CN2384188Y - Reducing flow area heat exchanger - Google Patents
Reducing flow area heat exchanger Download PDFInfo
- Publication number
- CN2384188Y CN2384188Y CN 99229134 CN99229134U CN2384188Y CN 2384188 Y CN2384188 Y CN 2384188Y CN 99229134 CN99229134 CN 99229134 CN 99229134 U CN99229134 U CN 99229134U CN 2384188 Y CN2384188 Y CN 2384188Y
- Authority
- CN
- China
- Prior art keywords
- tube
- pipe
- heat
- roundtrip
- cooling section
- 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
Links
Images
Abstract
The utility model relates to a reducing flow area heat exchanger, which is mainly composed of a housing body, a pipe box, a pipe plate, a heat exchange pipe bundle, a pass partition plate, a baffle plate, a draw rod, a distance sink pipe, a supporting seat, etc. The planes of bending of all U-shaped pipes of the heat exchange pipe bundle are all in horizontal arrangement; a pipe pass steam condensing section in the heat exchange pipe bundle is partitioned into a double return passages or a multi-return passages with different flow passage area, and the flow area of the latter return passage is smaller the flow area of former of the return passage; ports of all U-shaped heat exchange pipe on the side of the pipe box of a pipe pass condensed water cooling section are in sequence communicated with each other via an outlet and an inlet of a single pipe or outlets and inlets of multiple pipes, and condensed water flow passages with the single pipe or the multiple pipes of the cooling section can be formed.
Description
The utility model relates to the heat transmission equipment in fields such as a kind of chemical industry, medicine, HVAC, weaving, is the shell-and-tube heat exchanger that heating agent heats other medium with water vapour (or gas of similar water steam) especially.
Up to now, be that the condensate water heat recovery problem of the heating agent heat exchanger that heats other medium never has the rational solution of less expensive with the water vapour.Centering, low pressure water vapor if its condensate water is cooled to 50 ℃ from saturation temperature, can reclaim 20% heat approximately.But in fact the heat recovery of condensate water is unsatisfactory, mainly has following problem:
One, if in same heat exchanger, reclaim the heat of condensate water, water vapour is walked tube side, heated medium is walked shell side, because the water vapour condensation segment is identical with the tube side circulation area of its condensate water cooling section, the volume of condensate water is much smaller than the volume of its steam, thereby the condensate water flow velocity in the cooling section heat exchanger tube is very low, the tube fluid film heat transfer coefficient is little, so heat exchanger cooling section overall heat-transfer coefficient is little.Adding hot water with water vapour is example, and its cooling section overall heat-transfer coefficient is about 300kcal/ (m
2H ℃).This means that will reclaim 20% heat need increase about 1 times heat exchange area, equipment investment increases.If water vapour is walked shell side, heated medium is walked tube side, and the circulation area than tube side is big usually owing to the shell side circulation area, and the flow velocity of condensate water is lower, so the recovery of its heat is more unrealistic.
They are two years old, if being introduced another heat exchanger, the condensate water under the saturation temperature make its continuation cooling reclaim heat, although can improve overall heat-transfer coefficient, the more above-mentioned situation of heat exchange area little, but, must increase equipment investment and operating maintenance expense owing to increased a heat exchanger and respective valves pipe fitting etc.
In addition, the heat exchanging process only is the heat exchanger of condensation heat transfer (latent heat of vaporization that heated medium only absorbs water vapour does not absorb the condensate water heat), because water vapour constantly is condensed, the vapour amount reduces gradually, and the circulation passage area is constant, thereby its flow velocity reduction, and film coefficient of heat transfer also decreases.
The purpose of this utility model provides a kind of heat exchanger with reducing channel area, make water vapour roundtrip behind the tube side condensation segment still maintain high flow velocities, and significantly improve the flow velocity of its condensate water at the tube side cooling section, thereby raising overall heat-transfer coefficient, reduce investment outlay and the energy, less expensive is reasonably realized the condensation of tube side water vapour (or gas of similar water steam) and cooling, the heated heat transfer process of shell side medium of condensate water (liquid) thereof with the separate unit heat exchanger.
Technical solution of the present utility model:
A kind of heat exchanger with reducing channel area, it is mainly by housing, bobbin carriage, tube sheet, heat-exchanging tube bundle, pass partition, deflection plate, pull bar, composition such as distance sink tube and bearing, heat-exchanging tube bundle is made up of many U-shaped pipes, bobbin carriage is provided with water vapour inlet tube and condensate water outlet, be provided with pass partition in the bobbin carriage, housing is provided with heated medium inlet tube and heated medium outlet, pass partition (in case of necessity) also can be set in the housing, the equal horizontal positioned of plane of bending that it is characterized in that each U-shaped pipe of heat-exchanging tube bundle, tube side water vapour condensation segment in the heat-exchanging tube bundle is divided into the different two roundtrips of circulation passage area (water vapour flow into to flow out at U-shaped Guan Zhongcong and is called 1 roundtrip) or many roundtrips circulation passage by pass partition, and the circulation area of the more last roundtrip passage of back one roundtrip passage is little; Export and import with single tube or multitube between each U-shaped heat exchanger tube mouth of pipe of the tube case side of tube side condensate water cooling section interconnects connection successively with the bustle pipe circle, forms the single tube or the multitube condensate water circulation passage of cooling section integral body.
The advantage of the logical area heat exchanger of unsteady flow of the present utility model: the circulation area of a roundtrip diminishes behind the water vapour condensation segment, make water vapour because condensation and under the situation that the vapour amount reduces, one roundtrip still keeps higher flow velocity in the back: condensate water can only flow in single tube that circulation area diminishes or multitube condensate water circulation passage at cooling section, and its flow velocity significantly improves.Adopt the bustle pipe circle to connect the single tube or the multitube condensate water circulation passage of cooling section integral body, the spacing that heat exchanger tube is arranged is consistent with tube pitch commonly used.By diminishing of water vapour condensation segment and condensate water cooling section circulation area, can make the overall heat-transfer coefficient of heat exchanger improve about 60%, reduce investment outlay about 10%～40%, energy-conservation about 20%, but less expensive is reasonably realized the condensation of tube side water vapour (or gas of similar water steam) and cooling, the heated technical process of shell side medium of condensate water (liquid) thereof with the separate unit heat exchanger.
Below in conjunction with drawings and Examples, the logical area heat exchanger of unsteady flow of the present utility model is further described:
Fig. 1 looks schematic diagram for structure master of the present utility model;
Fig. 2 is the structure schematic top plan view of Fig. 1;
Fig. 3 looks the B-B generalized section for the structure left side of Fig. 1;
Fig. 4 is the local enlarged diagram of Fig. 3;
Fig. 5 is the C-C generalized section of Fig. 4.
Shown in Fig. 1～5, the utility model mainly is made up of housing 11, bobbin carriage 5, tube sheet 4, heat-exchanging tube bundle 12, deflection plate 13, pull bar 15, distance sink tube 14 and bearing 18.Heat-exchanging tube bundle 12 is many U-shaped pipes, and U-shaped canal curvature planar horizontal is placed, and is installed with deflection plate 13 on it, and deflection plate 13 is fixed its position by the pull bar 15, nut 16 and the distance sink tube 14 that are fixed on the tube sheet 4.Each U-shaped pipe passes tube sheet, end and tube plate expanded-connecting or be welded to connect.Heat-exchanging tube bundle 12 is inserted in the housing 11, and flange 9, double-screw bolt 7 and nut 8 grip tube sheet 4, and bobbin carriage 5 and housing 11 are connected as one.Bobbin carriage 5 is provided with water vapour inlet tube 6 and condensate water outlet 1, is provided with pass partition 2,3 and 19 in it.Housing 11 is provided with heated medium inlet tube 17 and heated medium outlet 10, and housing 11 is welded to connect with bearing 18.Of the present utility model being characterised in that: tube side water vapour condensation segment is divided into two roundtrips or many roundtrips circulation road by pass partition 2,3,19, the radical of the U-shaped pipe of back one roundtrip channel water steam inlet 21 is less than the U-shaped pipe radical of last roundtrip channel water steam (vapor) outlet 20, and promptly the circulation area of back one roundtrip passage is less than the circulation area of last roundtrip passage; The condensate water cooling section that communicates with the outlet 24 of water vapour condensation segment U-shaped pipe keeps the import of single or multiple U-shaped pipes, export and import with single tube or multitube between all the other each U-shaped pipe mouths of pipe interconnects connection successively, forms the single tube or the multitube condensate water circulation passage of cooling section integral body.
In the utility model, the single tube condensate water circulating channel structure that each U-shaped pipe of condensate water cooling section heat-exchanging tube bundle forms is, keep the import 25 that exports a U-shaped pipe in the 24 cooling section heat-exchanging tube bundles that communicate with the condensation segment heat-exchanging tube bundle, the import of another U-shaped pipe of outlet and homonymy of this U-shaped pipe of the pass partition opposite side connection that is connected, in like manner connect remaining U-shaped pipe, keep at last the outlet 22 of a U-shaped pipe at the opposite side of the import of cooling section U-shaped pipe, form holistic single tube condensate water circulation passage, be this structure shown in Fig. 3,4 and 5.
The multitube condensate water circulating channel structure that each U-shaped pipe of condensate water cooling section heat-exchanging tube bundle forms is, keep the import that exports the two or more U-shaped pipes in the 24 cooling section heat-exchanging tube bundles that communicate with the condensation segment heat-exchanging tube bundle, the outlet of the two or more U-shaped pipes of this of pass partition opposite side, connection is connected with the import of other two or more U-shaped pipes of homonymy, in like manner connect remaining U-shaped pipe, keep at last the outlet of two or more U-shaped pipes, form holistic two or more multitube condensate water circulation passage at the opposite side of the import of cooling section U-shaped pipe.
In the utility model, the structure of the two roundtrip circulation passages of water vapour condensation segment is, the import 23,21 of water vapour condensation segment heat-exchanging tube bundle U-shaped pipe and export 20,24, be separated to form the two roundtrip circulation passages of water vapour condensation segment by pass partition 2,3 and 19, the radical of the U-shaped pipe of back one roundtrip water vapour import 21 is less than the U-shaped pipe radical of last roundtrip steam outlet 20, promptly the circulation area of back one roundtrip is less than the circulation area of last roundtrip, shown in Figure 3ly is this structure.
The structure of many roundtrips of water vapour condensation segment circulation passage is, the import and the outlet of water vapour condensation segment heat-exchanging tube bundle U-shaped pipe, be separated to form three of water vapour condensation segments or three above roundtrip circulation passages by some pass partitions, the radical of the U-shaped pipe of each back roundtrip water vapour import is less than the U-shaped pipe radical of its last roundtrip steam outlet, and promptly the circulation area of each back roundtrip is less than the circulation area of its last roundtrip.
The water vapour condensation segment adopts two roundtrips or many roundtrips structure, and the condensate water cooling section adopts single tube or multitube condensate water circulating channel structure, decides on the size that the size and the tube side pressure of water vapour or condensing water flow falls.Like this, not only water vapour can keep higher flow velocity at condensation segment, and condensate water greatly improves at the flow velocity of cooling section, thereby the overall heat-transfer coefficient of heat exchanger is significantly improved.
In the utility model, the import of each U-shaped pipe and being connected of outlet in the condensate water cooling section heat-exchanging tube bundle, can adopt the structure that is welded between bustle pipe circle 20 that sheet metal makes and the tube sheet 4 to connect, be this structure shown in the Figure 4 and 5, also can adopt other connector to connect.
The heat exchange course of work of heat exchanger with reducing channel area of the present utility model is as follows:
After water vapour enters bobbin carriage 5 by inlet tube 6, flow with certain speed from being flowed into the U-shaped pipe by the import 23 of tube pass partition 3 and the 19 condensation segment heat-exchanging tube bundles of separating, the part water vapour is condensed into condensate water, the latent heat of vaporization of emitting is passed to the outer heated medium of pipe by the heat exchange tube wall, remaining water vapour flows out from U-shaped pipe outlet 20 after a roundtrip, in the inflow import 21 with heat-exchanging tube bundles U-shaped pipe outlet 20 next roundtrip of condensation segment that communicate that separate by pass partition 2 and 19, because the quantity of the U-shaped pipe outlet 20 of the more last roundtrip of quantity of the U-shaped pipe import 21 of back one roundtrip is few, circulation area is little, thereby remaining water vapour the back one roundtrip still can maintain higher flow velocity, heat transfer coefficient is also higher.Through after behind the condensation heat transfer of a roundtrip, water vapour all is condensed into condensate water, after the outlet 24 of condensate water heat-exchanging tube bundle of a roundtrip behind the condensation segment is flowed out, inflow is by the single tube or the multitube import 25 of pass partition 3 and the 19 cooling section heat-exchanging tube bundles of separating that communicate with its outlet, repeatedly come and go in the single tube of cooling section or multitube circulation passage with higher flow velocity and to flow, by the heat exchange tube wall heat is passed to the outer heated medium of pipe, be cooled to suitable temperature at last, flow out from the outlet 22 of cooling section heat-exchanging tube bundle, through outlet 1 outflow heat exchanger.In the water vapour condensation with condense the water-cooled while, heated medium flows in the housings 11 through inlet tube 17, and is repeatedly mobile heat-exchanging tube bundle 12 outside around deflection plate 13, the transversal flow heat-exchanging tube bundle, absorption is by the heat that tube wall spreads out of, reach heated temperature after, through outlet 10 outflow heat exchangers.
Claims (6)
1, a kind of heat exchanger with reducing channel area, it is mainly by housing, bobbin carriage, tube sheet, heat-exchanging tube bundle, pass partition, deflection plate, pull bar, composition such as distance sink tube and bearing, heat-exchanging tube bundle is made up of many U-shaped pipes, bobbin carriage is provided with water vapour inlet tube and condensate water outlet, be provided with pass partition in the bobbin carriage, housing is provided with heated medium inlet tube and heated medium outlet, the equal horizontal positioned of plane of bending that it is characterized in that each U-shaped pipe of heat-exchanging tube bundle, tube side water vapour condensation segment in the heat-exchanging tube bundle is divided into the different two roundtrips of circulation passage area or many roundtrips circulation passage by pass partition, and the circulation area of the more last roundtrip passage of back one roundtrip passage is little; Export and import with single tube or multitube between each U-shaped heat exchanger tube mouth of pipe of the tube case side of tube side condensate water cooling section interconnects connection successively with the bustle pipe circle, forms the single tube or the multitube condensate water circulation passage of cooling section integral body.
2, by the described heat exchanger with reducing channel area of claim 1, it is characterized in that the single tube condensate water circulating channel structure that each U-shaped pipe of tube side condensate water cooling section heat-exchanging tube bundle forms is, keep the import of a U-shaped pipe in the cooling section heat-exchanging tube bundle that communicates with the outlet of condensation segment heat-exchanging tube bundle, the import of another U-shaped pipe of outlet and homonymy of this U-shaped pipe of the pass partition opposite side connection that is connected, in like manner connect remaining U-shaped pipe, keep at last the outlet of a U-shaped pipe, form holistic single tube condensate water circulation passage at the opposite side of the import of cooling section U-shaped pipe.
3, by the described heat exchanger with reducing channel area of claim 1, it is characterized in that the multitube condensate water circulating channel structure that each U-shaped pipe of tube side condensate water cooling section heat-exchanging tube bundle forms is, keep the import of the two or more U-shaped pipes in the cooling section heat-exchanging tube bundle that communicates with the outlet of condensation segment heat-exchanging tube bundle, the outlet of the two or more U-shaped pipes of this of pass partition opposite side, connection is connected with the import of other two or more U-shaped pipes of homonymy, in like manner connect remaining U-shaped pipe, keep at last the outlet of two or more U-shaped pipes, form holistic two or more multitube condensate water circulation passage at the opposite side of the import of cooling section U-shaped pipe.
4,, it is characterized in that the import of each U-shaped pipe in the tube side cooling section heat-exchanging tube bundle and bustle pipe circle and tube sheet welded structure that outlet adopts sheet metal to make connect by claim 1 or 2 or 3 described heat exchanger with reducing channel area.
5, by claim 1 or 2 or 3 described heat exchanger with reducing channel area, it is characterized in that tube side water vapour condensation segment is divided into two roundtrip circulation passages by pass partition, the circulation passage area difference of each roundtrip, the circulation area of the more last roundtrip of back one roundtrip is little.
6. by claim 1 or 2 or 3 described heat exchanger with reducing channel area, it is characterized in that tube side water vapour condensation segment separated many roundtrips circulation passage by pass partition, the circulation passage area difference of each roundtrip, each back roundtrip is little than the circulation area of its last roundtrip.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99229134 CN2384188Y (en) | 1999-08-12 | 1999-08-12 | Reducing flow area heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99229134 CN2384188Y (en) | 1999-08-12 | 1999-08-12 | Reducing flow area heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2384188Y true CN2384188Y (en) | 2000-06-21 |
Family
ID=34018413
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 99229134 Expired - Fee Related CN2384188Y (en) | 1999-08-12 | 1999-08-12 | Reducing flow area heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2384188Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100419366C (en) * | 2005-07-27 | 2008-09-17 | 西安华广电站锅炉有限公司 | High efficiency plate pipe reverse running type square box heat exchanger |
| CN100567874C (en) * | 2005-08-18 | 2009-12-09 | 株式会社东芝 | Moisture separation heater |
| CN101943540A (en) * | 2009-07-06 | 2011-01-12 | 巴伯考克博斯格服务股份有限公司 | The tubular type adjuster that is used for indirect heat exchange |
| CN103615843A (en) * | 2013-11-22 | 2014-03-05 | 昆山方佳机械制造有限公司 | Novel dry-type evaporator and application method thereof |
| CN103673683A (en) * | 2013-12-30 | 2014-03-26 | 张家港市江南锅炉压力容器有限公司 | Multi-shell-pass recycle gas condenser |
| CN110822952A (en) * | 2019-12-03 | 2020-02-21 | 南通兆华机械制造有限公司 | Four-tube-pass heat exchanger arranged in inclined mode |
-
1999
- 1999-08-12 CN CN 99229134 patent/CN2384188Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100419366C (en) * | 2005-07-27 | 2008-09-17 | 西安华广电站锅炉有限公司 | High efficiency plate pipe reverse running type square box heat exchanger |
| CN100567874C (en) * | 2005-08-18 | 2009-12-09 | 株式会社东芝 | Moisture separation heater |
| US7857895B2 (en) | 2005-08-18 | 2010-12-28 | Kabushiki Kaisha Toshiba | Moisture separation heater |
| CN101943540A (en) * | 2009-07-06 | 2011-01-12 | 巴伯考克博斯格服务股份有限公司 | The tubular type adjuster that is used for indirect heat exchange |
| CN101943540B (en) * | 2009-07-06 | 2013-07-10 | 巴伯考克博斯格服务股份有限公司 | Tube register for indirect heat exchange |
| CN103615843A (en) * | 2013-11-22 | 2014-03-05 | 昆山方佳机械制造有限公司 | Novel dry-type evaporator and application method thereof |
| CN103673683A (en) * | 2013-12-30 | 2014-03-26 | 张家港市江南锅炉压力容器有限公司 | Multi-shell-pass recycle gas condenser |
| CN110822952A (en) * | 2019-12-03 | 2020-02-21 | 南通兆华机械制造有限公司 | Four-tube-pass heat exchanger arranged in inclined mode |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104864747A (en) | Energy-saving heating network heater | |
| CN2384188Y (en) | Reducing flow area heat exchanger | |
| CN201106994Y (en) | Asymmetry type high-efficiency condenser | |
| CN104930882A (en) | U-shaped pipe energy-saving heater for heating network | |
| CN110057215A (en) | A kind of high temperature and pressure sand heat-exchanger rig | |
| CN202757502U (en) | Hot medium self-circulating heat exchanger with adjustable load | |
| CN1284646A (en) | Heat exchanger with reducing channel area | |
| EP4279849A1 (en) | Steam heat exchanger | |
| CN202973674U (en) | Heat recycling type shell tube type condenser | |
| CN2196773Y (en) | Multiple-effect heat exchanger | |
| CN100582607C (en) | Liquid division type double-pipe condenser | |
| CN210292446U (en) | Refrigeration cycle condenser using water as refrigerant | |
| CN2372651Y (en) | Changeable cross-section positive displacement heat exchanger | |
| CN208075628U (en) | Biflow path pipe shell-type exchangers | |
| CN209214394U (en) | A kind of condenser with four processes | |
| CN102980332B (en) | Heat recovery shell and tube condenser | |
| CN112229233A (en) | Two-section type heat conduction oil recovery heat exchanger for groove type photo-thermal power plant | |
| CN2723428Y (en) | Large plate type evaporator | |
| TW552395B (en) | Constant flow velocity vapor-liquid heat exchanger | |
| CN1502954A (en) | All fins heat-exchanger combined lithium bromide absorption refrigerator | |
| CN2378706Y (en) | Separating heat-tube heat-exchanger | |
| CN101398268B (en) | Parallel flow heat exchanger | |
| CN109579366A (en) | A kind of dry type shell and tube evaporator condenser combined system | |
| CN217504441U (en) | Steam heating device | |
| CN204705243U (en) | U-shaped pipe energy-saving heat exchangers for district heating |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C53 | Correction of patent for invention or patent application | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: PATENTEE; FROM: SHUANGLIANG BOILER CO., LTD., JIANGSU PROV. TO: JIANGSU SHUANGLIANG TECHNOLOGY CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Patentee after: Jiangsu Shuangliang Science &. Technology Co., Ltd. Patentee before: Shuangliang Boiler Co., Ltd. Jiangsu |
|
| 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 |