CN103063060B - Novel casing type heat exchanger - Google Patents

Novel casing type heat exchanger Download PDF

Info

Publication number
CN103063060B
CN103063060B CN201310015126.1A CN201310015126A CN103063060B CN 103063060 B CN103063060 B CN 103063060B CN 201310015126 A CN201310015126 A CN 201310015126A CN 103063060 B CN103063060 B CN 103063060B
Authority
CN
China
Prior art keywords
heat exchanger
tube
shaped heat
tube side
heat exchange
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.)
Active
Application number
CN201310015126.1A
Other languages
Chinese (zh)
Other versions
CN103063060A (en
Inventor
方真健
覃正乐
蒋志武
黄林锋
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.)
Zhejiang Intech Technology Co., Ltd
Original Assignee
Extek Energy Equipment Zhejiang Ltd
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 Extek Energy Equipment Zhejiang Ltd filed Critical Extek Energy Equipment Zhejiang Ltd
Priority to CN201310015126.1A priority Critical patent/CN103063060B/en
Publication of CN103063060A publication Critical patent/CN103063060A/en
Priority to PCT/CN2014/070658 priority patent/WO2014111015A1/en
Application granted granted Critical
Publication of CN103063060B publication Critical patent/CN103063060B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/08Heat-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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/16Heat-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
    • F28D7/163Heat-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
    • F28D7/1638Heat-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
    • F28D7/1646Heat-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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/04Arrangements for sealing elements into header boxes or end plates
    • F28F9/16Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling
    • F28F9/18Arrangements for sealing elements into header boxes or end plates by permanent joints, e.g. by rolling by welding
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
    • F28F2009/222Particular 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

Novel shell tubular type heat exchanger
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 manufacturing, because tube side medium (cold-producing medium) has compared with high workload pressure, high for the seal request between bobbin carriage and housing, this has just caused processing, manufacture, installation difficulty, and in use procedure, easily cause tube side dielectric leakage, sealing effectiveness is poor; And a heat exchanger has the faying face sealing of two places, has increased considerably manufacturing cost, secondly, tube side medium enters in 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 object of the invention is, for the deficiencies in the prior art part, provides a kind of Novel shell tubular type heat exchanger, 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 described Novel shell tubular type heat exchanger the import of tube side medium and a plurality of U-shaped heat exchanger tube import are communicated with and the tube side homogeneous media entering from the import of described tube side medium is assigned to the distributor in each U-shaped heat exchanger tube; Described U-shaped heat exchanger tube is the two or more U-shaped heat exchanger tube being mutually 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 flowing out from U-shaped heat exchanger tube again enter other U-shaped heat exchanger tube, tube side medium is done circulation in multiple times and is turned back in 2 or a plurality of U-shaped heat exchanger tube, both can make up the shortcoming of tube side deficiency, can shorten heat exchanger length dimension again, dwindle spatial volume; Reduced again tube side loop quantity, be more conducive to medium and distribute, heat exchanger heat exchange efficiency is not fully exerted.The minimizing of tube side quantity, makes dispensing arrangement compacter.
As preferably, it is also 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 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 medium gas-liquid two-phase produces turbulent flow and fully mixes in screwed pipe, improves 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.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the present invention is described further:
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 present invention;
Fig. 3 is dispensing arrangement schematic diagram of the present invention;
Fig. 4 is deflection plate schematic perspective view of the present invention.
in 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 only preferred embodiment of the present invention, not scope of the present invention is limited.
Embodiment, is shown in accompanying drawing 1,2,3,4, Novel shell tubular type heat exchanger, comprise and have medium 1 import 1, medium 1 outlet 2, installs housing 10, U-shaped heat exchanger tube 9, the deflection plate 11 of medium 2 import/exports 3,4, 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, be also provided with discharge outlet 13 and exhaust outlet 14 and mounting bracket 15, medium 2 import 3 positions are positioned at the front end of described medium 2 outlets 4, and the cover plate 12 of close described heat exchanger, in medium 2 imports 3, be provided with medium 2 import temperature-sensing pipes and place mouth 16, in medium 2 outlets, be provided with medium 2 outlet temperature-sensing pipes and place mouth 17, described housing 10 ends are connected with cover plate 12 with bolt, 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 901 imports of described a plurality of U-shaped heat exchanger tube are communicated with, and the tube side homogeneous media entering from described tube side medium import 1 is assigned to 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 of 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 entering from tube side medium import 1 can be assigned in heat exchanger tube 9 uniformly, and collector 7 collects the tube side medium 1 in U-shaped heat exchanger tube 9, by tube side media outlet 2, transfers out.In the present embodiment, described distributor 6 comprises the distributor body 601 with through flow hole 601a, is provided with tube side medium restriction that tube side medium to entering from medium 1 import carries out throttling speed-raising, the tube side medium throttling speed-raising is broken up to the mixing portion of breaing up of mixing and by the tube side medium dispenser of breaing up mixed tube side medium and dispensing in described distributor body 601; Further, described tube side medium restriction comprises the throttling stopple 601b being arranged in described through flow hole, and throttling stopple 601b welds or is riveted in through flow hole 601a, also can be one-body molded, and it has one for the through hole of throttling; The described mixing portion 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 diminishing gradually near described throttling stopple diameter; The tube side medium entering after throttle orifice plug 601b throttling speed-raising enters in hybrid chamber 601c, by bullet, 601d breaks up, 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 described throttling stopple 601b axis is along with the linear or non-linear increase away from described throttling stopple 601b; Throttling stopple 601b is less than all dispensing orifice 601e cross-sectional area sums for the cross-sectional area of the through hole of throttling.
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 there is no 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, the 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 in described shell and tube exchanger, 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.
Novel shell tubular type heat exchanger of the present invention, by medium 1 import 1, medium 1 outlet is all arranged on a cover plate, pass through distributor, collector respectively with U-shaped heat exchanger tube import, outlet is communicated with, adopt an end to coordinate a sealing gasket to seal, reduced sealing, processing and assembly difficulty, adopt distributor to carry out uniform distribution to tube side medium, 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 entering in each heat exchanger tube is inhomogeneous, but also in the U-shaped heat exchanger tube that can cause, tube side medium air content is many, in the U-shaped heat exchanger tube having, tube side medium air content is few, flow velocity is unreasonable, and the present invention distributes tube side medium by distributor, make to enter the tube side homogeneous media in U-shaped heat exchanger tube, flow velocity is reasonable, significantly improve heat exchange efficiency.
Described distributor 6 comprises the distributor body 601 with through flow hole 601a, is provided with tube side medium restriction that tube side medium to entering from tube side medium import 1 carries out throttling speed-raising, the tube side medium throttling speed-raising is broken up to the mixing portion of breaing up of mixing and by the tube side medium dispenser of breaing up mixed tube side medium and dispensing in described distributor body 601.
Described tube side medium restriction comprises the throttling stopple 601b being arranged in described through flow hole; The described mixing portion 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 diminishing 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 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 in described housing 10 repeatedly roundabout formation comprise " U " shape heat exchanger tube of line part and U-shaped portion.
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 exchange capability of heat size.
The caliber of described 901 straight tubes and 902 " U " type heat exchanger tube is minimum, is positioned at after distributor 6, and " U " type heat exchanger tube of other serial connections is isometrical or reducing with 902 " U " type heat exchanger tube, with " U " type elbow being applicable to, is communicated with.
Because the tube side medium of vapour-liquid two-phase complexity exists phase transformation in heat transfer process, single tube side latus rectum cannot meet giving full play to of its best heat exchange property, and above-mentioned setting can effectively address this problem.(cold-producing medium is that liquid is main vapour-liquid two-phase mixture to tube side medium, in heat transfer process, continuous heat absorption evaporation due to 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 the shirt rim that thickness is less than described deflection plate.Shirt rim can overcome housing 10 with deflection plate due to the gap that dimensional tolerance coordinates, avoided the incidental by-pass flow of medium 2, leakage current; Guarantee that deflection plate is unlikely to unsettled in housing 10 simultaneously, avoid the vibration of " U " type heat exchanger tube, improve heat exchanger product reliability and service life, improve heat exchange efficiency.
More than explanation is only explanation of the invention, make those of ordinary skills' can completely implement this programme, but be not limitation of the present invention, those skilled in the art can make to the present embodiment the modification that there is no creative contribution as required after reading this description, and these are all not creative modifications.But as long as within the scope of claim of the present invention, be all subject to the protection of Patent Law.

Claims (5)

1. Novel shell tubular type heat exchanger, is characterized in that: in described Novel shell tubular type heat exchanger, be provided with tube side medium import (1) and a plurality of U-shaped heat exchanger tube (9) import are communicated with and the tube side homogeneous media entering from described tube side medium import (1) is assigned to the 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 being mutually 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, tube side medium is done circulation in multiple times and is turned back in 2 or a plurality of U-shaped heat exchanger tube, make up the shortcoming of tube side deficiency, the connection between described distributor (6) and described U-shaped heat exchanger tube (9) adopts welding; Described distributor (6) comprises the have through flow hole distributor body (601) of (601a), is provided with tube side medium restriction that tube side medium to entering from tube side medium import (1) carries out throttling speed-raising, the tube side medium throttling speed-raising is broken up to the mixing portion of breaing up of mixing and by the tube side medium dispenser of breaing up mixed tube side medium and dispensing in described distributor body (601).
2. Novel shell tubular type heat exchanger according to claim 1, is characterized in that: it is also 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 Novel shell tubular type heat exchanger.
3. Novel shell tubular type heat exchanger according to claim 1 and 2, is characterized in that: U-shaped heat exchanger tube is reducer pipe or equal pipe.
4. Novel shell tubular type heat exchanger according to claim 1 and 2, is characterized in that: described distributor (6) arrival end adopts screwed pipe (5), and medium produces turbulent flow and fully mixes and enter distributor (6) in screwed pipe (5), improves distribution effects.
5. according to the Novel shell tubular type heat exchanger described in claim 1 or 2 or 3, it is characterized in that, 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.
CN201310015126.1A 2013-01-16 2013-01-16 Novel casing type heat exchanger Active CN103063060B (en)

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 CN103063060A (en) 2013-04-24
CN103063060B true 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)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
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
CN104329979B (en) * 2014-07-16 2016-08-17 江苏南通申通机械有限公司 A kind of clapboard of heat pipe exchanger and heat exchange of heat pipe evaporation ends structure thereof
US11913736B2 (en) * 2017-08-28 2024-02-27 Watlow Electric Manufacturing Company Continuous helical baffle heat exchanger
US11920878B2 (en) * 2017-08-28 2024-03-05 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
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
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
CN112857127B (en) * 2021-01-18 2022-05-31 中国神华煤制油化工有限公司 Self-cleaning end cover and heat exchange equipment

Family Cites Families (8)

* Cited by examiner, † Cited by third party
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
CN100362305C (en) * 2005-07-01 2008-01-16 彭建华 Return pipe heat exchanger
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
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
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
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
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

Also Published As

Publication number Publication date
WO2014111015A1 (en) 2014-07-24
CN103063060A (en) 2013-04-24

Similar Documents

Publication Publication Date Title
CN103063060B (en) Novel casing type heat exchanger
CN105937857A (en) Shell-and-tube heat exchanger suitable for three-fluid heat exchange
CN203163551U (en) Novel shell and tube heat exchanger
CN111561785A (en) Novel stainless steel heat exchanger
CN102767983A (en) Guiding device and heat exchanger capable of achieving even distribution of fluid
WO2014059893A1 (en) Heat exchanger
CN109780925A (en) A kind of plate-fin heat exchanger baffle nozzle structure end socket
CN203385245U (en) Shell-and-tube condenser
CN202158700U (en) Flow equalizing device, evaporator and air-conditioner
CN108225063A (en) A kind of three media heat exchangers and its manufacturing method, a kind of three media for heat exchange equipment
CN103438753A (en) Novel baffle plate
CN207922920U (en) Three media heat exchangers of one kind and three media for heat exchange equipment
CN200993547Y (en) Baffle plate with special hole
CN205090407U (en) Coiled heat exchange device
CN101419004A (en) Heat exchange method of pipe shell type heat-exchanger and heat exchanger thereof
CN209763847U (en) Dry-type shell-and-tube heat exchanger for improving liquid supply distribution of refrigerant
CN105371492A (en) Heat exchanger and gas water heater with heat exchanger
CN204165423U (en) Micro-channel heat exchanger
CN207779180U (en) A kind of Heat Exchangers
CN204153978U (en) Heat exchanger and the gas heater with it
CN204043474U (en) Shell-and-tube phase change heat exchanger and liquid spray thrower thereof
CN209147781U (en) A kind of shell-and-tube exchanger
CN205156699U (en) Double -helical -baffle heat exchanger
CN201724596U (en) Baffle plate and shell and tube heat exchanger with the same
CN215810424U (en) Distribution pipe and heat exchanger with same

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CP01 Change in the name or title of a patent holder

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.

CP01 Change in the name or title of a patent holder