CN1260468A - Heat exchanger - Google Patents
Heat exchanger Download PDFInfo
- Publication number
- CN1260468A CN1260468A CN 99125982 CN99125982A CN1260468A CN 1260468 A CN1260468 A CN 1260468A CN 99125982 CN99125982 CN 99125982 CN 99125982 A CN99125982 A CN 99125982A CN 1260468 A CN1260468 A CN 1260468A
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- ring plate
- fan section
- inner ring
- end socket
- 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.)
- Granted
Links
- 238000007789 sealing Methods 0.000 claims abstract description 8
- 239000004033 plastic Substances 0.000 claims description 18
- 229920003023 plastic Polymers 0.000 claims description 18
- 239000000463 material Substances 0.000 claims description 6
- 238000000926 separation method Methods 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 4
- 230000008676 import Effects 0.000 claims description 3
- 125000006850 spacer group Chemical group 0.000 claims description 3
- 238000012856 packing Methods 0.000 claims description 2
- 239000000779 smoke Substances 0.000 abstract 2
- 239000007789 gas Substances 0.000 description 15
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 10
- 239000003546 flue gas Substances 0.000 description 10
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- 230000007797 corrosion Effects 0.000 description 5
- 238000005260 corrosion Methods 0.000 description 5
- 229910000831 Steel Inorganic materials 0.000 description 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000011229 interlayer Substances 0.000 description 2
- 230000000505 pernicious effect Effects 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- AKEJUJNQAAGONA-UHFFFAOYSA-N sulfur trioxide Chemical compound O=S(=O)=O AKEJUJNQAAGONA-UHFFFAOYSA-N 0.000 description 2
- 239000002341 toxic gas Substances 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The axial-flow type haet-exchanger is characterized by that its heat-exchanger self-body is a cylindrical multi-layer spiral-plate heat-exchange structure, and the end faces of self-body are respectively equipped with six sectors and alternatively spaced sealing portions and annular spaces, and the flanges of end faces are respectively connected with uppler and lower closure heads which possess the sectors which are corresponding to the sectors of self-body and closed partially and annular channels,and its inner ring boards are formed into a smoke inlet and outlet, the smoke is fed into self-body spiral-plate layer from taper hole of upper closure head, and discharged from taper hole of lower closure head, and the air is fed into another layer of spiral plate from annular channel of upper closure head and discharged from annular channel of lower closure head to attain the goal of exchanging heat.
Description
The present invention relates to Thermal Equipment, be specifically related to a kind of boiler heat exchanger.
At present, the exhaust gas temperature of all kinds of boilers is general many more than 150 degree, contain sour composition and water vapour and contain a large amount of sulfur dioxide, sulfur trioxide and nitrogen oxide etc. in the flue gas, make the flue gas dew point temperature, higher 150 degree that reach, lower as exhaust gas temperature, then sulfuric acid, corrosion heating surface are formed in the condensation of acid gas and water vapour chance, for avoiding cold end corrosion, just must improve exhaust gas temperature, will reduce the thermal efficiency of boiler like this, simultaneously a large amount of pernicious gases be arranged to atmosphere, serious environment pollution, and waste energy.In order to address these problems, heat exchanger technology has appearred, be about to heat exchanger and be connected in all kinds of boiler tail exhaust openings, utilize the fume afterheat heating to enter the air of boiler, participate in burning, improve boiler thermal output, and the reduction exhaust gas temperature, heat exchanger now commonly used has shell-and-tube and pulls the formula heat exchanger, and shell-and-tube heat exchanger is to be inserted in the housing that steel plates surround by many steel pipes to constitute, flue gas passes through from steel pipe, and air passes through between the steel pipe from housing.Utilize tube wall to reach the heat exchange purpose, plate type heat exchanger then is that heat exchanger plates is set in housing, air and the flue gas two sides of slave plate respectively pass through, utilize wooden partition to conduct heat, reach the purpose of heat exchange, though this two classes heat exchanger can solve some boiler thermal output problems, but exist following shortcoming, if exhaust gas temperature is higher, then the exhaust gas temperature of heat exchanger is also high because structure to limit its heat exchange efficiency lower, heat-energy losses is bigger, and noxious gas emission is serious, if improve the heat exchange efficiency of heat exchanger, falls its exhaust gas temperature of the end, cold end corrosion then takes place, damage heat exchanger, simultaneously because material limit the thermal efficiency that scale formation on its heat-transfer surface also can reduce heat exchanger, snaking also is a troublesome problem.
The purpose of this invention is to provide and a kind ofly can reduce exhaust gas temperature, improve the thermal efficiency, reduce noxious gas emission, and the self-cleaning new type heat exchanger that is not corroded.
In order to achieve the above object, the present invention adopts following technical scheme: comprise heat exchanger body, the axial flow-type heat exchanger that heat exchanger plates and fluid media (medium) are imported and exported, be characterized in: heat exchanger body is the cylindrical plastic shell, establish at the shell center one with the contour plastic central post of shell, on newel, axially connect the plastics heat exchanger plates, heat exchanger plates is the center with the newel, be connected with the body housing inwall after multi-turn with certain spacer ring, forming the heat exchanger plates cross section is helical structure and the heat exchanger body with multi-layer annular space, the heat exchanger plates helix pitch is fixed with spherical or columnar stays, each is divided into the fan section of a plurality of symmetries the heat exchanger body upper and lower end face by radial many plastic sealing strips, in the fan section, replace and the annular stratiform of separation seal part space with the ring-shaped plastics sealing plate is symmetric, the upper and lower end face of heat exchanger body connects the plastic end enclosure end with flattened cylindrical shape respectively by flange, end socket be by cylindricality outer ring plate and inner ring plate and up and down ring plate surround end socket end and surround and extend the end socket top that constitutes conical through-hole and constitute by the cylindricality inner ring plate with ring packing passage.Symmetry has several medium import or exports on outer ring plate, the space symmetry division that the radial many seal diaphragms of connection surround inner ring plate on the inner ring plate inwall of end socket end becomes a plurality of fan sections and corresponding with the fan section of heat exchange body end face, end with plastics fanning strip separation seal part end socket fan section, form the seal cavity that separates with conical through-hole and communicate with heat exchanger body, have through hole and communicate with the circular passage on sealed fan-shaped inner ring plate, not sealed fan section then communicates with bellmouth.
The quantity in the body end face fan section of above-mentioned a plurality of end sockets fan section and correspondence, it optimizes quantity is 6-8.And above-mentioned plastic material is a polytetrafluoroethylene (PTFE), and other good material replaces also can to select other corrosion-resistant heat transfer for use.
Operation principle of the present invention is such, after the flue gas with uniform temperature enters exchanger head from the conical through-hole on upper cover top, axially enter a side of heat exchanger body stratiform spiral space by the end socket fan section of not sealed, disturbance through the heat exchanger plates support, enter atmosphere through the fan section that low head is not sealed from the low head bellmouth again, the flue gas owing to axially circulate, resistance is very little, flow velocity is fast, make non flouling behaviour on the heat exchanger plates, air then is that the air inlet by upper cover enters the circular passage after the through hole on the end socket inner ring plate enters the opposite side that sealed end socket fan section axially enters the stratiform spiral space of heat exchanger body again, through the sealed fan section of low head, through hole from the inner ring plate enters behind the circular passage to discharge from the low head exhaust outlet and enters boiler and participate in burning, because the annular space that flue gas and air form from spiral heat exchanger plates both sides passes through, make heat absorption of heat exchanger plates two plate faces and heat release, the temperature of high-temperature flue gas medium is passed to the air dielectric of low temperature, realize the heat exchange between two kinds of fluid media (medium)s, the spiral plate form has then increased heat exchange area, support between the spiral plate interlayer is played perturbation action to the fluid media (medium) that flows through, and has increased heat exchange efficiency.As the size that changes support also can change heat exchanger plates stratiform spacing, thereby change the heat exchange area of heat exchanger body, when needs increase heat exchange area significantly reduces exhaust gas temperature, several heat exchanger bodies can be used by the adpting flange series connection, or with the use in parallel of several heat exchangers.
Because whole parts have all adopted corrosion resistant plastic material manufacturing in the technique scheme; adopted last low head that the heat exchanger body structure of fan section and spiral heat exchanger plates is set again; make this heat exchanger heat exchange efficiency height; reduced effectively condensation pernicious gas of exhaust gas temperature and energy; and do not corroded; reduced to the airborne release harmful substance; according to surveying and determination in the flue gas that this heat exchanger is discharged; content of sulfur dioxide reduces 20-30%; amount of nitrogen oxides reduces 15-20%, and boiler thermal output can improve more than 5%, and effect is obvious; reached the saving energy, protection environment and the purpose that prolongs the heat exchanger life-span.
Below in conjunction with accompanying drawing in detail the present invention is described in detail:
Fig. 1 is a structural representation of the present invention.
Fig. 2 is the fan section schematic diagram of heat exchanger body end face of the present invention.
Fig. 3 is the fan section schematic diagram in the end socket of the present invention.
Fig. 1 and Fig. 2 and Fig. 3 demonstrate the structure of this heat exchanger, comprise heat exchanger body (1), end socket (4) spiral heat exchanger plates (2) and flue gas medium import (7), outlet (19), air intlet (10), air outlet slit (13), in the shell of heat exchanger body (1) newel is set, on newel, connect heat exchanger plates (2), heat exchanger plates one end axially is connected on the newel, and be connected with the body housing inwall around 6 circle backs with 3 millimeters spacer ring around newel, constitute the spiral plate structure, diameter is that 3 millimeters annular brace (8) is fixed in spiral plate (2) interlayer, the upper and lower end face of heat exchanger body (1) is divided into the fan section of 6 symmetries by radial 6 sealing strips, on the fan section with annular sealing plate (12) symmetric alternately and separation seal part fan section form a plurality of annular stratiforms spaces (11), from Fig. 2, can find out this structure in detail, heat exchanger body (1) upper and lower side connects the end of the last low head (4) with oblate post respectively by flange, the end of last low head (4) is by outer ring plate and inner ring plate and goes up the structure with circular passage (9) that lower annular plate surrounds, on the periphery of outer ring plate, be provided with the air intlet (10) of 3 symmetries, and air outlet slit (13), on the inner ring plate inwall, connect to be and put radial 6 seal diaphragms, the space segmentation that inner ring plate is surrounded becomes 6 fan sections (5), 6 end socket fan sections are corresponding with heat exchanger body end face fan section, with the end in fan-shaped sealing plate (6) three end socket fan sections of separation seal (5), Fig. 3 then demonstrates this structure.Having through hole (3) on the sealed fan section inner ring plate communicates with circular passage (9), the annular inner ring plate extends to the exhanst gas outlet (14) that end socket (4) top constitutes upper cover gas approach (7) and low head, each parts are telfon plastic in the above-mentioned heat exchanger, and this heat exchanger also can be used for paper industry, chemical industry except that being used for all kinds of boiler waste gas waste heat recoveries and purifying waste gas residual heat reclaims and purifies.
Claims (3)
1. heat exchanger, comprise heat exchanger body, the axial flow-type heat exchanger that heat exchanger plates and fluid media (medium) are imported and exported, it is characterized in that: heat exchanger body (1) is the cylindrical plastic shell, establish at the shell center one with the contour plastic central post of shell, on newel, axially connect plastics heat exchanger plates (2), heat exchanger plates is that the center is connected with the body housing inwall after multi-turn with certain spacer ring with the newel, forming heat exchanger plates (2) cross section is helical structure and the heat exchanger body (1) with multi-layer annular space (11), the heat exchanger plates helix pitch is fixing with spherical or columnar stays (8), each is divided into the fan section of a plurality of symmetries heat exchanger body (1) upper and lower end face by radial many plastic sealing strips, in the fan section, replace and the annular stratiform of separation seal part space (11) with ring-shaped plastics sealing plate (12) is symmetric, the upper and lower end face of heat exchanger body (1) connects plastic end enclosure (4) end with flattened cylindrical shape respectively by flange, end socket (4) be by cylindricality outer ring plate and inner ring plate and up and down ring plate surround end socket end and surround and extend the end socket top that constitutes conical through-hole and constitute by the cylindricality inner ring plate with ring packing passage (9).Symmetry has several medium import or exports on outer ring plate, the space symmetry division that the radial many seal diaphragms of connection surround inner ring plate on the inner ring plate inwall of end socket end becomes a plurality of fan sections and corresponding with the fan section of heat exchange body end face, end with plastics fanning strip (6) separation seal part end socket fan section, form the seal cavity that separates with conical through-hole and communicate with heat exchanger body (1), have through hole (3) and communicate with circular passage (9) on sealed fan-shaped inner ring plate, not sealed fan section then communicates with bellmouth.
2. heat exchanger according to claim 1 is characterized in that: described end socket fan section and corresponding body end face fan section its optimal value of number are 6-8.
3. heat exchanger according to claim 1 is characterized in that: described plastic material is a polytetrafluoroethylmaterial material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99125982 CN1099577C (en) | 1999-12-10 | 1999-12-10 | heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99125982 CN1099577C (en) | 1999-12-10 | 1999-12-10 | heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1260468A true CN1260468A (en) | 2000-07-19 |
| CN1099577C CN1099577C (en) | 2003-01-22 |
Family
ID=5284268
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 99125982 Expired - Fee Related CN1099577C (en) | 1999-12-10 | 1999-12-10 | heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1099577C (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103547879A (en) * | 2011-03-07 | 2014-01-29 | 阿威德热合金有限公司 | Thermal transfer device with spiral fluid pathways |
| CN104457346A (en) * | 2013-09-25 | 2015-03-25 | 王心宇 | Heat exchange device |
| CN105318752A (en) * | 2015-11-04 | 2016-02-10 | 兰州兰洛炼化设备有限公司 | End face double-sealing spiral plate type high-temperature flue gas reboiler |
| CN109579049A (en) * | 2018-12-29 | 2019-04-05 | 苏州协宏泰节能科技有限公司 | The board-like turbogenerator heat exchanger of annular |
| CN109579051A (en) * | 2018-12-29 | 2019-04-05 | 苏州协宏泰节能科技有限公司 | Screen plate propeller for turboprop machine heat exchanger |
| CN113503752A (en) * | 2021-06-16 | 2021-10-15 | 东风汽车股份有限公司 | Multiphase fluid temperature changing device |
| CN116072318A (en) * | 2023-01-18 | 2023-05-05 | 哈尔滨工程大学 | Multi-loop brayton cycle energy conversion system for heat pipe stacks and method of operation |
-
1999
- 1999-12-10 CN CN 99125982 patent/CN1099577C/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103547879A (en) * | 2011-03-07 | 2014-01-29 | 阿威德热合金有限公司 | Thermal transfer device with spiral fluid pathways |
| CN103547879B (en) * | 2011-03-07 | 2016-03-16 | 阿威德热合金有限公司 | There is the heat-transfer arrangement of helical fluid path |
| CN104457346A (en) * | 2013-09-25 | 2015-03-25 | 王心宇 | Heat exchange device |
| CN105318752A (en) * | 2015-11-04 | 2016-02-10 | 兰州兰洛炼化设备有限公司 | End face double-sealing spiral plate type high-temperature flue gas reboiler |
| CN105318752B (en) * | 2015-11-04 | 2017-04-12 | 兰州兰洛炼化设备有限公司 | End face double-sealing spiral plate type high-temperature flue gas reboiler |
| CN109579049A (en) * | 2018-12-29 | 2019-04-05 | 苏州协宏泰节能科技有限公司 | The board-like turbogenerator heat exchanger of annular |
| CN109579051A (en) * | 2018-12-29 | 2019-04-05 | 苏州协宏泰节能科技有限公司 | Screen plate propeller for turboprop machine heat exchanger |
| CN113503752A (en) * | 2021-06-16 | 2021-10-15 | 东风汽车股份有限公司 | Multiphase fluid temperature changing device |
| CN116072318A (en) * | 2023-01-18 | 2023-05-05 | 哈尔滨工程大学 | Multi-loop brayton cycle energy conversion system for heat pipe stacks and method of operation |
| CN116072318B (en) * | 2023-01-18 | 2024-01-23 | 哈尔滨工程大学 | Multi-loop brayton cycle energy conversion system for heat pipe stacks and method of operation |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1099577C (en) | 2003-01-22 |
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| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C06 | Publication | ||
| PB01 | Publication | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |