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CN102692137A - Air-cooling-type tubular condensation device - Google Patents

Air-cooling-type tubular condensation device Download PDF

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Publication number
CN102692137A
CN102692137A CN201210192894XA CN201210192894A CN102692137A CN 102692137 A CN102692137 A CN 102692137A CN 201210192894X A CN201210192894X A CN 201210192894XA CN 201210192894 A CN201210192894 A CN 201210192894A CN 102692137 A CN102692137 A CN 102692137A
Authority
CN
China
Prior art keywords
gas
condenser pipe
separation chamber
liquid separation
metal line
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.)
Pending
Application number
CN201210192894XA
Other languages
Chinese (zh)
Inventor
王金平
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhenjiang Xinmengxi Energy Science & Technology Co Ltd
Original Assignee
Zhenjiang Xinmengxi Energy Science & Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Zhenjiang Xinmengxi Energy Science & Technology Co Ltd filed Critical Zhenjiang Xinmengxi Energy Science & Technology Co Ltd
Priority to CN201210192894XA priority Critical patent/CN102692137A/en
Publication of CN102692137A publication Critical patent/CN102692137A/en
Pending legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The invention discloses an air-cooling-type tubular condensation device, wherein the condensation device comprises a condenation tube, a fin and a gas-liquid separation chamber; air can be taken as a cooling medium, and the mixture of steam and other gases can be condensed into a liquid, and gas and liquid separation is realized.

Description

A kind of air-cooled tubular type condensing unit
One, technical field
The present invention relates to the installation for steam condensation field, refer in particular to a kind of air-cooled tubular type condensing unit that can the mixture of steam and other gases be condensed into liquid and realize gas-liquid separation.
Two, background technology
Steam-sprayed refrigerator generally adopts mixing condenser or shell-and-tube heat exchanger.When application mix formula condenser, cooling water descends from last spray, and steam feeds from the bottom, directly contacts with the cooling water that sprays during rising, and condensation becomes liquid phase, and cooling water then heating temperature raises.Because cooling water can be dissolved with a certain amount of air at a lower temperature, wherein air was overflowed when temperature raise, and therefore vavuum pump need be set extract out, had increased input and operating cost.When using shell-and-tube cooler,, cause cooling effectiveness to reduce because liquid phase and gas phase media are present in the condenser simultaneously.For addressing the above problem, the present invention has designed a kind of air-cooled, can the mixture of steam and other gases be condensed into liquid and realize the trumpet cooler of gas-liquid separation.
Three, summary of the invention
The present invention proposes a kind of air-cooled tubular type condensing unit; Structure comprises: gas-liquid separation chamber, condenser pipe, fin; Wherein gas-liquid separation chamber is divided into a plurality of cavitys by the dividing plate that stretches into below the metal line; The demarcation strip lower end is in the position near gas-liquid separation chamber bottom, but is not connected with the bottom, makes that the liquid in each cavity can flow each other.Condenser pipe vertically is welded on the gas-liquid separation chamber top.The import condenser pipe of condenser stretches into below the metal line, and the outlet condenser pipe of condenser is more than metal line.Other condenser pipe one ends stretch into below the metal line; The other end strides across the inside that demarcation strip probes into another cavity; And more than liquid level, a plurality of condenser pipes distribute successively, make gas after condenser pipe import entering gas-liquid separation chamber; Be introduced under the liquid level, gas gets into next cavity from the opening that another root condenser pipe is positioned on the liquid level then.Be welded with a plurality of fins on the every condenser pipe, when air-flow externally flows through fin under the fan action, heat taken away.Fin thickness is 1 millimeter, and width is 6 centimetres to 10 centimetres.There are an inlet and a liquid outlet in the gas-liquid separation chamber two ends, and the inlet position is higher, and the liquid outlet position is lower.The indoor metal line of gas-liquid separation position must maintain certain altitude, makes the opening of demarcation strip lower end, condenser pipe lower end all below metal line, and the opening of condenser pipe upper end is more than metal line.
Four, description of drawings
Below in conjunction with accompanying drawing, the present invention is described further.
Fig. 1 is the front section view of this device.
Fig. 2 is the A-A cross-sectional view of this device.
The position of marking is respectively among the figure: 1, import condenser pipe; 2, condenser pipe; 3, fin; 4, metal line; 5, gas-liquid separation chamber; 6, liquid outlet; 7, inlet; 8, outlet condenser pipe.
Five, the specific embodiment
Below in conjunction with accompanying drawing, embodiment of the present invention is described further.
Steam gets into condenser pipe 2 from steam inlet 1, flows and condensations gradually along condenser pipe 2, and the liquid after condensing gets into the cavity of gas-liquid separation chamber 5 with the gas that does not condense.Because below 4, liquid imports the liquid of gas-liquid separation chamber 5 to condenser pipe 2 one ends at metal line, gas is overflowed and is got into next cooling procedure from next root condenser pipe 2.Through repeats condensation process repeatedly, last incondensible gas is overflowed from steam (vapor) outlet 8, and liquid is stayed in the gas-liquid separation chamber 5.At last through liquid outlet 6 and inlet 7 control metal line height.Blower fan can be placed in the condenser outside, quickens air and flows, and improves cooling velocity.

Claims (5)

1. air-cooled tubular type condensing unit, this device is made up of condenser pipe (2), fin (3), gas-liquid separation chamber (5), and wherein: condenser pipe (2) vertically is welded on the top of gas-liquid separation chamber (5), and fin (3) is welded on the condenser pipe (2).
2. a kind of air-cooled tubular type condensing unit according to claim 1; It is characterized in that: gas-liquid separation chamber (5) is divided into a plurality of cavitys by the dividing plate that stretches into below the metal line; The demarcation strip lower end is in the position near gas-liquid separation chamber (5) bottom; But be not connected, make that the liquid in each cavity can flow each other with the bottom.
3. a kind of air-cooled tubular type condensing unit according to claim 1 is characterized in that: the import condenser pipe (1) of condenser stretches into below the metal line (4), and the outlet condenser pipe (8) of condenser is more than metal line; Other condenser pipe (2) one ends stretch into below the metal line (4); The other end strides across the inside that demarcation strip probes into another cavity; And more than liquid level, a plurality of condenser pipes (2) distribute successively, make gas after import condenser pipe (1) entering gas-liquid separation chamber (5); Be introduced under the liquid level, gas gets into next cavity from the opening that another root condenser pipe is positioned on the liquid level then.
4. a kind of air-cooled tubular type condensing unit according to claim 1 is characterized in that: fin (3) thickness is 1 millimeter, and width is 6 centimetres to 10 centimetres.
5. a kind of air-cooled tubular type condensing unit according to claim 1 is characterized in that: there are an inlet (7) and a liquid outlet (6) in gas-liquid separation chamber (5) two ends, and inlet (7) position is higher, and liquid outlet (6) position is lower; The interior metal line of gas-liquid separation chamber (5) (4) position must maintain certain altitude, makes the opening of demarcation strip lower end, condenser pipe lower end all below metal line, and the opening of condenser pipe upper end is more than metal line.
CN201210192894XA 2012-06-07 2012-06-07 Air-cooling-type tubular condensation device Pending CN102692137A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210192894XA CN102692137A (en) 2012-06-07 2012-06-07 Air-cooling-type tubular condensation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210192894XA CN102692137A (en) 2012-06-07 2012-06-07 Air-cooling-type tubular condensation device

Publications (1)

Publication Number Publication Date
CN102692137A true CN102692137A (en) 2012-09-26

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210192894XA Pending CN102692137A (en) 2012-06-07 2012-06-07 Air-cooling-type tubular condensation device

Country Status (1)

Country Link
CN (1) CN102692137A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107883783A (en) * 2017-11-23 2018-04-06 丹阳市华诚包装有限公司 A kind of degradable cellulose packaging special Sewage treatment cooling tank of film preparation
CN109888431A (en) * 2019-01-22 2019-06-14 重庆交通大学 Battery Thermal Management System

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54150507A (en) * 1978-05-19 1979-11-26 Toshiba Corp Condenser
DE3826761A1 (en) * 1988-08-04 1990-02-08 Siemens Ag HEAT EXCHANGER WITH DEGASSING DEVICE
JPH0926272A (en) * 1995-07-14 1997-01-28 Hitachi Ltd Condenser
US20020053505A1 (en) * 1999-04-23 2002-05-09 Arrison Norman L. Horizontal distillation apparatus and method
JP2007285576A (en) * 2006-04-14 2007-11-01 Tlv Co Ltd Heat exchanger
JP4361203B2 (en) * 2000-11-15 2009-11-11 株式会社テイエルブイ Steam heating device
CN201583154U (en) * 2010-01-22 2010-09-15 北京白象新技术有限公司 Water refrigerating drier for quickly cleaning sterilizers
JP2011145021A (en) * 2010-01-15 2011-07-28 Tlv Co Ltd Waste steam recovery device

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54150507A (en) * 1978-05-19 1979-11-26 Toshiba Corp Condenser
DE3826761A1 (en) * 1988-08-04 1990-02-08 Siemens Ag HEAT EXCHANGER WITH DEGASSING DEVICE
JPH0926272A (en) * 1995-07-14 1997-01-28 Hitachi Ltd Condenser
US20020053505A1 (en) * 1999-04-23 2002-05-09 Arrison Norman L. Horizontal distillation apparatus and method
JP4361203B2 (en) * 2000-11-15 2009-11-11 株式会社テイエルブイ Steam heating device
JP2007285576A (en) * 2006-04-14 2007-11-01 Tlv Co Ltd Heat exchanger
JP2011145021A (en) * 2010-01-15 2011-07-28 Tlv Co Ltd Waste steam recovery device
CN201583154U (en) * 2010-01-22 2010-09-15 北京白象新技术有限公司 Water refrigerating drier for quickly cleaning sterilizers

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107883783A (en) * 2017-11-23 2018-04-06 丹阳市华诚包装有限公司 A kind of degradable cellulose packaging special Sewage treatment cooling tank of film preparation
CN109888431A (en) * 2019-01-22 2019-06-14 重庆交通大学 Battery Thermal Management System

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Application publication date: 20120926