CN203629363U - Dry type reflux high-level condenser - Google Patents
Dry type reflux high-level condenser Download PDFInfo
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- CN203629363U CN203629363U CN201320580245.7U CN201320580245U CN203629363U CN 203629363 U CN203629363 U CN 203629363U CN 201320580245 U CN201320580245 U CN 201320580245U CN 203629363 U CN203629363 U CN 203629363U
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- dry type
- goes out
- knockout drum
- pipe
- condensing chamber
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Abstract
The utility model discloses a dry type reflux high-level condenser which comprises a condensing chamber, wherein staggered water spraying plates are arranged in the condensing chamber; the top of the condensing chamber is semispherical; a cooling water inlet pipe and a non-condensed gas outlet pipe are arranged on the two symmetric side of the top of the condensing chamber; a steam inlet pipe and a gas pressure pipe are arranged at the bottom of the condensing chamber; the non-condensed gas outlet pipe is connected to a separating tank and extends to the middle part of the separating tank; a gas outlet of the non-condensed gas outlet pipe is downwards arranged; a gas exhaust opening is formed in the top of the separating tank; the gas pressure pipe is arranged at the lower end of the separating tank; the lower end of the gas pressure pipe extends into the water tank. According to the dry type reflux high-level condenser, cooling water is sprayed from the top, and steam enters the condensing chamber from the bottom, so that the condensing efficiency of the steam is improved.
Description
Technical field
The utility model relates to dry type countercurrent flow high up condenser, belongs to chemical industry equipment field.
Background technology
Dry type countercurrent flow high up condenser is a kind of conventional mixing condenser, and the condensation process of the cooling or steam to some gas can make heat, cold fluid directly mix and carry out heat exchange; This heat exchange mode is only applicable to permission in technique and mutually mixes two fluids; The advantage of this heat exchange mode is that heat-transfer effect is good, and device structure is simple.Traditional dry type countercurrent flow high up condenser, water inlet pipe and entering on the sidewall that steam pipe is all arranged on condenser, the condensation efficiency of steam is low, and the space availability ratio of condenser is low.
Summary of the invention
In order to solve the problem of above-mentioned existence, the utility model discloses a kind of dry type countercurrent flow high up condenser, this condenser, the complete adverse current of steam and cooling water, both contact fully, improve the condensation efficiency of steam.
Dry type countercurrent flow high up condenser, comprises condensation chamber, is provided with the drip water plate of intersection in condensation chamber, and the top of described condensation chamber is hemispherical, and cooling water inlet pipe is set symmetrical both sides, top and fixed gas goes out pipe, and bottom arranges steam inlet tube and pneumatic tube.
Described fixed gas goes out pipe and is connected on a knockout drum, and fixed gas goes out pipe and reaches knockout drum middle part, and the gas outlet that fixed gas goes out pipe arranges downwards, and the top of knockout drum is provided with exhaust outlet.
The lower end of described knockout drum arranges pneumatic tube, and pneumatic tube lower end extends in tank.
The utility model, cooling water is from the top ejection of condensation chamber, and cool water shower is even, and steam enters from condensation chamber bottom, and air-flow is even, and steam can fully mix with cooling water, forms condensate liquid.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model,
Accompanying drawing is indicated list: 1-knockout drum, and 2-exhaust outlet, 3-fixed gas goes out pipe, 4-cooling water inlet pipe, 5-condensation chamber, 6-drip water plate, 7-steam inlet tube, 8,8 '-pneumatic tube, 9-tank.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, further illustrate the utility model.Should understand the following specific embodiment and only be not used in restriction scope of the present utility model for the utility model is described.It should be noted that, word 'fornt', 'back', " left side ", " right side ", "up" and "down" that use is described below refer to the direction in accompanying drawing, and word " interior " and " outward " refer to respectively the direction towards or away from specific features geometric center.
Fig. 1 is structural representation of the present utility model, as we can see from the figure, this dry type countercurrent flow high up condenser, comprise condensation chamber 5, in condensation chamber 5, be provided with the drip water plate 6 of intersection, the top of condensation chamber 5 is hemispherical, and cooling water inlet pipe 4 is set symmetrical both sides, top and fixed gas goes out pipe 3, and bottom arranges steam inlet tube 7 and pneumatic tube 8; Fixed gas goes out pipe 3 and is connected on a knockout drum 1, and fixed gas goes out pipe 3 and reaches knockout drum 1 middle part, and the gas outlet that fixed gas goes out pipe 3 arranges downwards, and the top of knockout drum 1 is provided with exhaust outlet 2; The lower end of knockout drum 1 arranges pneumatic tube 8 ', and pneumatic tube 8 and pneumatic tube 8 ' lower end extend in tank 9.
The utility model, in use, cooling water from top spray, cooling water is in the process falling, through drip water plate 6, intersect and change the flow direction, final, steam is dissolved in cooling water, form condensate liquid, in steam, on-condensible gas, in the interior rising of condensation chamber 5, goes out pipe 3 from the fixed gas at top and discharges.Knockout drum 1 is used for separating and goes out Guan Zhongke from fixed gas and congeal into point, and on-condensible gas is discharged from exhaust outlet 2, drops to knockout drum 1 bottom after point condensation of can congealing into, and enters pneumatic tube 8 '.
The disclosed technological means of the utility model scheme is not limited only to the disclosed technological means of above-mentioned technological means, also comprises the technical scheme being made up of above technical characterictic.
Claims (3)
1. dry type countercurrent flow high up condenser, comprise condensation chamber, it is characterized in that being provided with in described condensation chamber the drip water plate of intersection, top and the bottom of described condensation chamber are hemispherical, cooling water inlet pipe is set symmetrical both sides, top and fixed gas goes out pipe, bottom sidewall arranges steam inlet tube, and pneumatic tube is set in the middle of bottom.
2. dry type countercurrent flow high up condenser according to claim 1, is characterized in that described fixed gas goes out pipe and is connected on a knockout drum, and fixed gas goes out pipe and reaches knockout drum middle part, and the gas outlet that fixed gas goes out pipe arranges downwards, and the top of knockout drum is provided with exhaust outlet.
3. dry type countercurrent flow high up condenser according to claim 2, is characterized in that the lower end of described knockout drum arranges pneumatic tube, and pneumatic tube lower end extends in tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320580245.7U CN203629363U (en) | 2013-09-21 | 2013-09-21 | Dry type reflux high-level condenser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320580245.7U CN203629363U (en) | 2013-09-21 | 2013-09-21 | Dry type reflux high-level condenser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203629363U true CN203629363U (en) | 2014-06-04 |
Family
ID=50815829
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320580245.7U Expired - Fee Related CN203629363U (en) | 2013-09-21 | 2013-09-21 | Dry type reflux high-level condenser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203629363U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103471423A (en) * | 2013-09-21 | 2013-12-25 | 南京福昌环保有限公司 | Dry type countercurrent high-order condenser |
| CN104567467A (en) * | 2014-12-24 | 2015-04-29 | 无锡市南长区科技创业服务中心 | Heat exchanger with relatively high efficiency |
| CN106288468A (en) * | 2016-09-20 | 2017-01-04 | 天津商业大学 | Vertical downstream directly contacts the air-cooled refrigeration system of auxiliary of condensation |
| CN106288467A (en) * | 2016-09-20 | 2017-01-04 | 天津商业大学 | The auxiliary water cooling refrigeration system of condensing heat exchanger is directly contacted with vertical counterflow |
| CN106642836A (en) * | 2017-02-17 | 2017-05-10 | 天津商业大学 | Direct contact condensation refrigeration system with saturated liquid supercooled completely |
| CN106766314A (en) * | 2017-02-17 | 2017-05-31 | 天津商业大学 | Directly contact with auxiliary circulation condenses refrigeration system |
-
2013
- 2013-09-21 CN CN201320580245.7U patent/CN203629363U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103471423A (en) * | 2013-09-21 | 2013-12-25 | 南京福昌环保有限公司 | Dry type countercurrent high-order condenser |
| CN104567467A (en) * | 2014-12-24 | 2015-04-29 | 无锡市南长区科技创业服务中心 | Heat exchanger with relatively high efficiency |
| CN106288468A (en) * | 2016-09-20 | 2017-01-04 | 天津商业大学 | Vertical downstream directly contacts the air-cooled refrigeration system of auxiliary of condensation |
| CN106288467A (en) * | 2016-09-20 | 2017-01-04 | 天津商业大学 | The auxiliary water cooling refrigeration system of condensing heat exchanger is directly contacted with vertical counterflow |
| CN106642836A (en) * | 2017-02-17 | 2017-05-10 | 天津商业大学 | Direct contact condensation refrigeration system with saturated liquid supercooled completely |
| CN106766314A (en) * | 2017-02-17 | 2017-05-31 | 天津商业大学 | Directly contact with auxiliary circulation condenses refrigeration 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: 20140604 Termination date: 20140921 |
|
| EXPY | Termination of patent right or utility model |