CN106839830A - Multipaths detachable plate type autoclave evaporator - Google Patents
Multipaths detachable plate type autoclave evaporator Download PDFInfo
- Publication number
- CN106839830A CN106839830A CN201710036351.1A CN201710036351A CN106839830A CN 106839830 A CN106839830 A CN 106839830A CN 201710036351 A CN201710036351 A CN 201710036351A CN 106839830 A CN106839830 A CN 106839830A
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- China
- Prior art keywords
- plate
- heat exchange
- exchange plate
- housing
- core body
- 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
-
- 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
- F28D9/0006—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 the plate-like or laminated conduits being enclosed within a pressure vessel
-
- 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
- F28D9/0031—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 the conduits for one heat-exchange medium being formed by paired plates touching each other
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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
- F28F21/00—Constructions of heat-exchange apparatus characterised by the selection of particular materials
- F28F21/08—Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F21/00—Constructions of heat-exchange apparatus characterised by the selection of particular materials
- F28F21/08—Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
- F28F21/081—Heat exchange elements made from metals or metal alloys
- F28F21/086—Heat exchange elements made from metals or metal alloys from titanium or titanium alloys
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/08—Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning
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
This application discloses a kind of multipaths detachable plate type autoclave evaporator, including housing and plate core body;Housing is provided with shell side import and shell-side outlet;Plate core body is provided with the import of plate journey and the outlet of plate journey;Plate core body includes more than 2 heat exchange plate flows;Each heat exchange plate flow includes being sequentially overlapped more than 4 heat exchange plates of setting, the top of every heat exchange plate is provided with interior circular hole, bottom is provided with lower interior circular hole, heat exchange plate includes the first heat exchange plate, the second heat exchange plate, the 3rd heat exchange plate and the 4th heat exchange plate, upper inner circle eyelet welding is connected together after second heat exchange plate and the superposition of the 3rd heat exchange plate, lower inner circle eyelet welding is connected together, form plate pair, plate is to the heat exchange plate of peripheral solder first of side, the hot plate piece of peripheral solder the 4th of opposite side;Pass partition is provided with a through hole, and the through hole is corresponding with upper interior circular hole or lower inner circle hole site and is interconnected.Evaporator of the invention has small volume, lightweight advantage.
Description
Technical field
The disclosure relates generally to heat transfer unit (HTU) technical field, and in particular to a kind of multipaths detachable plate type autoclave evaporator.
Background technology
Energy-saving and emission-reduction are the themes of " 13 ", improve self energy efficiency and matched energy saving equipment reduction specific energy consumption
It is the main energy saving means of " 13 ".The industrial energy consumption of China 50% or so waste heat in a variety of manners is directly wasted, wherein
Recovery rate is up to 60%, and the average recovery utilization rate 30% or so of China's residual heat resources falls behind international most advanced level 10-20%,
Industrial afterheat recovery is an important component of energy conservation, is the important channel for realizing energy-saving and emission-reduction target.
Organic Rankine bottoming cycle (ORC, Organic Rankine Cycle) generation technology appears in the seventies in last century, its
Application field not only includes industrial low-temperature cogeneration, also relates to the new energy fields such as biomass energy, geothermal energy, solar energy.
Because the boiling point of organic solution is relatively low, therefore the relatively low thermal source running of temperature can be utilized.Heat source temperature can influence its workflow
The selection of body, suitable working fluid is various refrigerants (100° centigrade to 180 degree), hydrocarbon (180 degree Celsius to 250
Degree), siloxanes (250 degree to 400 degree Celsius).By the end of 2012, in operation and in the organic Rankine bottoming cycle power generation project built
More than 500 is reached, has been reached in the organic Rankine bottoming cycle TRT of operation and covered 2000 more, general assembly acc power has existed
2000MW or so, maximum single-machine capacity reaches 14000kW.So far, organic Rankine bottoming cycle (ORC) technology has been generally considered
It is the maximally effective technology of low temperature heat energy power-conversion in realizing.
But because the Low Temperature Difference heat-transfer character of middle low temperature heat energy necessarily causes evaporator to use common pipe heat exchanger, from
And make organic rankine cycle system equipment it is huge, working medium filling amount is big, cost is high, heat recovery efficiency is low, greatly hamper
The popularization and application of the technology.
The content of the invention
In view of drawbacks described above of the prior art or deficiency, expect to provide a kind of small volume, lightweight multipaths removable
Board-like autoclave evaporator.
The present invention provides a kind of multipaths detachable plate type autoclave evaporator, including housing and the plate being arranged in the housing
Piece core body;
The housing is provided with shell side import and shell-side outlet;
The plate core body is provided with the import of plate journey and the outlet of plate journey;
The plate core body includes more than 2 heat exchange plate flows being connected by pass partition;
Each described heat exchange plate flow includes being sequentially overlapped more than 4 heat exchange plates of setting, the every heat exchanger plates
The top of piece is provided with interior circular hole, and bottom is provided with lower interior circular hole, and the heat exchange plate includes the first heat exchange plate, the second heat exchanger plates
Upper inner circle eyelet welding after piece, the 3rd heat exchange plate and the 4th heat exchange plate, second heat exchange plate and the superposition of the 3rd heat exchange plate
It is connected together, lower inner circle eyelet welding is connected together, forms a plate pair, periphery of the plate to the second heat exchange plate of side
Weld the first heat exchange plate, peripheral solder fourth hot plate piece of the plate to the 3rd heat exchange plate of opposite side;
The pass partition is provided with a through hole, and the through hole is corresponding with upper interior circular hole or lower inner circle hole site and mutually interconnects
It is logical.
The end of the plate core body is placed on together by bend pipe connecting plate journey import, plate journey import and the outlet of plate journey
On one flange, the flange connects the housing, and the plate core body is by can be from the housing after dismantling the flange
Extract out.
The housing is autoclave structure, guide rail is provided with the housing, after the plate core body is used to be slided on guide rail
In the housing.
The heat exchange plate is circular or Long Circle structure, is set between the outer wall and the inner walls of the plate core body
There are bypass block and/or impingement baffle.
The surface of the heat exchange plate is evenly distributed with arc fin or ball is convex and ball impression, when convex ball and ball impression is distributed,
In the plate pair, the ball impression of first heat exchange plate and the second heat exchange plate opposite face is corresponding with ball impression, and ball is convex
It is convex with ball corresponding.
The depth of the arc fin is 2~10mm.
Convex and ball impression the depth of the ball is 2~5 millimeters, a diameter of 8~15 millimeters.
The shell side import is located at the bottom of the housing, and the shell-side outlet is located at the top of the housing, the shell
Wire mesh demister is provided with the shell space of journey outlet bottom.
1.2-2 times of a diameter of plate core diameter of the housing;The thickness of the pass partition is 3~20mm.
The material of the heat exchange plate is 254SMO high-alloy stainless steels, 316L stainless steels or Ti;It is described be welded as it is complete from
Dynamic laser welding.
Compared with prior art, beneficial effects of the present invention:
(1), using plates such as 316L, Ti or 254SMO, good corrosion resistance can for this kind of autoclave evaporator of structure type
The replacement frequency of equipment is greatly reduced, the mounting cost and maintenance cost of device are reduced to greatest extent, and ensure that device is long
Cycle safe and reliable operation.
(2) core body of heat exchange plate using corrugated plating can augmentation of heat transfer, heat exchange efficiency is high, reduces terminal temperature difference, lifting
Tow taste heat organic efficiency.
(3) heat exchange core body uses the structure-reinforced heat transfer of multipaths, further lifts heat transfer efficiency, reduces heat exchange area, subtracts
Skinny device size and housing size, reduce working medium filling amount and system fading margin reaction time in housing.
(4) heat exchange core body is connected with housing using flange, and removable structure facilitates core pulling clean and maintenance and maintenance.
(5) bypass block can be set up in housing, reduces working medium filling amount.
Brief description of the drawings
By the detailed description made to non-limiting example made with reference to the following drawings of reading, the application other
Feature, objects and advantages will become more apparent upon:
Fig. 1 is the structural representation of multipaths detachable plate type autoclave evaporator provided in an embodiment of the present invention;
Fig. 2 is the side view of Fig. 1;
Fig. 3 is the structural representation of the first heat exchange plate provided in an embodiment of the present invention;
Fig. 4 is the structural representation of second heat exchange plate provided in an embodiment of the present invention;
Fig. 5 is the structural representation of multipaths plate core body provided in an embodiment of the present invention.
Wherein, the import of 1- plates journey, the outlet of 2- plates journey, the import of 3- shell sides, 4- shell-side outlets, 5- exhaust valve ports, 6- safety valves
Mouth, 7- sewage draining exits, 8- thermometer bosses, 9- pressure gauge connections, 10- housings, 11- plates core body, 12- wire mesh demisters, 13- prevent
It is punching, 14- guide rails, 15- heat exchange plates, 16- pass partitions, 17- bypasses block, 18- hot sides medium, 19- cold sides medium, 20 curved
Pipe, 21 flanges, interior circular hole on 22, circular holes in 23 times.
Specific embodiment
The application is described in further detail with reference to the accompanying drawings and examples.It is understood that this place is retouched
The specific embodiment stated is used only for explaining related invention, rather than the restriction to the invention.It also should be noted that, in order to
It is easy to description, the part related to invention is illustrate only in accompanying drawing.
It should be noted that in the case where not conflicting, the feature in embodiment and embodiment in the application can phase
Mutually combination.Describe the application in detail below with reference to the accompanying drawings and in conjunction with the embodiments.
Refer to Fig. 1, Fig. 2 and Fig. 5, a kind of multipaths detachable plate type autoclave evaporator, including housing 10 and be arranged on shell
Plate core body 11 in body 10;
Housing 10 is provided with shell side import 3 and shell-side outlet 4;
Plate core body 11 is provided with plate journey import 1 and plate journey outlet 2;
Plate core body 11 includes more than 2 heat exchange plate flows being connected by pass partition 16;
Each described heat exchange plate flow includes being sequentially overlapped more than 4 heat exchange plates 15 of setting, every heat exchange plate
15 top is provided with interior circular hole 22, and bottom is provided with lower interior circular hole 23, and heat exchange plate 15 includes the first heat exchange plate, the second heat exchange
Upper interior circular hole after plate, the 3rd heat exchange plate and the 4th heat exchange plate, second heat exchange plate and the superposition of the 3rd heat exchange plate
22 weld together, and lower interior circular hole 23 welds together, and form a plate pair, second heat exchange plate of the plate to side
The heat exchange plate of peripheral solder first, peripheral solder fourth hot plate piece of the plate to the 3rd heat exchange plate of opposite side;
Pass partition 16 is provided with a through hole, and the through hole is corresponding with upper interior circular hole 22 or the lower position of interior circular hole 23 and mutual
Connection.
Upper interior circular hole or lower interior circular hole on a piece of heat exchange plate of the present invention are arranged symmetrically, and multiple heat exchange plate stackings are affixed
A heat exchange process, multiple heat exchange process composing plate piece core bodys are formed afterwards.Evaporator of the invention have small volume, it is lightweight,
Heat transfer efficiency advantage high.
On the basis of above-described embodiment, the end of plate core body 11 passes through the connecting plate journey import 1 of bend pipe 20 to the present embodiment,
Plate journey import 1 and plate journey outlet 2 are placed on same flange 21, and the connection housing 10 of flange 21, plate core body 11 passes through disassembly method
Can be extracted out from housing 10 after blue 21.
The present invention realizes that plate journey outlet 2 and plate journey import 1, in flange homonymy, facilitate dismounting by increasing by one section of bend pipe.
Further, guide rail 14 is provided with housing 10, plate core body 11 is arranged on housing after being used to be slided on guide rail 14
In 10.Plate core body of the invention is pushed in housing by guide rail, by setting guide rail so that plate core body is convenient install and
Dismounting.
As shown in figure 1, housing 10 is autoclave structure, plate core body 11 is arranged on inside housing 10, under plate core body 11
Surface is contacted with the bottom of housing 10 by guide rail 14, has shell-side outlet 4, exhaust valve port 5, safety valve in the top surface of housing 10
Mouth 6, thermometer boss 8, pressure gauge connection 9, have sewage draining exit 7 in the lower surface of housing 10, and shell side import 3 can be arranged in housing
Bottom or housing upper;Plate journey of the invention import 1 can be arranged in the upper circular hole of plate core 11, it is also possible to be arranged in lower circular hole.
Referring to Fig. 3 and Fig. 4, for the ease of welding, heat exchange plate 15 is circular or Long Circle structure, outside plate core body 11
17 and/or impingement baffle 13 are provided between wall and the inwall of housing 10.Heat exchange plate shown in Fig. 2 is circular wave plate, shown in Fig. 3
Heat exchange plate is Long Circle corrugated plating.The surface of heat exchange plate is corrugated, spherical or other plate type heat exchanger runner forms.
Bypass block of the invention is arranged on the cylindrical and inner walls between of plate core body, and bypass block Main Function is
Certain space is occupied, reduces housing internal volume, reach the purpose for reducing working medium filling amount.Impingement baffle is also disposed at plate core body
It is cylindrical and inner walls between, for reducing into housing the flow velocity of liquid or gas-liquid two-phase, making it into housing and distribute
It is as far as possible uniform.Impingement baffle can be a feed liquor distributor, or one piece of baffle plate.
On the basis of above-described embodiment, the surface of heat exchange plate 15 is evenly distributed with arc fin to the present embodiment, in ripple
Line shape, it is preferable that the depth of arc fin is 2~10mm.
On the basis of above-described embodiment, the surface of heat exchange plate 15 is evenly distributed with that ball is convex and ball impression to the present embodiment;
The ball impression of the plate centering, first heat exchange plate and the second heat exchange plate opposite face is corresponding with ball impression, ball it is convex with
The convex correspondence of ball.The fin of strip can also be set on certain heat exchange plate, increased the area of heat exchange.
Preferably, convex and ball impression the depth of ball is 2~5 millimeters, a diameter of 8~15 millimeters.
Heat exchange plate using corrugated plating or convex with ball in sheet material of ball impression, can augmentation of heat transfer, heat exchange efficiency is high, reduces
Terminal temperature difference, lifts tow taste heat organic efficiency.
Referring to Fig. 1 and Fig. 2, on the basis of above-described embodiment, shell side import 3 is located at the bottom of housing 10 to the present embodiment,
Shell-side outlet 4 is located at the top of housing 10, and wire mesh demister 12 is provided with the shell space of the bottom of shell-side outlet 4.
The present embodiment on the basis of above-described embodiment, 1.2-2 times of a diameter of diameter of plate core body 11 of housing 10;Point
The thickness of journey dividing plate 16 is 3~20mm.
The present invention is smaller than diameter of the housing by the diameter of arranging plate piece core body, in housing and plate core body outer circumference surface and shell
The space formed between internal periphery is gas-liquid separation space, and wire mesh demister is disposed with gas-liquid separation space, enters one
Step separates droplet, it is ensured that gaseous phase outlet does not press from both sides liquid.
Referring to Fig. 3 and Fig. 4, it is preferable that the material of heat exchange plate 15 be 254SMO high-alloy stainless steels, 316L stainless steels or
Ti;It is described to be welded as fully-automatic laser welding.
The present invention is immersed in kettle using the tube bank of plate core body substitution autoclave heat exchanger, the evaporator have small volume,
The advantage that lightweight, heat transfer efficiency is high, working medium filling amount is small.Heat exchange plate material is high using 316L stainless steels, Ti or 254SMO
Stainless steel alloy etc., it is corrosion-resistant, the replacement frequency of equipment can be greatly reduced, the mounting cost of device is reduced to greatest extent
And maintenance cost, and ensure device long period safe and reliable operation.
In order to ensure the reliability of evaporator, hot side and cold side two media should be made not to contact, do not leaked, equipment must be close
It is tamping close.Weld to form plate core body by fully-automatic laser between the heat exchange plate of evaporator heat transfer element two of the invention.Make
Use full-welding plate-type structure type so that the evaporator is while heat-exchangers of the plate type efficient heat transfer performance is played, it is ensured that
Sealing property, improves bearing capacity, equipment safety reliability.
Referring to Fig. 1, Fig. 2 and Fig. 5, the forming process of plate core body 11 of the present invention is:2 heat exchange plates are superimposed first,
Its interior circular hole is contacted with each other, and two interior circular holes are respectively welded at into one plate pair of formation together, and many plates are to by outer
Circle contacts with each other, and the plate of coaxial placement is respectively welded to foreign round to form a heat exchange plate flow, by multiple heat exchange plates
Flow is connected by pass partition 16, forms plate core body, and passage constitutes shell between the plate pair and plate pair of plate core body 11
Cheng Tongdao, runner constitutes plate journey runner between plate pair and plate pair in plate core body 11.In the end of plate core body 11 by curved
Be placed on core plate journey inlet and outlet on same flange by pipe, realizes that multipaths heat exchange plate core body is removable.Pass partition with
Heat exchange plate inner circle is with position Jin Kaiyi holes.
Referring to Fig. 1 and Fig. 5, the operation principle of evaporator of the present invention:Hot side medium 18 enters plate core body from plate journey import 1
11, in plate core body 11 after repeatedly turning back, flowed out from plate journey outlet 2 by bend pipe, bend pipe 20 also functions to part heating
Effect.Cold side medium 19 is entered in housing 10 from shell side import 3 with liquid phase or gas-liquid two-phase, and it is high to set up liquid level in housing 10
Degree, liquid enters from the bottom of plate core body 11, and thermogenetic gas entrainment portions drop is changed by gas-liquid by plate core body 11
Separated space and wire mesh demister separate drop, and gas is discharged from shell-side outlet 4.Yield supplement liquid phase according to gas phase, dimension
Hold liquid level in housing 10 within a certain range.Bypass block 17 can be set up in housing 10, reduces working medium filling amount.
Above description is only the preferred embodiment and the explanation to institute's application technology principle of the application.People in the art
Member is it should be appreciated that involved invention scope in the application, however it is not limited to the technology of the particular combination of above-mentioned technical characteristic
Scheme, while should also cover in the case where the inventive concept is not departed from, is carried out by above-mentioned technical characteristic or its equivalent feature
Other technical schemes for being combined and being formed.Such as features described above has similar work(with (but not limited to) disclosed herein
The technical scheme that the technical characteristic of energy is replaced mutually and formed.
Claims (10)
1. a kind of multipaths detachable plate type autoclave evaporator, it is characterised in that including housing and the plate being arranged in the housing
Piece core body;
The housing is provided with shell side import and shell-side outlet;
The plate core body is provided with the import of plate journey and the outlet of plate journey;
The plate core body includes more than 2 heat exchange plate flows being connected by pass partition;
Each described heat exchange plate flow includes being sequentially overlapped more than 4 heat exchange plates of setting, every heat exchange plate
Top is provided with interior circular hole, and bottom is provided with lower interior circular hole, the heat exchange plate include the first heat exchange plate, the second heat exchange plate,
Upper inner circle eyelet welding is connected on after 3rd heat exchange plate and the 4th heat exchange plate, second heat exchange plate and the superposition of the 3rd heat exchange plate
Together, lower inner circle eyelet welding is connected together, and forms a plate pair, peripheral solder of the plate to the second heat exchange plate of side
First heat exchange plate, peripheral solder fourth hot plate piece of the plate to the 3rd heat exchange plate of opposite side;
The pass partition is provided with a through hole, and the through hole is corresponding with upper interior circular hole or lower inner circle hole site and is interconnected.
2. multipaths detachable plate type autoclave evaporator according to claim 1, it is characterised in that the end of the plate core body
End is placed on same flange by bend pipe connecting plate journey import, plate journey import and the outlet of plate journey, and the flange connects institute
Housing is stated, the plate core body from the housing after dismantling the flange by that can extract out.
3. multipaths detachable plate type autoclave evaporator according to claim 1, it is characterised in that the housing is autoclave knot
Structure, is provided with guide rail in the housing, the plate core body is arranged in the housing after being used to be slided on guide rail.
4. the multipaths detachable plate type autoclave evaporator according to claim any one of 1-3, it is characterised in that the heat exchange
Plate is circular or Long Circle structure, be provided between the outer wall and the inner walls of the plate core body bypass block and/or
Impingement baffle.
5. multipaths detachable plate type autoclave evaporator according to claim 4, it is characterised in that the table of the heat exchange plate
Face is evenly distributed with arc fin or ball is convex and ball impression, and when convex ball and ball impression is distributed, in the plate pair, described first changes
The ball impression of hot plate piece and the second heat exchange plate opposite face is corresponding with ball impression, and ball is convex convex with ball corresponding.
6. multipaths detachable plate type autoclave evaporator according to claim 4, it is characterised in that the depth of the arc fin
It is 2~10mm to spend.
7. multipaths detachable plate type autoclave evaporator according to claim 6, it is characterised in that the ball is convex and ball impression
Depth is 2~5 millimeters, a diameter of 8~15 millimeters.
8. multipaths detachable plate type autoclave evaporator according to claim 3, it is characterised in that the shell side import is located at
The bottom of the housing, the shell-side outlet is located at the top of the housing, is set in the shell space of the shell-side outlet bottom
There is wire mesh demister.
9. multipaths detachable plate type autoclave evaporator according to claim 8, it is characterised in that the housing it is a diameter of
1.2-2 times of plate core diameter;The thickness of the pass partition is 3~20mm.
10. multipaths detachable plate type autoclave evaporator according to claim 1, it is characterised in that the heat exchange plate
Material is 254SMO high-alloy stainless steels, 316L stainless steels or Ti;It is described to be welded as fully-automatic laser welding.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201710036351.1A CN106839830A (en) | 2017-01-17 | 2017-01-17 | Multipaths detachable plate type autoclave evaporator |
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Application Number | Priority Date | Filing Date | Title |
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CN201710036351.1A CN106839830A (en) | 2017-01-17 | 2017-01-17 | Multipaths detachable plate type autoclave evaporator |
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ID=59124648
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CN201710036351.1A Pending CN106839830A (en) | 2017-01-17 | 2017-01-17 | Multipaths detachable plate type autoclave evaporator |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN109442870A (en) * | 2018-10-25 | 2019-03-08 | 江西赣锋锂业股份有限公司 | A kind of method of dry monohydrate lithium hydroxide |
CN110887389A (en) * | 2019-12-13 | 2020-03-17 | 江西新电汽车空调系统有限公司 | Multi-flow serial plate heat exchanger |
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CN205867607U (en) * | 2016-07-08 | 2017-01-11 | 上海齐耀热能工程有限公司 | Kettle -type reboiler of board tubular |
CN106322339A (en) * | 2015-07-06 | 2017-01-11 | 天津华赛尔传热设备有限公司 | Plate type steam generator |
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CN103827620A (en) * | 2011-09-22 | 2014-05-28 | 阿尔法拉瓦尔股份有限公司 | A plate evaporator of the falling film type, and a plate evaporator apparatus having such a plate evaporator arranged in a housing |
CN102853695A (en) * | 2012-09-28 | 2013-01-02 | 陈建平 | Method and product for improving heat exchanging efficiency of multi-path plate-type heat exchanger |
CN202951261U (en) * | 2012-11-28 | 2013-05-29 | 江山顺泰化工机械工程有限公司 | Heat transmission plate type evaporator |
CN103808190A (en) * | 2014-01-27 | 2014-05-21 | 中国船舶重工集团公司第七一一研究所 | Dimple type heat exchange core body and lamella heat exchanger with same |
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Publication number | Priority date | Publication date | Assignee | Title |
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CN109442870A (en) * | 2018-10-25 | 2019-03-08 | 江西赣锋锂业股份有限公司 | A kind of method of dry monohydrate lithium hydroxide |
CN109442870B (en) * | 2018-10-25 | 2020-11-03 | 江西赣锋锂业股份有限公司 | Method for drying lithium hydroxide monohydrate |
CN110887389A (en) * | 2019-12-13 | 2020-03-17 | 江西新电汽车空调系统有限公司 | Multi-flow serial plate heat exchanger |
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