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CN2783240Y - Trough pipe counter-flow heat exchanger - Google Patents

Trough pipe counter-flow heat exchanger Download PDF

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Publication number
CN2783240Y
CN2783240Y CN 200520017418 CN200520017418U CN2783240Y CN 2783240 Y CN2783240 Y CN 2783240Y CN 200520017418 CN200520017418 CN 200520017418 CN 200520017418 U CN200520017418 U CN 200520017418U CN 2783240 Y CN2783240 Y CN 2783240Y
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CN
China
Prior art keywords
spiral
outlet
coil
utility
model
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
Application number
CN 200520017418
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Chinese (zh)
Inventor
郭远杰
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN 200520017418 priority Critical patent/CN2783240Y/en
Application granted granted Critical
Publication of CN2783240Y publication Critical patent/CN2783240Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a slot pipe counter-flow heat exchanger. The utility model is characterized in that a spiral pipe slot (3) which is provided with a hole in the middle part is fixed in a high-pressure sealing outer drum (1); spiral coil pipes (2) are fixedly arranged on a coil pipe support frame (5) and a coil pipe support column (6) in the spiral pipe slot (3); the spiral pipe slot (3) is provided with a coil pipe slot inserting plate (7); partition plates (4) are arranged between the spiral coil pipes (2) at intervals; the upper part and the lower part of the high-pressure sealing outer drum (1) are respectively provided with a sealing cover; the upper sealing cover (12) is provided with a primary inlet (8) and a secondary outlet (11); the lower sealing cover (13) is provided with a primary outlet (9) and a secondary inlet (10); the spiral coil pipes (2) respectively extend out from the primary inlet (8) and the primary outlet (9); the secondary inlet (10) and the secondary outlet (11) are respectively connected with the spiral pipe slot. The utility model has the advantages of simple structure, few connecting openings and little fluid resistance. The utility model can integrally combine and mix central and separated air conditioners, heat pumps and refrigerators.

Description

The barrel contra-flow heat exchanger
Technical field
The utility model relates to a kind of barrel contra-flow heat exchanger.
Background technology
At present, various heat exchangers such as well-known pipe heat exchanger, spiral heat exchanger, removable heat exchanger, plate type heat exchanger, drawer formula heat exchanger, the ubiquity heat exchange efficiency is low, heat exchange is only dispelled the heat, the heat transferring medium flow is big, and heat exchanger volume is big, complex process, produce, the application cost height, waste heat has a narrow range of temperature and problem such as can't utilize again.Aspect heat energy energy applications and consumption, the heat exchange effect of heat exchanger and can utilize of crucial importancely again, technology is crucial, wherein air-conditioning power consumption, cold and hot exchange and inferior cold and hot utilizing again be air conditioner energy saving, reduce cost and key that the air conditioning applications situation is opened.
Summary of the invention
The purpose of this utility model provides a kind of barrel contra-flow heat exchanger.
The technical scheme that its technical problem that solves the utility model adopts is: middle porose spiral tube seat is fixed in the outer bucket of high pressure sealing, spiral coil is fixedly mounted on spiral tube seat interior the coil pipe support and coil pipe pillar, coil pipe groove plate is installed on the spiral tube seat, dividing plate is installed between the spiral coil at interval, the upper and lower seal cover of respectively installing of the outer bucket of high pressure sealing, have import just and time outlet on the top cover labyrinth, have outlet just and time import on the lower sealing cover; Spiral coil stretches out from first import with just exporting respectively, and inferior import is connected with the spiral tube seat respectively with time outlet.
Heat exchange partly is the heat insulation spiral line type groove of a laminated plastics preferably and heat conduction multi-layer helical line style copper pipe preferably, and the copper pipe support that is fixed is fixed on the centre of plastic channel.Heat exchange gas-liquid convection, the temperature of the heat energy that swaps out are entered temperature near what change, enter temperature by the outlet temperature after changing during near parallel operation.Three-point fix fixed tube support in the groove is arranged in a crossed manner to play eddy current effect, make do not have current stabilization in the groove, direct current liquid, improved heat transfer rate, or lacked the deposition of impurity in the groove and prevented fouling.Reach the purpose of efficient, high temperature, the heat exchange of low stream.The beneficial effects of the utility model are: this heat exchanger not only manufacturing process is simple, volume is little, in light weight, interface is few, fluid resistance is little, and time heat comprehensive utilization that can produce the low stream of high temperature, reduce application cost greatly, it can make central authorities, split-type air conditioner, heat pump, refrigerator share, use with reach integrated.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1 is a vertical section of the present utility model structural map;
Fig. 2 is the structural perspective of spiral tube seat and dividing plate;
Fig. 3 is a multi-layer helical coil pipe inclined-plane stereogram.
Among the figure: 1. the outer bucket of high pressure sealing, 2. spiral coil, 3. spiral tube seat, 4. dividing plate, 5. coil pipe support, 6. coil pipe pillar, 7. coil pipe groove plate, 8. import just, 9. outlet just, 10. time import, 11. outlets, 12. top cover labyrinths, 13. lower sealing cover.
The specific embodiment
Middle porose spiral tube seat 3 is fixed in the outer bucket 1 of high pressure sealing, spiral coil 2 is fixedly mounted on the coil pipe support 5 and coil pipe pillar 6 in the spiral tube seat 3, coil pipe groove plate 7 is installed on the spiral tube seat 3, dividing plate 4 is installed between the spiral coil 2 at interval, the outer bucket of the high pressure sealing 1 upper and lower seal cover of respectively installing, have import just 8 and time outlet 11 on the top cover labyrinth 12, have outlet 9 just and time import 10 on the lower sealing cover 13; Spiral coil 2 stretches out from first import 8 and first outlet 9 respectively, and inferior import 10 is connected with spiral tube seat 3 respectively with time outlet 11.

Claims (1)

1, a kind of barrel contra-flow heat exchanger, it is characterized in that: middle porose spiral tube seat (3) is fixed in the outer bucket of high pressure sealing (1), spiral coil (2) is fixedly mounted on spiral tube seat (3) interior the coil pipe support (5) and coil pipe pillar (6), coil pipe groove plate (7) is installed on the spiral tube seat (3), dividing plate (4) is installed between the spiral coil (2) at interval, the outer bucket of high pressure sealing (1) upper and lower seal cover of respectively installing, have import (8) just and time outlet (11) on the top cover labyrinth (12), have outlet (9) just and time import (10) on the lower sealing cover (13); Spiral coil (2) stretches out from first import (8) and first outlet (9) respectively, and inferior import (10) is connected with spiral tube seat (3) respectively with time outlet (11).
CN 200520017418 2005-04-15 2005-04-15 Trough pipe counter-flow heat exchanger Expired - Fee Related CN2783240Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200520017418 CN2783240Y (en) 2005-04-15 2005-04-15 Trough pipe counter-flow heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200520017418 CN2783240Y (en) 2005-04-15 2005-04-15 Trough pipe counter-flow heat exchanger

Publications (1)

Publication Number Publication Date
CN2783240Y true CN2783240Y (en) 2006-05-24

Family

ID=36768225

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200520017418 Expired - Fee Related CN2783240Y (en) 2005-04-15 2005-04-15 Trough pipe counter-flow heat exchanger

Country Status (1)

Country Link
CN (1) CN2783240Y (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102847844A (en) * 2012-08-10 2013-01-02 上海双开燃气用具有限公司 Heat exchange coil processing device
CN103278023A (en) * 2013-06-07 2013-09-04 合肥彩虹蓝光科技有限公司 Convenient and fast acid-alkali-resistant anticorrosive efficient condenser
CN103438734A (en) * 2013-08-27 2013-12-11 姜堰市泰怡金属网管有限公司 Detachable plate-shaped heat exchanger
CN103438617A (en) * 2013-08-27 2013-12-11 姜堰市泰怡金属网管有限公司 Detachable upright heat exchanger
CN104995473A (en) * 2012-12-05 2015-10-21 波利视觉股份有限公司 Spiral or helical counterflow heat exchanger
CN106017146A (en) * 2016-06-12 2016-10-12 洛阳文森科技有限公司 High-temperature heat pump heat exchanger and process
CN109696066A (en) * 2017-10-24 2019-04-30 翰昂汽车零部件有限公司 Contra-flow heat exchanger

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102847844A (en) * 2012-08-10 2013-01-02 上海双开燃气用具有限公司 Heat exchange coil processing device
CN102847844B (en) * 2012-08-10 2014-10-01 上海双开燃气用具有限公司 Heat exchange coil processing device
CN104995473A (en) * 2012-12-05 2015-10-21 波利视觉股份有限公司 Spiral or helical counterflow heat exchanger
CN104995473B (en) * 2012-12-05 2017-03-15 波利视觉股份有限公司 Heat exchanger
CN103278023A (en) * 2013-06-07 2013-09-04 合肥彩虹蓝光科技有限公司 Convenient and fast acid-alkali-resistant anticorrosive efficient condenser
CN103438734A (en) * 2013-08-27 2013-12-11 姜堰市泰怡金属网管有限公司 Detachable plate-shaped heat exchanger
CN103438617A (en) * 2013-08-27 2013-12-11 姜堰市泰怡金属网管有限公司 Detachable upright heat exchanger
CN103438617B (en) * 2013-08-27 2015-07-22 姜堰市泰怡金属网管有限公司 Detachable upright heat exchanger
CN106017146A (en) * 2016-06-12 2016-10-12 洛阳文森科技有限公司 High-temperature heat pump heat exchanger and process
CN109696066A (en) * 2017-10-24 2019-04-30 翰昂汽车零部件有限公司 Contra-flow heat exchanger
US11002487B2 (en) 2017-10-24 2021-05-11 Hanon Systems Counter flow heat exchanger

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20060524