CN2181669Y - Separated heat pipe with recirculation pipe - Google Patents

Separated heat pipe with recirculation pipe Download PDF

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Publication number
CN2181669Y
CN2181669Y CN 93245949 CN93245949U CN2181669Y CN 2181669 Y CN2181669 Y CN 2181669Y CN 93245949 CN93245949 CN 93245949 CN 93245949 U CN93245949 U CN 93245949U CN 2181669 Y CN2181669 Y CN 2181669Y
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CN
China
Prior art keywords
pipe
heat pipe
utility
collecting box
model
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Expired - Fee Related
Application number
CN 93245949
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Chinese (zh)
Inventor
曹子栋
沈月芬
庄正宁
陈立勋
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Xian Jiaotong University
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Xian Jiaotong University
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Publication date
Application filed by Xian Jiaotong University filed Critical Xian Jiaotong University
Priority to CN 93245949 priority Critical patent/CN2181669Y/en
Application granted granted Critical
Publication of CN2181669Y publication Critical patent/CN2181669Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a separated heat pipe with a recirculation pipe. The utility model comprises an evaporation section and a condensing section which is matched with the evaporation section. The evaporation section comprises an upper collecting box, a lower collecting box, an evaporating pipe (5) and a recirculation pipe which are arranged between the upper collecting box and the lower collecting box. The upper collecting box is provided with a subminiature separator which can ensure that the dryness of the steam which goes into the condensation section is 1. The complicated site hot state adjustment can be replaced by the disposable liquid. The utility model can automatically adapt the change of the heat pipe heat exchange loading, especially for the process of the starting and the stoppage. The utility model thoroughly solves the heat pipe safety trouble caused by the heat transferring deterioration of the working solution.

Description

Separated heat pipe with recirculation pipe
The utility model relates to a kind of heat pipe, particularly a kind of separate heat pipe.
Separate heat pipe is 80 a kind of heat pipe application technologies for new development, it had both had the basic heat exchange property of monoblock type thermal siphon heat pipe, have again big, the hot fed distance of heat exchange power far away, as design of heat exchanger arrangement convenience and other special benefits, (the document: " branch news formula Study of Heat Pipe Heat Exchanger use with estimate " of in large-scale heat exchange of heat pipe, being used widely, Chen Yuanguo, 1988,9 second heat pipe China proceeding P225).But at present domestic and international applied separate heat pipe all adopts the natural circulation mode of circulating ratio K=1, and this has all proposed strict requirement for the steam quality that enters condensation segment and evaporator section working solution to the infiltration degree of the whole pipe range that is heated.If it is bigger to enter the steam moisture of condensation segment, promptly there is liquid to bring into, the condensation segment liquid film is thickeied rapidly, worsen the condensation exothermic process, causing whole piping operating pressure to raise influences the safe operation of heating surface.If it is not enough that the evaporator section working solution soaks into whole pipe range, certainly will cause certain section evaporation tube " dry combustion method ", cause wall temperature to raise and the mechanical strength reduction of material, not only influence the heat exchange efficiency of heat pipe but also the safe operation of entail dangers to equipment.Take place for fear of above-mentioned phenomenon, domestic scholars all is devoted to seek one rational " liquid filled ratio " (being the ratio R that the cold conditions working solution accounts for evaporator section length and whole evaporator section pipe range).And liquid filled ratio R not only has also with the pepeline characteristic of heat transmission equipment, also relevant with the thermic load of heat pipe, a well-known cover separate type heat pipe exchanger all is made up of several groups of independence device roads, every group of loop thermic load is all inequality, this just requires every group of liquid filled ratio all should change, and does not have the operation debugging of coagulating to heat pipe and brings difficulty.In addition, heat pipe is in running, and particularly thermic load is to change in time in the start-up course, and the adjustment of liquid filled ratio at this moment is just more difficult.
The purpose of this utility model is to overcome the shortcoming of above-mentioned prior art, has proposed the irrelevant separate heat pipe of a kind of liquid filled ratio and thermic load, guarantees that entering the condensation segment steam quality is 1, thereby the evaporator section heating surface is had protective effect efficiently.
Fig. 1 is a structure principle chart of the present utility model.
Fig. 2 be microminiature separator 2 partial enlarged drawing,
Below in conjunction with accompanying drawing the utility model structural principle and operation principle are done detailed explanation.
The utility model comprises an evaporator section 8, and evaporator section 8 is connected with condensation segment 10 by the steam fairlead, and the next part case 9 of condensation segment 10 is connected with the next part case 6 of evaporator section 8 by saturated solution inlet tube 7.Said evaporator section 8 comprise one with the upper collecting chamber of steam fairlead 1 phase configuration, with the next part case 6 of saturated solution inlet tube 7 phase configuration, 6 in upper collecting chamber 3 and next part case dispose evaporation tube 5 and recirculation pipe 4,1 of upper collecting chamber 3 and steam fairlead dispose microminiature separator 2, and said microminiature separator 2 is formed with the tangent guide vane 11 of steam fairlead 1 by one group.
Microminiature separator 2 is principles of utilizing free vortex to form.With outside upper collecting chamber 3 is connected, one group of guide vane 11 axially is set at steam fairlead 1, impels the steam water interface rotation that enters steam fairlead 1, thereby reach the effect that carbonated drink is separated along collector.Recirculation pipe 4 is not heated, be full state in the pipe, it is communicated with evaporation tube 5 and causes the two heavily to have pressure reduction on the height of position, thereby guarantee the descending motion of the working solution of upper collecting chamber 3, promote evaporation tube 5 working solutions to move upward, (K=1 loop) adds a closed circuit again on whole heat pipe closed circuit, thereby guaranteed the trouble free service of evaporation tube 5.
The utility model does not have under the big change condition in existing separate heat pipe structure, and available disposable topping up replaces miscellaneous on-the-spot hot adjustment.The utility model can adapt to the variation of heat pipe heat exchanging load automatically, particularly starts and the stoppage in transit process, has thoroughly solved the heat pipe safety obstacle that the heat transfer deterioration because of working solution causes.
The used blast furnace coal of certain 220T/ high pressure blast furnace coal boiler furnace vapour heater, jeopardize personal safety for preventing that blast furnace gas from leaking to reveal, must adopt separate heat pipe as heat exchange element, 5 every groups 2 of heat exchange power N=15000KW recirculation pipes, diameter phi=65 millimeter, wall thickness=3.5 millimeters totally 22 groups, every steam fairlead is furnished with the microminiature separator, the high h=25 millimeter of its guide vane, 200 millimeters of length L, pitch angle alpha will=45 ° axial symmetry arranges, vane thickness=4 millimeter, the disposable topping up in the whole loops of liquid filled ratio R=45%().

Claims (2)

1, the separate heat pipe that has recirculation pipe, comprise an evaporator section (8), evaporator section (8) is connected with condensation segment (10) by steam fairlead (1), the next part case (9) of condensation segment (10) is connected with the next part case (6) of evaporator section (8) by saturated solution inlet tube (7), feature of the present utility model is, said evaporator section (8) comprise one with the upper collecting chamber (3) of steam fairlead (1) phase configuration, with the next part case (6) of saturated solution inlet tube (7) phase configuration, dispose evaporation tube (5) and recirculation pipe (4) between upper collecting chamber (3) and next part case (6).
2, separate heat pipe according to claim 1, it is characterized in that, dispose microminiature separator (2) between said upper collecting chamber (3) and steam fairlead (1), said microminiature separator (2) is formed with the tangent guide vane (11) of steam fairlead (1) by one group.
CN 93245949 1993-12-01 1993-12-01 Separated heat pipe with recirculation pipe Expired - Fee Related CN2181669Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 93245949 CN2181669Y (en) 1993-12-01 1993-12-01 Separated heat pipe with recirculation pipe

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 93245949 CN2181669Y (en) 1993-12-01 1993-12-01 Separated heat pipe with recirculation pipe

Publications (1)

Publication Number Publication Date
CN2181669Y true CN2181669Y (en) 1994-11-02

Family

ID=33818756

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 93245949 Expired - Fee Related CN2181669Y (en) 1993-12-01 1993-12-01 Separated heat pipe with recirculation pipe

Country Status (1)

Country Link
CN (1) CN2181669Y (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100386587C (en) * 2006-06-12 2008-05-07 北京科技大学 Pump-free self-circulation non-vacuum split type gravity heat pipe
CN100424457C (en) * 2006-06-20 2008-10-08 青岛大学 Controllable bi-circulating hot-pipe system
CN100443850C (en) * 2007-02-15 2008-12-17 南京工业大学 Heat pipe type solid phase powder heat exchange system
CN102087053A (en) * 2011-03-04 2011-06-08 浙江大学 Solar flat plate collector capable of exchanging heat through micro-channel
CN102116588A (en) * 2011-03-04 2011-07-06 浙江大学 Evaporation and heat conduction device with micro passageway
CN106197102A (en) * 2016-08-29 2016-12-07 何其伦 Steam chest type adopting heat pipes for heat transfer mechanism

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100386587C (en) * 2006-06-12 2008-05-07 北京科技大学 Pump-free self-circulation non-vacuum split type gravity heat pipe
CN100424457C (en) * 2006-06-20 2008-10-08 青岛大学 Controllable bi-circulating hot-pipe system
CN100443850C (en) * 2007-02-15 2008-12-17 南京工业大学 Heat pipe type solid phase powder heat exchange system
CN102087053A (en) * 2011-03-04 2011-06-08 浙江大学 Solar flat plate collector capable of exchanging heat through micro-channel
CN102116588A (en) * 2011-03-04 2011-07-06 浙江大学 Evaporation and heat conduction device with micro passageway
CN102087053B (en) * 2011-03-04 2012-07-25 浙江大学 Solar flat plate collector capable of exchanging heat through micro-channel
CN106197102A (en) * 2016-08-29 2016-12-07 何其伦 Steam chest type adopting heat pipes for heat transfer mechanism

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C19 Lapse of patent right due to non-payment of the annual fee
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