottom, be located at the on-condensible gas escape pipe of upper cover, be located at the outlet pipe of lower cone, and be located at condensation element in the cylindrical shell, it is characterized in that described condensation element comprises atomising device and drip water plate, the staggered cylinder inboard wall that is fixed on of drip water plate, atomising device then is stratified and set in the cylindrical shell, and alternate setting with drip water plate, then be provided with the annular water tank that communicates with water inlet manifold at cylinder body outer wall, atomising device is communicated with annular water tank.
Above-mentioned atomising device comprises to be taken over and atomizer, can divide 1～5 group of setting, and every group is provided with 1～2 layer, and wherein two-layer atomising device is that branch is crisscross arranged up and down.
Above-mentioned annular water tank correspondingly is provided with 1～5 corresponding to the grouping of atomising device, and is communicated with atomizer by taking over.
Be evenly distributed with aperture on the above-mentioned drip water plate, its end is provided with baffle plate.
Advantage of the present utility model is to adopt the atomizer that is crisscross arranged and drip water plate as the condensation element, making cooling water be vaporific evenly sprays downwards, the frigorimeter area can increase 30%, impel condensed gas and cooling water to carry out sufficient heat exchange, improve cooling effect widely, thereby make cooling water inflow reduce 20%, fluid resistance reduces by 200 millimetress of mercury (mmHg) simultaneously, vacuum improves 15 millimetress of mercury (mmHg), saves investment 15%, has very obvious energy-saving effect.
Description of drawings
Accompanying drawing 1 is the utility model front view;
Accompanying drawing 2 is partial enlarged drawings of accompanying drawing 1;
Accompanying drawing 3 is the utility model atomising device distribution maps;
Accompanying drawing 4 is drip water plate structure charts;
Accompanying drawing 5 is partial enlarged drawings of accompanying drawing 4.
The specific embodiment
Below in conjunction with accompanying drawing the utility model embodiment is further described.
With KTPL-2200 type hollow-spraying-tower condenser is the example explanation: this kind condenser comprises cylindrical shell 14, lower cone 2, upper cover 12, feet 3, be located at the outlet pipe 1 of lower cone small end, the indirect steam air inlet pipe 5 that is communicated with the cylindrical shell bottom, air inlet pipe reinforcement 4, be located at the outer water inlet manifold 9 of cylindrical shell, be located at the on-condensible gas escape pipe 13 at upper cover 12 tops, be located at the condensation element of forming by atomizer 16 and drip water plate 10 in the cylindrical shell 14, be located at the annular water tank 7 of cylinder body outer wall, and be located at manhole 15 and 17 etc. on the cylindrical shell.Cylindrical shell 14 diameter 2200mm, thickness 14mm welds upper cover 12 and lower cone 2 up and down respectively, and feet is provided with four, is welded on respectively on the lower cone 2.Water inlet manifold 9 diameter 426mm, thickness 10mm be arranged in parallel with cylindrical shell.Annular water tank 7 minutes is the two-layer cylinder body outer wall that is welded on up and down, external diameter 2600mm, and internal diameter 2230mm, height 400mm, wall thickness 14mm, and be communicated with water inlet manifold 9 by water inlet pipe pipe nipple 8.Atomizer 16 is provided with two groups corresponding to water tank, every group 17, the two-layer setting of every component, two-layer the upper strata is provided with 5 at a distance of 340mm, and lower floor is provided with 12, and two-layer up and down being crisscross arranged, it takes over long 740mm at the middle and upper levels, and lower floor takes over long 370mm, and 16 of atomizers pass through adapter 11 and flange is communicated with annular water tank 7.At cylindrical shell 14 inwalls, with two groups of shower nozzles, 16 alternate two drip water plates 10 and 6 of being welded with, two drip water plates are symmetrical arranged, and are mososeries, and are connected to the zigzag plate washer in the string side weld, the radius of two drip water plates is 1100mm, thickness is 14mm, and the chord length of its middle and upper part drip water plate 10 is 1571mm, and the chord length of bottom drip water plate 6 is 2198mm, also have on two drip water plates and be the equally distributed circular hole of isosceles triangle, the aperture is 10mm.
Operation principle of the present utility model is: the indirect steam in the vapo(u)rization system enters in the cylindrical shell 14 from steam inlet pipe 5, cooling water enters annular water tank 7 by water inlet manifold 9, from atomizer 16, be vaporific evenly sprinkling downwards by taking over 11 again, to condensable gas carry out in a large number, condensation fully, make system form high vacuum state, reach the purpose of consumption reduction, energy-conservation, volume increase, can be widely used in the multiple-effect evaporation production technology of industries such as chemical industry, medicine, metallurgy.
Claims (4)
1, a kind of hollow-spraying-tower condenser, comprise cylindrical shell, feet, be located at cylindrical shell outer water inlet manifold, the indirect steam air inlet pipe that is communicated with the cylindrical shell bottom, the on-condensible gas escape pipe that is located at upper cover, be located at the outlet pipe of lower cone and be located at the interior condensation element of cylindrical shell, it is characterized in that described condensation element comprises atomising device and drip water plate, the staggered cylinder inboard wall that is fixed on of drip water plate, atomising device then is stratified and set in the cylindrical shell, and alternate setting with drip water plate, then be provided with the annular water tank that communicates with water inlet manifold at cylinder body outer wall, atomising device is communicated with water tank.
2, hollow-spraying-tower condenser according to claim 1 is characterized in that described atomising device comprises adapter and atomizer, can divide 1～5 group of setting, and every group is provided with 1～2 layer, and wherein two-layer atomising device is that branch is crisscross arranged up and down.
3, hollow-spraying-tower condenser according to claim 1 and 2 is characterized in that the grouping of described annular water tank corresponding to atomising device, correspondingly is provided with 1～5, and is communicated with atomizer by taking over.
4, hollow-spraying-tower condenser according to claim 1 is characterized in that being evenly distributed with aperture on the described drip water plate, and its end is provided with baffle plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02221331 CN2520494Y (en) | 2002-01-17 | 2002-01-17 | Empty tower spray condenser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02221331 CN2520494Y (en) | 2002-01-17 | 2002-01-17 | Empty tower spray condenser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2520494Y true CN2520494Y (en) | 2002-11-13 |
Family
ID=33699454
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 02221331 Expired - Fee Related CN2520494Y (en) | 2002-01-17 | 2002-01-17 | Empty tower spray condenser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2520494Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100354591C (en) * | 2003-12-31 | 2007-12-12 | 大连理工大学 | Phacelloid throat type automatic gas exhausting direct contact steam condenser and its use method |
| CN102200396A (en) * | 2011-07-01 | 2011-09-28 | 北京市劳动保护科学研究所 | Mixed heat exchange device for gaseous and liquid materials |
| CN102435079A (en) * | 2011-10-12 | 2012-05-02 | 厦门大学 | Condensation system of biomass pyrolyzed steam |
| CN105674761A (en) * | 2016-04-13 | 2016-06-15 | 成都信息工程大学 | Mixing condenser |
-
2002
- 2002-01-17 CN CN 02221331 patent/CN2520494Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100354591C (en) * | 2003-12-31 | 2007-12-12 | 大连理工大学 | Phacelloid throat type automatic gas exhausting direct contact steam condenser and its use method |
| CN102200396A (en) * | 2011-07-01 | 2011-09-28 | 北京市劳动保护科学研究所 | Mixed heat exchange device for gaseous and liquid materials |
| CN102435079A (en) * | 2011-10-12 | 2012-05-02 | 厦门大学 | Condensation system of biomass pyrolyzed steam |
| CN105674761A (en) * | 2016-04-13 | 2016-06-15 | 成都信息工程大学 | Mixing condenser |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |