CN103471423A - Dry type countercurrent high-order condenser - Google Patents
Dry type countercurrent high-order condenser Download PDFInfo
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- CN103471423A CN103471423A CN2013104277911A CN201310427791A CN103471423A CN 103471423 A CN103471423 A CN 103471423A CN 2013104277911 A CN2013104277911 A CN 2013104277911A CN 201310427791 A CN201310427791 A CN 201310427791A CN 103471423 A CN103471423 A CN 103471423A
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- condensation chamber
- dry type
- condenser
- goes out
- knockout drum
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Abstract
The invention discloses a dry type countercurrent high-order condenser. The dry type countercurrent high-order condenser comprises a condensation chamber, crossed drip water plates are arranged in the condensation chamber, the top of the condensation chamber is semi-spherical, a cooling water inlet pipe and a non-condensable gas outlet pipe are arranged at two symmetric sides of the top of the condensation chamber, two steam inlet pipes and a pneumatic pipe are arranged at the bottom of the condensation chamber, the non-condensable gas outlet pipe is connected with a separating tank and extends into the middle of the separating tank, a gas outlet of the non-condensable gas outlet pipe is downward, an exhaust opening is formed in the top of the separating tank, the lower end of the separating tank is provided with the pneumatic pipe, and the lower end of the pneumatic pipe extends into a water tank. According to the condenser disclosed by the invention, cooling water is sprayed from the top, and steam is capable of entering the condensation chamber from the bottom so as to improve the condensation efficiency of the steam.
Description
Technical field
The present invention relates to dry type countercurrent flow high up condenser, belong to the chemical industry equipment field.
Background technology
Dry type countercurrent flow high up condenser is a kind of mixing condenser commonly used, to the condensation process of the cooling or steam of some gas, can make heat, cold fluid directly mix and carry out heat exchange; This heat exchange mode is only applicable on technique allow mutually to mix 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 advancing on the sidewall that steam pipe all is 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 invention 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, comprise condensation chamber, is provided with the drip water plate of intersection in condensation chamber, and the top of described condensation chamber is hemispherical, and the 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 the 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 the pneumatic tube lower end extends in tank.
The present invention, cooling water is from the top ejection of condensation chamber, and cool water shower is even, and steam enters from the condensation chamber bottom, and air-flow is even, and steam can fully mix with cooling water, forms condensate liquid.
The accompanying drawing explanation
Fig. 1 is structural representation of the present invention,
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 present invention.Should understand the following specific embodiment only is not used in and limits the scope of the invention for the present invention 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, word " interior " and " outward " refer to respectively towards or away from the direction of particular elements geometric center.
Fig. 1 is structural representation of the present invention, as we can see from the figure, this dry type counter-current flow high-order condenser, comprise condensation chamber 5, be provided with the drip water plate 6 of intersection in condensation chamber 5, 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 present invention, in use, cooling water from top spray, cooling water is in the process fallen, 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 discharges from the fixed gas at top.Knockout drum 1 is used for separating and goes out Guan Zhongke from fixed gas and congeal into minute, and on-condensible gas, from exhaust outlet 2 discharges, drops to knockout drum 1 bottom after minute condensation of can congealing into, enter pneumatic tube 8 '.
The disclosed technological means of the present invention program is not limited only to the disclosed technological means of above-mentioned technological means, also comprises the technical scheme be comprised of above technical characterictic any combination.
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, the cooling water inlet pipe is set symmetrical both sides, top and fixed gas goes out pipe, the 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 the 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 the pneumatic tube lower end extends in tank.
Priority Applications (1)
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CN2013104277911A CN103471423A (en) | 2013-09-21 | 2013-09-21 | Dry type countercurrent high-order condenser |
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CN2013104277911A CN103471423A (en) | 2013-09-21 | 2013-09-21 | Dry type countercurrent high-order condenser |
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CN103471423A true CN103471423A (en) | 2013-12-25 |
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CN2013104277911A Pending CN103471423A (en) | 2013-09-21 | 2013-09-21 | Dry type countercurrent high-order condenser |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104215089A (en) * | 2014-09-16 | 2014-12-17 | 昆山黑格特温控设备有限公司 | High-level condenser |
CN105152245A (en) * | 2015-08-31 | 2015-12-16 | 太仓英达锅炉设备有限公司 | High-position condensing device capable of automatically controlling temperature |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61114711A (en) * | 1984-11-09 | 1986-06-02 | Kenichi Nakagawa | Method and apparatus for recovering heat from contaminated high temperature exhaust gas |
CN2062816U (en) * | 1990-03-22 | 1990-09-26 | 魏仕英 | Spray-type mixing condenser |
CN201177462Y (en) * | 2007-10-31 | 2009-01-07 | 北京弘泰汇明能源技术有限责任公司 | Coke quenching steam-condensed water separation and recovery plant |
CN203629363U (en) * | 2013-09-21 | 2014-06-04 | 南京福昌环保有限公司 | Dry type reflux high-level condenser |
-
2013
- 2013-09-21 CN CN2013104277911A patent/CN103471423A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61114711A (en) * | 1984-11-09 | 1986-06-02 | Kenichi Nakagawa | Method and apparatus for recovering heat from contaminated high temperature exhaust gas |
CN2062816U (en) * | 1990-03-22 | 1990-09-26 | 魏仕英 | Spray-type mixing condenser |
CN201177462Y (en) * | 2007-10-31 | 2009-01-07 | 北京弘泰汇明能源技术有限责任公司 | Coke quenching steam-condensed water separation and recovery plant |
CN203629363U (en) * | 2013-09-21 | 2014-06-04 | 南京福昌环保有限公司 | Dry type reflux high-level condenser |
Non-Patent Citations (1)
Title |
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胡素华: "怎样使用干式逆流冷凝器", 《发酵科技通讯》 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104215089A (en) * | 2014-09-16 | 2014-12-17 | 昆山黑格特温控设备有限公司 | High-level condenser |
CN105152245A (en) * | 2015-08-31 | 2015-12-16 | 太仓英达锅炉设备有限公司 | High-position condensing device capable of automatically controlling temperature |
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Application publication date: 20131225 |