CN103063060A - Novel casing type heat exchanger - Google Patents
Novel casing type heat exchanger Download PDFInfo
- Publication number
- CN103063060A CN103063060A CN2013100151261A CN201310015126A CN103063060A CN 103063060 A CN103063060 A CN 103063060A CN 2013100151261 A CN2013100151261 A CN 2013100151261A CN 201310015126 A CN201310015126 A CN 201310015126A CN 103063060 A CN103063060 A CN 103063060A
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- China
- Prior art keywords
- heat exchanger
- tube
- shaped heat
- exchanger tube
- type heat
- 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.)
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/08—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
- F28D7/163—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing
- F28D7/1638—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing with particular pattern of flow or the heat exchange medium flowing inside the conduits assemblies, e.g. change of flow direction from one conduit assembly to another one
- F28D7/1646—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation with conduit assemblies having a particular shape, e.g. square or annular; with assemblies of conduits having different geometrical features; with multiple groups of conduits connected in series or parallel and arranged inside common casing with particular pattern of flow or the heat exchange medium flowing inside the conduits assemblies, e.g. change of flow direction from one conduit assembly to another one with particular pattern of flow of the heat exchange medium flowing outside the conduit assemblies, e.g. change of flow direction
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/04—Arrangements for sealing elements into header boxes or end plates
- F28F9/16—Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling
- F28F9/18—Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling by welding
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
- F28F2009/222—Particular guide plates, baffles or deflectors, e.g. having particular orientation relative to an elongated casing or conduit
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Geometry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a novel casing type heat exchanger. A distributor is arranged in the novel casing type heat exchanger and is used for communicating a tube pass medium inlet with a plurality of U-shaped heat exchange tube inlets and uniformly distributing tube pass media entering from the tube pass medium inlet to each U-shaped heat exchange tube. The U-shaped heat exchange tubes are two or more U-shaped heat exchange tubes which are serially connected through U-shaped bends. By changing the serial-connection number of the U-shaped heat exchange tubes, tube pass length of the heat exchange tubes is increased doubly, so that the tube pass media flowing out of the U-shaped heat exchange tubes can enter the other U-shaped heat exchange tubes again, and can repeatedly circulate and return in the two or more U-shaped heat exchange tubes, and the defect of insufficient tube pass is overcome. Further, the distributor and the U-shaped heat exchange tubes are welded connectively. The novel casing type heat exchanger is good in reliability, high in heat exchange efficiency, simple in structure, easy to manufacture and convenient to mount.
Description
Technical field
The present invention relates to technical field of heat exchangers, relate in particular a kind of Novel shell tubular type heat exchanger.
Background technology
The Chinese disclosure of the invention of public announcement of a patent application CN102748965 A, Shen Qing Publication day 2012.10.24 a kind of shell and tube exchanger, in this patent of invention, the import of tube side medium and outlet are arranged on two bobbin carriages, be fixed on the two ends of housing, it is when making, because tube side medium (cold-producing medium) has than high workload pressure, high for the seal request between bobbin carriage and the housing, this has just caused processing, manufacturing, installation difficulty, and easily cause the tube side dielectric leakage in the use procedure, sealing effectiveness is poor; And a heat exchanger has the faying face sealing of two places, has increased considerably manufacturing cost, and secondly, the tube side medium enters in the heat exchanger tube, and the tube side dielectric distribution in each heat exchanger tube is inhomogeneous, causes heat exchanger effectiveness poor.
Summary of the invention
The objective of the invention is provides a kind of Novel shell tubular type heat exchanger for the deficiencies in the prior art part, and its good reliability, heat exchange efficiency are high; And simple in structure, make easily, be convenient to install.
In order to solve the problems of the technologies described above, technical scheme of the present invention is as follows: Novel shell tubular type heat exchanger is provided with in the described Novel shell tubular type heat exchanger and the import of tube side medium and a plurality of U-shaped heat exchanger tube import be communicated with and will be assigned to from the tube side homogeneous media that the import of described tube side medium enters distributor in each U-shaped heat exchanger tube; Described U-shaped heat exchanger tube is the two or more U-shaped heat exchanger tube that mutually is connected in series; 2 or a plurality of U-shaped heat exchanger tube are serially connected by return bend, by changing the quantity of U-shaped heat exchanger tube serial connection, the tube side length of heat exchanger tube increases exponentially, make the tube side medium that flows out from U-shaped heat exchanger tube again enter other U-shaped heat exchanger tube, the tube side medium is done repeatedly to circulate to turn back in 2 or a plurality of U-shaped heat exchanger tube, both can remedy the shortcoming of tube side deficiency, can shorten the heat exchanger length dimension again, dwindle spatial volume; Reduced again tube side loop quantity, be more conducive to medium and distribute, so that the heat exchanger heat exchange efficiency is not fully exerted.The minimizing of tube side quantity is so that dispensing arrangement is compacter.
As preferably, it also is included in the collector that described tube side media outlet and described a plurality of U-shaped heat exchanger tube outlet are communicated with of establishing in the Novel shell tubular type heat exchanger.
As preferably, described deflection plate is spiral or segmental baffle.
As preferably, U-shaped heat exchanger tube is reducer pipe or equal pipe.
As preferably, described distributor arrival end adopts screwed pipe, and the medium gas-liquid two-phase produces turbulent flow and fully mixes in screwed pipe, improve distribution effects.
Beneficial effect of the present invention is:
Novel shell tubular type heat exchanger of the present invention, good reliability, heat exchange efficiency are high; And simple in structure, make easily, be convenient to install.
Description of drawings
The present invention is described further below in conjunction with accompanying drawing:
Fig. 1 is Novel shell tubular type heat exchanger schematic diagram of the present invention;
Fig. 2 is the structure chart of the embodiment of the invention;
Fig. 3 is dispensing arrangement schematic diagram of the present invention;
Fig. 4 is deflection plate schematic perspective view of the present invention.
Among the figure:
1, medium 1 import;
2, medium 1 outlet;
3, medium 2 imports;
4, medium 2 outlets;
5, screwed pipe;
6, distributor 601-distributor body, 601a-through flow hole, 601b-throttling stopple, 601c-hybrid chamber, 601d-bullet, 601e-dispensing orifice;
7, collector;
8, U-shaped elbow;
9, U-shaped heat exchanger tube;
10, housing;
11, deflection plate;
12, cover plate;
13, discharge outlet;
14, exhaust outlet;
15, mounting bracket;
16, medium 2 import temperature-sensing pipes are placed mouth;
17, medium 2 outlet temperature-sensing pipes are placed mouth.
The specific embodiment
The following stated is preferred embodiment of the present invention only, is not that scope of the present invention is limited.
Embodiment sees accompanying drawing 1,2,3,4, Novel shell tubular type heat exchanger, comprise having medium 1 import 1, medium 2 import/exports 3,4 housing 10, U-shaped heat exchanger tube 9, deflection plate 11 are installed in medium 1 outlet 2, U-shaped heat exchanger tube 9 is equal pipe or reducer pipe, and two or more U-shaped heat exchanger tubes 9 are connected in series mutually.Simultaneously, on housing 10, also be provided with discharge outlet 13 and exhaust outlet 14 and mounting bracket 15, medium 2 imports 3 positions are positioned at the front end of described medium 2 outlets 4, and the cover plate 12 of close described heat exchanger, be provided with medium 2 import temperature-sensing pipes in medium 2 imports 3 and place mouth 16, be provided with medium 2 outlet temperature-sensing pipes in medium 2 outlets and place mouth 17, connection is connected with bolt in described housing 10 ends with cover plate, and keep sealing by sealing gasket, described cover plate 12 is provided with tube side medium 1 import/export 1 and 2, in described Novel shell tubular type heat exchanger, be provided with the import 1 of described tube side medium and described a plurality of U-shaped heat exchanger tube 901 imports are communicated with, and will be assigned to from the tube side homogeneous media that described tube side medium import 1 enters the distributor 6 in each U-shaped heat exchanger tube 902, in described Novel shell tubular type heat exchanger, be provided with the collector 7 with described tube side medium 1 outlet 2 and the 906 outlet connections of described a plurality of U-shaped heat exchanger tube.Distributor 6 guarantees that the tube side medium 1 that enters from tube side medium import 1 can be assigned in the heat exchanger tube 9 uniformly, and collector 7 collects the tube side medium 1 in the U-shaped heat exchanger tube 9, transfers out by tube side media outlet 2.In the present embodiment, described distributor 6 comprises the distributor body 601 with through flow hole 601a, be provided with in the described distributor body 601 to the tube side medium that enters from medium 1 import carry out throttling speed-raising tube side medium restriction, the tube side medium after the throttling speed-raising is broken up the mixing section of breaing up of mixing and will be broken up the tube side medium dispenser that mixed tube side medium dispenses; Further, described tube side medium restriction comprises the throttling stopple 601b that is arranged in the described through flow hole, and throttling stopple 601b welds or is riveted in the through flow hole 601a, also can be one-body molded, and it has a through hole that is used for throttling; The described mixing section of breaing up comprises by described throttling stopple 601b and described through flow hole bottom surface and forms hybrid chamber 601c and be arranged on described through flow hole bottom surface along with the bullet 601d that diminishes gradually near described throttling stopple diameter; The tube side medium that advanced after throttle orifice plug 601b throttling is raised speed enters in the hybrid chamber 601c, 601d breaks up by bullet, mix, bullet 601d is cone, described tube side medium dispenser comprises the dispensing orifice 601e that a plurality of and described hybrid chamber 601c communicates, and the air line distance between described dispensing orifice 601e axis and the described throttling stopple 601b axis is along with the linear or non-linear increase away from described throttling stopple 601b; Throttling stopple 601b is used for the cross-sectional area of through hole of throttling less than all dispensing orifice 601e cross-sectional area sums.
Described distributor 6 is positioned at described collector 7 belows, and described distributor 6 arrival ends and described collector 7 ports of export are fixedly connected with described cover plate 12.
Described distributor 6 and described U-shaped heat exchanger tube 901 are welded and fixed, and do not have bobbin carriage and expanded joint.In the present embodiment, described deflection plate 8 is made for injection moulding or other moulding, adopts the technique of injection mo(u)lding to carry out one-shot forming processing, and machining accuracy is high, good sealing effect.
Described Novel shell tubular type heat exchanger, comprise housing 10, a plurality of U-shaped heat exchanger tube 9, deflection plate 11 with medium 2 imports 3 and medium 2 outlets 4, described housing 10 ends are fixed with the end plate 12 that housing 10 is closed, described cover plate 12 is provided with medium 1 import 1 and medium 1 outlet 2, and medium 1 import 1 is communicated with by distributor 6 and a plurality of U-shaped heat exchanger tube 9 imports in described shell and tube exchanger.
Medium 1 outlet 2 is communicated with by collector 7 and 9 outlets of a plurality of U-shaped heat exchanger tube in described shell and tube exchanger.
Novel shell tubular type heat exchanger of the present invention, with medium 1 import 1, medium 1 outlet all is arranged on the cover plate, pass through distributor, collector respectively with U-shaped heat exchanger tube import, outlet is communicated with, adopt an end to cooperate a sealing gasket to seal, reduced sealing, processing and assembly difficulty, adopt distributor that the tube side medium is carried out uniform distribution, especially when the tube side medium of vapour-liquid two-phase complexity, more can embody its incomparable superiority, because a lot of tube side media are when for example freon enters from the import of tube side medium, it is the liquid state that contains gas, when adopting bobbin carriage to distribute in the past, the tube side medium that enters in each heat exchanger tube is inhomogeneous, but also tube side medium air content is many in the U-shaped heat exchanger tube that can cause, and tube side medium air content is few in the U-shaped heat exchanger tube that has, and flow velocity is unreasonable, and the present invention distributes the tube side medium by distributor, so that enter the interior tube side homogeneous media of U-shaped heat exchanger tube, flow velocity is reasonable, significantly improves heat exchange efficiency.
Described distributor 6 comprises the distributor body 601 with through flow hole 601a, be provided with in the described distributor body 601 to the tube side medium that enters from tube side medium import 1 carry out throttling speed-raising tube side medium restriction, the tube side medium after the throttling speed-raising is broken up the mixing section of breaing up of mixing and will be broken up the tube side medium dispenser that mixed tube side medium dispenses.
Described tube side medium restriction comprises the throttling stopple 601b that is arranged in the described through flow hole; The described mixing section of breaing up comprises by described throttling stopple 601b and described through flow hole bottom surface and forms hybrid chamber 601c and be arranged on described through flow hole bottom surface along with the bullet 601d that diminishes gradually near described throttling stopple diameter; Described tube side medium dispenser comprises the dispensing orifice 601e that a plurality of and described hybrid chamber 601c communicates, and the air line distance between described dispensing orifice 601e axis and the described throttling stopple 601b axis is along with the linear or non-linear increase away from described throttling stopple 601b.
Described U-shaped heat exchanger tube 9 circuitous " U " shape heat exchanger tube that comprises line part and U-shaped section that forms repeatedly in described housing 10.
Described collector 7 and the connection of 906 " U " type heat exchanger tube, 906 " U " type heat exchanger tube and 904 " U " type heat exchanger tube are communicated with by 905 " U " type elbow, 904 " U " type heat exchanger tube and 902 " U " type heat exchanger tube are communicated with by 903 " U " type elbow, and 902 " U " type heat exchanger tube and distributor 6 are communicated with by 901 straight tubes; Described 902,904 and 906 " U " type heat exchanger tube is connected in series by 903 and 905 " U " type elbow, forms the loop of 3 bafflings.By increasing or reduce the quantity of " U " type heat exchanger tube and " U " type elbow, change baffling number of times and tube side; Or/can by changing caliber and the length of " U " type heat exchanger tube, adjust the exchange capability of heat size.
The caliber of described 901 straight tubes and 902 " U " type heat exchanger tube is minimum, be positioned at distributor 6 after, " U " type heat exchanger tube of other serial connections is isometrical or reducing with 902 " U " type heat exchanger tube, is communicated with " U " type elbow that is fit to.
Because there is phase transformation in the tube side medium of vapour-liquid two-phase complexity in heat transfer process, single tube side latus rectum can't satisfy giving full play to of its best heat exchange property, and above-mentioned the setting can effectively address this problem.(cold-producing medium is that liquid is main vapour-liquid two-phase mixture to the tube side medium, in heat transfer process, because the continuous heat absorption evaporation of liquid, volume expands rapidly, and tube side medium 1 is inadequate at the heat exchanger tube first half place of single latus rectum flow velocity, but too fast at the latter half of place of heat exchanger tube flow velocity, resistance increment, affected heat exchanger effectiveness, above-mentioned measure has well solved this difficult problem, has improved heat exchange efficiency.
Described deflection plate 11 is helical baffles or segmental baffle, and described deflection plate edge is provided with thickness less than the shirt rim of described deflection plate.The shirt rim can overcome housing 10 with deflection plate because medium 2 incidental by-pass flows, leakage current have been avoided in the gap that dimensional tolerance cooperates; Guarantee that simultaneously deflection plate is unlikely to unsettled in housing 10, avoid the vibration of " U " type heat exchanger tube, improve heat exchanger product reliability and service life, improve heat exchange efficiency.
Above explanation only is explanation of the invention, so that complete enforcement this programme of those of ordinary skills' energy, but be not limitation of the present invention, those skilled in the art can make the modification that does not have creative contribution to the present embodiment as required after reading this specification, these all are not creative modifications.But as long as in claim scope of the present invention, all be subject to the protection of Patent Law.
Claims (6)
1. Novel shell tubular type heat exchanger is characterized in that: be provided with in the described Novel shell tubular type heat exchanger and tube side medium import (1) and a plurality of U-shaped heat exchanger tube (9) import be communicated with and will be assigned to from the tube side homogeneous media that described tube side medium import (1) enters distributor (6) in each U-shaped heat exchanger tube (9); Described U-shaped heat exchanger tube (9) is the two or more U-shaped heat exchanger tube that mutually is connected in series; 2 or a plurality of U-shaped heat exchanger tube are serially connected by return bend (8), by changing the quantity of U-shaped heat exchanger tube (9) serial connection, the tube side length of heat exchanger tube increases exponentially, the tube side medium is done repeatedly to circulate to turn back in 2 or a plurality of U-shaped heat exchanger tube, remedy the shortcoming of tube side deficiency, welding is adopted in the connection between described distributor (6) and the described U-shaped heat exchanger tube (9).
2. Novel shell tubular type heat exchanger according to claim 1 is characterized in that: it also is included in the collector (7) that described tube side media outlet (2) and described a plurality of U-shaped heat exchanger tubes (9) outlet are communicated with of establishing in the Novel shell tubular type heat exchanger.
3. Novel shell tubular type heat exchanger according to claim 2, it is characterized in that: described deflection plate (11) is spiral or segmental baffle.
4. according to claim 1 and 2 or 3 described Novel shell tubular type heat exchangers, it is characterized in that: U-shaped heat exchanger tube is reducer pipe or equal pipe.
5. according to claim 1 and 2 or 3 described Novel shell tubular type heat exchangers, it is characterized in that: described distributor (6) arrival end adopts screwed pipe (5), medium produces turbulent flow and fully mixes and enter distributor (6) in screwed pipe (5), improve distribution effects.
6. described Novel shell tubular type heat exchanger is characterized in that according to claim 1-5, and the material of described return bend (8) and U-shaped heat exchanger tube (9) is red copper, Alpaka, stainless steel, titanium, aluminum or aluminum alloy.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310015126.1A CN103063060B (en) | 2013-01-16 | 2013-01-16 | Novel casing type heat exchanger |
| PCT/CN2014/070658 WO2014111015A1 (en) | 2013-01-16 | 2014-01-15 | Novel shell and tube heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310015126.1A CN103063060B (en) | 2013-01-16 | 2013-01-16 | Novel casing type heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103063060A true CN103063060A (en) | 2013-04-24 |
| CN103063060B CN103063060B (en) | 2014-09-17 |
Family
ID=48105793
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310015126.1A Active CN103063060B (en) | 2013-01-16 | 2013-01-16 | Novel casing type heat exchanger |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN103063060B (en) |
| WO (1) | WO2014111015A1 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103644760A (en) * | 2013-12-04 | 2014-03-19 | 新昌县晶鑫精密机械配件厂 | Distributor suitable for shell and tube heat exchangers |
| WO2014111015A1 (en) * | 2013-01-16 | 2014-07-24 | 英特换热设备(浙江)有限公司 | Novel shell and tube heat exchanger |
| CN104329979A (en) * | 2014-07-16 | 2015-02-04 | 江苏南通申通机械有限公司 | Heat pipe heat exchanger partition plate and heat pipe heat exchanger evaporation end structure thereof |
| CN109708494A (en) * | 2019-01-06 | 2019-05-03 | 佛山市顺德区金舵空调冷冻设备有限公司 | A kind of shell and tube exchanger |
| CN110285694A (en) * | 2019-06-19 | 2019-09-27 | 武汉方特工业设备技术有限公司 | Coiled channel heat exchanger |
| CN112857127A (en) * | 2021-01-18 | 2021-05-28 | 中国神华煤制油化工有限公司 | Self-cleaning end cover and heat exchange equipment |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11920878B2 (en) * | 2017-08-28 | 2024-03-05 | Watlow Electric Manufacturing Company | Continuous helical baffle heat exchanger |
| US11913736B2 (en) * | 2017-08-28 | 2024-02-27 | Watlow Electric Manufacturing Company | Continuous helical baffle heat exchanger |
| CN109974294A (en) * | 2018-02-08 | 2019-07-05 | 淄博河轩化工设备有限公司 | A kind of oil shell and tube hot air heating apparatus |
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| CN2509532Y (en) * | 2001-09-21 | 2002-09-04 | 张凤岭 | Internal slugging shell-and-tube cooler |
| CN1719177A (en) * | 2005-07-01 | 2006-01-11 | 彭建华 | Return pipe heat exchanger |
| CN102374799A (en) * | 2010-08-20 | 2012-03-14 | 上海瀚艺冷冻机械有限公司 | Shell and tube heat exchanger |
| CN203163551U (en) * | 2013-01-16 | 2013-08-28 | 英特换热设备(浙江)有限公司 | Novel shell and tube heat exchanger |
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| CN200982777Y (en) * | 2006-12-11 | 2007-11-28 | 青岛海信空调有限公司 | Diverter of air conditioner |
| SE535397C2 (en) * | 2009-08-12 | 2012-07-24 | Alfa Laval Corp Ab | A deodorizer, heat exchanger system comprising deodorizers and method of using its |
| CN202382625U (en) * | 2011-11-24 | 2012-08-15 | 江苏沿江化工资源开发研究院有限公司 | Variable-diameter tube array heat exchanger |
| CN103063060B (en) * | 2013-01-16 | 2014-09-17 | 英特换热设备(浙江)有限公司 | Novel casing type heat exchanger |
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2013
- 2013-01-16 CN CN201310015126.1A patent/CN103063060B/en active Active
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2014
- 2014-01-15 WO PCT/CN2014/070658 patent/WO2014111015A1/en active Application Filing
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2509532Y (en) * | 2001-09-21 | 2002-09-04 | 张凤岭 | Internal slugging shell-and-tube cooler |
| CN1719177A (en) * | 2005-07-01 | 2006-01-11 | 彭建华 | Return pipe heat exchanger |
| CN102374799A (en) * | 2010-08-20 | 2012-03-14 | 上海瀚艺冷冻机械有限公司 | Shell and tube heat exchanger |
| CN203163551U (en) * | 2013-01-16 | 2013-08-28 | 英特换热设备(浙江)有限公司 | Novel shell and tube heat exchanger |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2014111015A1 (en) * | 2013-01-16 | 2014-07-24 | 英特换热设备(浙江)有限公司 | Novel shell and tube heat exchanger |
| CN103644760A (en) * | 2013-12-04 | 2014-03-19 | 新昌县晶鑫精密机械配件厂 | Distributor suitable for shell and tube heat exchangers |
| CN103644760B (en) * | 2013-12-04 | 2015-09-23 | 新昌县晶鑫精密机械配件厂 | A kind of distributor being applicable to shell and tube exchanger |
| CN104329979A (en) * | 2014-07-16 | 2015-02-04 | 江苏南通申通机械有限公司 | Heat pipe heat exchanger partition plate and heat pipe heat exchanger evaporation end structure thereof |
| CN109708494A (en) * | 2019-01-06 | 2019-05-03 | 佛山市顺德区金舵空调冷冻设备有限公司 | A kind of shell and tube exchanger |
| CN110285694A (en) * | 2019-06-19 | 2019-09-27 | 武汉方特工业设备技术有限公司 | Coiled channel heat exchanger |
| CN110285694B (en) * | 2019-06-19 | 2024-03-12 | 武汉方特工业设备技术有限公司 | Coiled pipe type channel heat exchanger |
| CN112857127A (en) * | 2021-01-18 | 2021-05-28 | 中国神华煤制油化工有限公司 | Self-cleaning end cover and heat exchange equipment |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103063060B (en) | 2014-09-17 |
| WO2014111015A1 (en) | 2014-07-24 |
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Address after: 313300, Zhejiang Anji Economic Development Zone, Huzhou Pu Industrial Park, the three inter platform heat exchange equipment (Zhejiang) Co., Ltd. Patentee after: Zhejiang Intech Technology Co., Ltd Address before: 313300, Zhejiang Anji Economic Development Zone, Huzhou Pu Industrial Park, the three inter platform heat exchange equipment (Zhejiang) Co., Ltd. Patentee before: EXTEK ENERGY EQUIPMENT (ZHEJIANG) Ltd. |
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