CN110260694A - Plate journey shunt plate heat exchanger - Google Patents
Plate journey shunt plate heat exchanger Download PDFInfo
- Publication number
- CN110260694A CN110260694A CN201910665956.6A CN201910665956A CN110260694A CN 110260694 A CN110260694 A CN 110260694A CN 201910665956 A CN201910665956 A CN 201910665956A CN 110260694 A CN110260694 A CN 110260694A
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- CN
- China
- Prior art keywords
- plate
- heat exchange
- heat
- auxiliary
- exchange module
- 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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- 239000007791 liquid phase Substances 0.000 abstract description 13
- 239000012530 fluid Substances 0.000 abstract description 4
- 239000007788 liquid Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
Classifications
-
- 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
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The present invention is a kind of plate journey shunt plate heat exchanger, including shell and it is mounted in shell and more than two heat exchange module arranged up and down, auxiliary heat-exchanging No. of plates is n1 in top layer's heat exchange module, auxiliary heat-exchanging No. of plates is n2 in its next layer of heat exchange module, auxiliary heat-exchanging No. of plates is n3 in next layer of heat exchange module again, the rest may be inferred, and n1, n2, n3 represent natural number, and the quantity of auxiliary heat-exchanging plate is not zero at least one layer of heat exchange module；In the heat exchange module of setting auxiliary heat-exchanging plate, the tie point between mainboard piece inlet pipe and inlet side collector is higher than the tie point between auxiliary plate inlet pipe and inlet side collector.It is introduced into individually auxiliary plate after in the middle part of the plate journey fluid points of liquid phase including oil is concentrated confluence by inlet side collector, accelerates liquid phase discharge, the content of the liquid phase and oil by main body heat exchanger fin is greatly lowered, to improve device overall heat exchange efficiency.
Description
Technical field
The present invention relates to a kind of plate type heat exchanger, it is mainly used in the heat exchange that plate journey is steam (especially containing oil vapour)
Device, such as condensing unit, vaporising device and fluid heater.
Background technique
It is existing by vapor condensation at the heat exchanger of liquid phase, such as condenser, mainly include that shell-and-plate (inhale by water in shell side
Heat), air-cooled (normal temperature air makees cold energy) and evaporate cold type (being absorbed heat by water evaporation).In above-mentioned heat transfer process, plate journey (belongs to
In tube side) in liquid phase (condensate liquid) gradually increase.In addition, oil-containing in some media, is easy to form oil in heat exchanger inner surface
Film.The formation and accumulation of condensate liquid and oil film will seriously affect media flow speed in heat exchanger, and heat exchange efficiency is caused to reduce.?
In compressor assembly, the formation and accumulation of condensate liquid and oil film also result in compressor and increase energy consumption because pressure at expulsion increases.
Especially in the higher place of environment temperature, Compressor Discharge Pressure is excessively high also to generate security risk.
The Chinese patent application of Publication No. CN104132557A is related to a kind of " intermediate drain formula high-efficiency condensation system.Its
Intermediate drain is implemented in prime heat exchanger end, this measure accelerates the discharge of liquid film, so that the coefficient of heat transfer be made to rise.And
And the utilization rate of heat exchanger heat-transfer surface is effectively increased, it ensure that prime heat exchanger is in high efficient heat exchanging state always.By making
With discovery, although the intermediate drain measure can have certain effect in terms of improving heat exchange efficiency, due to its way be by
Condensate liquid draws heat exchanger, and this part draws medium and is generally gas-liquid mixed phase, and still storing has very high thermal energy, on the one hand can make
It is reduced at heat utilization rate, on the other hand, increases the operating load of refrigeration system.
Summary of the invention
The technical problem to be solved by the invention is to provide a kind of plate journey shunt plate heat exchangers, will be in plate journey fluid
Liquid phase of the part including oil is introduced into individually auxiliary plate after concentrating confluence by inlet side collector, accelerates liquid phase discharge,
The content of the liquid phase and oil by main body heat exchanger fin is greatly lowered, to improve device overall heat exchange efficiency.
Technical scheme is as follows:
Plate journey shunt plate heat exchanger, including shell and be mounted in shell and more than two heat exchange mould arranged up and down
Block, heat exchange module include several main heat exchange plates and a certain number of auxiliary heat-exchanging plates installed side by side, heat exchange plate
Medium inlet side is equipped with inlet side collector, and medium outlet is equipped with outlet collector, and inlet side collector is changed by mainboard piece inlet pipe connection master
Hot plate piece, and auxiliary heat-exchanging plate is connected by auxiliary plate inlet pipe；The outlet collector of a upper heat exchange module is connected by connecting tube
Connecing the inlet side collector of next heat exchange module, it is characterised in that: auxiliary heat-exchanging No. of plates is n1 in top layer's heat exchange module, it
Auxiliary heat-exchanging No. of plates is that auxiliary heat-exchanging No. of plates is n3 in n2, then next layer of heat exchange module in next layer of heat exchange module,
The rest may be inferred, and n1, n2, n3 represent natural number, and the quantity of auxiliary heat-exchanging plate is not zero at least one layer of heat exchange module；?
It is arranged in the heat exchange module of auxiliary heat-exchanging plate, the tie point between mainboard piece inlet pipe and inlet side collector is higher than auxiliary plate inlet pipe
With the tie point between the collector of inlet side.
Preferably, the quantity of auxiliary heat-exchanging plate gradually increases in top-down each heat exchange module.
Preferably, the tie point between mainboard piece inlet pipe and inlet side collector is located at the centre of inlet side collector short transverse, auxiliary
The tie point helped between plate inlet pipe and inlet side collector is located at the bottom side of inlet side collector.
Preferably, auxiliary heat-exchanging plate is mounted on the same side of heat exchanger in each heat exchange module.
The positive effect of the present invention is:
One, present invention utilizes the confluence of inlet side collector and gas-liquid separating function, most of gas phase (steam) flows through main body heat exchange
Plate, most of liquid phase (including oil) enter auxiliary heat-exchanging plate.Since confluence acts on liquid phase flow faster, to improve liquid
Phase thermal coefficient, and the velocity of discharge of liquid phase is improved, heat exchange efficiency is improved on the whole.And due to liquid in main body heat exchange plate
Mutually and oil component (oil film) significantly reduce, heat exchange effect be improved significantly.In the case where realizing equivalent heat exchange amount, benefit
Heat exchanger specification can be greatly lowered with the present invention, so that the manufacture of heat-exchanger rig, O&M cost be greatly reduced, and reduce
Heat-exchanger rig occupied area.
Two, it in optimisation technique scheme, is provided in next module compared with the more auxiliary heat-exchanging plates of a upper module.It is this to set
Meter ensures that plate journey fluid flows from above to below in heat transfer process, and the liquid phase output gradually increased can shunt in time, it is ensured that heat exchange
Device balance movement always, obtains more optimized heat transfer effect.
Three, auxiliary heat-exchanging No. of plates of the present invention is less and is mounted on the same side of heat exchanger, is more convenient for dismantling oil removing,
And a large amount of main heat exchange plate trapped fuel amount is effectively controlled, and extends complete machine maintenance period.
Detailed description of the invention
Fig. 1 is the structure and operation principle schematic diagram of the embodiment of the present invention.In Fig. 1, due in each module of hiding relation
Only show a main heat exchange plate and an auxiliary heat-exchanging plate.
Fig. 2 is another viewing angle constructions schematic diagram of the embodiment of the present invention.Belong to left view schematic diagram relative to Fig. 1, Fig. 2.
Shell is omitted in two figures.
Specific embodiment
The present invention is further illustrated with reference to the accompanying drawings and examples.
Such as Fig. 1 and Fig. 2, the present embodiment includes shell and is mounted on the intracorporal three layers of heat exchange module of shell.Each heat exchange module
It include several main heat exchange plates 4 and at least one auxiliary heat-exchanging plate 5 installed side by side, the medium inlet side of heat exchange plate is pacified
Equipped with inlet side collector, medium outlet is equipped with outlet collector.Inlet side collector connects main heat exchange plate by mainboard piece inlet pipe 3, and
Auxiliary heat-exchanging plate is connected by auxiliary plate inlet pipe 15.Main heat exchange plate is logical by mainboard piece outlet pipe 6 and auxiliary heat-exchanging plate
It crosses auxiliary plate outlet pipe 16 and is separately connected outlet collector.
Various heat exchange module may be mounted in same housing, also may be mounted in different housings.
The installation arranged side by side refers to that bottom end is concordant and is disposed in parallel relation to one another.In general, whole main heat exchange plates are with identical
Height, whole auxiliary heat-exchanging plates height having the same and be equal to or less than main heat exchange plate, it is preferable that auxiliary is changed
Hot plate piece is lower than main heat exchange plate.
In the present embodiment, the upper inlet side collector 2 of upper layer heat exchange module connects total inlet pipe 1, the upper outlet of upper layer heat exchange module
Collector 7 connects the middle inlet side collector 9 of middle layer heat exchange module, the middle outlet collector 14 of middle layer heat exchange module by the first connecting tube 8
The lower inlet side collector 12 of lower layer's heat exchange module, lower outlet collector 10 connection of lower layer's heat exchange module are connected by the second connecting tube 13
Total outlet pipe 11.N1=1, n2=2, n=3 in this programme, such as Fig. 2.Fig. 2 is only structural schematic diagram, main heat exchange plate number in actual fabrication
It measures far more than auxiliary heat-exchanging plate.
In the heat exchange module of setting auxiliary heat-exchanging plate, the tie point between mainboard piece inlet pipe 3 and inlet side collector is higher than
The tie point between plate inlet pipe 15 and inlet side collector is assisted, the tie point between plate inlet pipe 15 and inlet side collector is assisted to be higher than
Assist the tie point between plate inlet pipe 15 and auxiliary heat-exchanging plate.In general, the company between mainboard piece inlet pipe 3 and inlet side collector
Contact is located at the centre of inlet side collector short transverse, and the tie point between plate inlet pipe 15 and inlet side collector is assisted to be located at inlet side collection
The bottom side of pipe.
It is an optimal enforcement example of the invention above.It meets auxiliary heat-exchanging plate in top-down each heat exchange module
The requirement (meeting n3 > n2 > n1) that gradually increases of quantity.Meet other specific technical solutions of this requirement such as: up and down
In several heat exchange modules of arrangement, top layer does not have auxiliary heat-exchanging plate, other layers have auxiliary heat-exchanging plate.Of the invention
The citing of ordinary skill scheme: in several heat exchange modules arranged up and down, only having auxiliary heat-exchanging plate for intermediate one layer, thereon,
Lower layer all without.
In actual fabrication, auxiliary heat-exchanging plate is generally installed concentratedly in place heat exchange module the same side, close to heat exchanger shell
Body the same side, in order to implement replacement or oil removing cleaning only for auxiliary heat-exchanging plate.
Plate described in the present invention is combined by the identical metal plate of two panels, is that medium is logical between two panels metal plate
Road.
Claims (5)
1. plate journey shunt plate heat exchanger, including shell and it is mounted in shell and more than two heat exchange moulds arranged up and down
Block, heat exchange module include several main heat exchange plates and a certain number of auxiliary heat-exchanging plates installed side by side, heat exchange plate
Medium inlet side is equipped with inlet side collector, and medium outlet is equipped with outlet collector, and inlet side collector is changed by mainboard piece inlet pipe connection master
Hot plate piece, and auxiliary heat-exchanging plate is connected by auxiliary plate inlet pipe；The outlet collector of a upper heat exchange module is connected by connecting tube
Connecing the inlet side collector of next heat exchange module, it is characterised in that: auxiliary heat-exchanging No. of plates is n1 in top layer's heat exchange module, it
Auxiliary heat-exchanging No. of plates is that auxiliary heat-exchanging No. of plates is n3 in n2, then next layer of heat exchange module in next layer of heat exchange module,
The rest may be inferred, and n1, n2, n3 represent natural number, and the quantity of auxiliary heat-exchanging plate is not zero at least one layer of heat exchange module；?
It is arranged in the heat exchange module of auxiliary heat-exchanging plate, the tie point between mainboard piece inlet pipe and inlet side collector is higher than auxiliary plate inlet pipe
With the tie point between the collector of inlet side.
2. plate journey shunt plate heat exchanger as described in claim 1, it is characterised in that: in top-down each heat exchange module
The quantity of auxiliary heat-exchanging plate gradually increases.
3. plate journey shunt plate heat exchanger as claimed in claim 1 or 2, it is characterised in that: mainboard piece inlet pipe and inlet side collection
Tie point between pipe is located at the centre of inlet side collector short transverse, assists the connection point between plate inlet pipe and inlet side collector
In the bottom side of inlet side collector.
4. plate journey shunt plate heat exchanger as claimed in claim 1 or 2, it is characterised in that: auxiliary is changed in each heat exchange module
Hot plate piece is mounted on the same side of heat exchanger.
5. plate journey shunt plate heat exchanger as claimed in claim 3, it is characterised in that: auxiliary heat-exchanging plate in each heat exchange module
Piece is mounted on the same side of heat exchanger.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910665956.6A CN110260694A (en) | 2019-07-23 | 2019-07-23 | Plate journey shunt plate heat exchanger |
| PCT/CN2020/100316 WO2021012936A1 (en) | 2019-07-23 | 2020-07-06 | Plate heat exchanger having flow-dividing plate path |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910665956.6A CN110260694A (en) | 2019-07-23 | 2019-07-23 | Plate journey shunt plate heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110260694A true CN110260694A (en) | 2019-09-20 |
Family
ID=67927826
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910665956.6A Pending CN110260694A (en) | 2019-07-23 | 2019-07-23 | Plate journey shunt plate heat exchanger |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN110260694A (en) |
| WO (1) | WO2021012936A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021012936A1 (en) * | 2019-07-23 | 2021-01-28 | 李永堂 | Plate heat exchanger having flow-dividing plate path |
| CN114992917A (en) * | 2022-05-19 | 2022-09-02 | 广东工业大学 | With CO 2 Plate-shell type heat exchanger with controllable dryness and supercooling degrees of working medium |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101504256A (en) * | 2009-03-05 | 2009-08-12 | 清华大学 | Vapor-liquid separation method for vertical condenser and condenser |
| CN103528407A (en) * | 2013-11-01 | 2014-01-22 | 烟台珈群高效节能设备有限公司 | Full welding plate type socket joint heat exchanger |
| CN204910850U (en) * | 2015-09-14 | 2015-12-30 | 李永堂 | High -efficient separation vacuum condensing system of incoagulable gas |
| CN105716440A (en) * | 2015-12-18 | 2016-06-29 | 广东工业大学 | Plate type condenser with gas-liquid separation function |
| CN205748016U (en) * | 2015-12-18 | 2016-11-30 | 广东工业大学 | Gas-liquid separation plate-type condenser |
| CN210268320U (en) * | 2019-07-23 | 2020-04-07 | 李永堂 | Plate pass shunting plate heat exchanger |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55155189A (en) * | 1979-05-18 | 1980-12-03 | Babcock Hitachi Kk | Heat exchanger with inclined header |
| CN100451522C (en) * | 2006-09-22 | 2009-01-14 | 清华大学 | Liquid separating air condenser |
| CN100491871C (en) * | 2007-03-30 | 2009-05-27 | 清华大学 | Multi-stage cooling middle liquid-separation air condenser |
| CN201867086U (en) * | 2010-10-23 | 2011-06-15 | 山东早春创尔沃热泵技术有限公司 | Gas-liquid separation type air cooled condenser |
| CN203964693U (en) * | 2014-07-30 | 2014-11-26 | 烟台珈群高效节能设备有限公司 | High-efficiency condensation device |
| CN104132557A (en) * | 2014-07-30 | 2014-11-05 | 烟台珈群高效节能设备有限公司 | Intermediate liquid discharge type efficient condensation system |
| CN110260694A (en) * | 2019-07-23 | 2019-09-20 | 李永堂 | Plate journey shunt plate heat exchanger |
-
2019
- 2019-07-23 CN CN201910665956.6A patent/CN110260694A/en active Pending
-
2020
- 2020-07-06 WO PCT/CN2020/100316 patent/WO2021012936A1/en active Application Filing
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101504256A (en) * | 2009-03-05 | 2009-08-12 | 清华大学 | Vapor-liquid separation method for vertical condenser and condenser |
| CN103528407A (en) * | 2013-11-01 | 2014-01-22 | 烟台珈群高效节能设备有限公司 | Full welding plate type socket joint heat exchanger |
| CN204910850U (en) * | 2015-09-14 | 2015-12-30 | 李永堂 | High -efficient separation vacuum condensing system of incoagulable gas |
| CN105716440A (en) * | 2015-12-18 | 2016-06-29 | 广东工业大学 | Plate type condenser with gas-liquid separation function |
| CN205748016U (en) * | 2015-12-18 | 2016-11-30 | 广东工业大学 | Gas-liquid separation plate-type condenser |
| CN210268320U (en) * | 2019-07-23 | 2020-04-07 | 李永堂 | Plate pass shunting plate heat exchanger |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021012936A1 (en) * | 2019-07-23 | 2021-01-28 | 李永堂 | Plate heat exchanger having flow-dividing plate path |
| CN114992917A (en) * | 2022-05-19 | 2022-09-02 | 广东工业大学 | With CO 2 Plate-shell type heat exchanger with controllable dryness and supercooling degrees of working medium |
| CN114992917B (en) * | 2022-05-19 | 2023-08-15 | 广东工业大学 | In the form of CO 2 Plate shell type heat exchanger with controllable dryness and supercooling degree of working medium |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2021012936A1 (en) | 2021-01-28 |
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