CN115435615A - Corrugated pipe heat exchanger with heat transfer enhancement effect - Google Patents
Corrugated pipe heat exchanger with heat transfer enhancement effect Download PDFInfo
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- CN115435615A CN115435615A CN202211174784.0A CN202211174784A CN115435615A CN 115435615 A CN115435615 A CN 115435615A CN 202211174784 A CN202211174784 A CN 202211174784A CN 115435615 A CN115435615 A CN 115435615A
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- 238000012546 transfer Methods 0.000 title claims abstract description 43
- 230000000694 effects Effects 0.000 title claims abstract description 22
- 239000007788 liquid Substances 0.000 claims abstract description 254
- 238000005192 partition Methods 0.000 claims abstract description 51
- 238000005259 measurement Methods 0.000 claims description 5
- 238000005457 optimization Methods 0.000 description 6
- 239000012530 fluid Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000006978 adaptation Effects 0.000 description 3
- 230000004308 accommodation Effects 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
- 241000521257 Hydrops Species 0.000 description 1
- 206010030113 Oedema Diseases 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
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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
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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
- F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
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- Engineering & Computer Science (AREA)
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- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention relates to a corrugated pipe heat exchanger with a heat transfer enhancement effect. The corrugated pipe heat exchanger with the heat transfer enhancement effect comprises a heat exchange shell, wherein the heat exchange shell is connected to an outer supporting piece, a first liquid inlet, a first liquid outlet, a second liquid inlet and a second liquid outlet are connected to the surface of the heat exchange shell, the first liquid inlet is communicated with the first liquid outlet, liquid A is input into the first liquid inlet, the second liquid inlet is communicated with the second liquid outlet, liquid B is input into the second liquid inlet, two groups of first partition plate pieces are arranged inside the heat exchange shell, a connecting pipe is arranged between the two groups of first partition plate pieces, a metering piece and a heat exchange assembly are further arranged in the two groups of first partition plate pieces, and the metering piece is used for collecting the volume of the liquid A in the two groups of first partition plate pieces; the corrugated pipe heat exchanger with the heat transfer enhancement effect is simple in structure, convenient to operate, flexible to use and high in adaptability, and meets the requirements of different amounts of liquid heat exchange.
Description
Technical Field
The invention belongs to the technical field of heat exchange shells, and particularly relates to a corrugated pipe heat exchanger with a heat transfer enhancement effect.
Background
The heat exchanger is an energy-saving device for transferring heat between materials between two or more fluids with different temperatures, and is used for transferring heat from the fluid with higher temperature to the fluid with lower temperature to make the temperature of the fluid reach the index specified by the process so as to meet the requirements of process conditions, and is also one of main devices for improving the utilization rate of energy. It can help some liquid to lower the temperature, and some liquid heats up.
The shell structure among the current bellows heat exchanger is comparatively single, only uses according to corresponding capacity after the casing of general heat exchanger is stereotyped, and the heat transfer that different liquid capacities of unable fine adaptation go on uses for some users including the laboratory need purchase the heat exchanger of a large amount of different models and use, uses with this service environment under the different liquid capacities of adaptation.
Disclosure of Invention
The present invention aims at providing a corrugated tube heat exchanger with simple structure and reasonable design and heat transfer strengthening effect to solve the above problems.
The invention realizes the purpose through the following technical scheme:
the utility model provides a bellows heat exchanger with effect is reinforceed in heat transfer, this casing includes heat transfer shell, heat transfer shell connects on outer support piece, heat transfer shell's surface is connected with first inlet, first liquid outlet, second inlet and second liquid outlet, first inlet and first liquid outlet communicate each other, and first inlet input A liquid, second inlet and second liquid outlet communicate each other, and second inlet input B liquid, heat transfer shell's inside is provided with two sets of first baffle pieces, and is two sets of be provided with the connecting pipe between the first baffle piece, and is two sets of still be provided with measurement piece and heat transfer assembly in the first baffle piece, measurement piece gathers two sets of the volume of A liquid in the first baffle piece, heat transfer assembly includes feed liquor valve and liquid valve, feed liquor valve and liquid valve are connected respectively in the both ends of connecting pipe, just feed liquor valve and liquid valve are connected with corresponding first baffle piece respectively, first inlet and first set up between first baffle piece, second set up outside two sets of first baffle pieces, liquid inlet and liquid valve are based on the liquid volume of a between the first baffle piece, and liquid inlet and liquid valve carry out the corresponding liquid volume of liquid and liquid inlet and liquid control liquid and liquid inlet to the corresponding liquid of liquid valve, make the liquid volume in the heat transfer shell carry out the liquid.
As a further optimization scheme of the invention, the housing is connected with a control module, the control module controls and connects the metering member, the liquid inlet valve and the liquid outlet valve, and the liquid inlet and outlet amounts of the first liquid inlet, the first liquid outlet, the second liquid inlet and the second liquid outlet can be controlled.
As a further optimized scheme of the present invention, the first liquid inlet is disposed at the upper portion of the heat exchange housing, the first liquid outlet is disposed at the lower portion of the heat exchange housing, a second partition plate member is disposed below a liquid outlet end of the first liquid inlet, a side cross section of the second partition plate member is arc-shaped, the second partition plate member is located above all the connecting pipes, and the liquid a output by the first liquid inlet is guided to the bottom by the second partition plate member and spreads upward from the bottom.
As a further optimization scheme of the invention, the second liquid outlet is arranged at the outer side of the heat exchange shell and close to the bottom.
As a further optimization scheme of the present invention, two groups of the first partition plates are sequentially divided into a first area, an adjustment area, and a second area, an adjustment plate is disposed at the head and the tail end of the adjustment area, a first connection pipe is disposed in the first area, a second connection pipe is disposed in the adjustment area, a third connection pipe is disposed in the second area, the first connection pipe and the third connection pipe are hoses, the second connection pipe is a hard pipe, and the adjustment plate adjusts the distance between the second connection pipes.
As a further optimized solution of the present invention, the second connection pipe is divided into an adjustable connection pipe and a fixed core pipe, the adjustable connection pipe is disposed around the fixed core pipe, and the adjustment plate adjusts a distance between the adjustable connection pipe and the fixed core pipe.
As a further optimization scheme of the invention, the adjustable connecting pipes are distributed in a multi-layer surrounding manner.
As a further optimization scheme of the invention, the adjusting plate comprises a fixed plate and a rotating plate, a first chute piece is arranged on the surface of the fixed plate, a second chute piece is arranged on the surface of the rotating plate, the second connecting pipe slides in the second chute piece, the second connecting pipe penetrates through the first chute piece and slides in the first chute piece, a driving assembly is arranged in the heat exchange shell and drives the rotating plate to rotate, and the second connecting pipe moves towards the center or away from the center along the first chute piece and the second chute piece.
As a further optimization scheme of the invention, an adjusting inner tube is arranged inside the heat exchange shell, the first liquid inlet and the first liquid outlet are both inserted into the adjusting inner tube, the adjusting inner tube comprises a plurality of groups of hard plates and a plurality of groups of soft plates, the hard plates and the soft plates are arranged at intervals and are arranged in a surrounding manner to form a tubular structure, the adjusting inner tube further comprises an adjusting component, and the adjusting component adjusts the hard plates or/and the soft plates to approach or depart from the tubular center.
As a further optimized scheme of the invention, the adjusting assembly comprises a pulling piece and a telescopic rod piece, the telescopic end of the telescopic rod piece is fixedly connected with the outer surface of the hard plate, and the pulling end of the pulling piece is connected with the outer center of the soft plate.
The invention has the beneficial effects that: the invention can selectively adopt partial connecting pipes to carry out heat exchange treatment by quantifying the volume of liquid entering the heat exchanger, changes the prior full-liquid heat exchange mode and adopts a liquid loading heat exchange mode, and improves the applicability of the heat exchanger; moreover, the gathering degree of the connecting pipe and the size of the inner pipe can be adjusted, so that the heat exchange conditions of different volumes or heat can be adapted; whole casing, simple structure, convenient operation uses in a flexible way, has very strong adaptability, satisfies the liquid heat transfer of different volume and uses.
Drawings
FIG. 1 is a schematic view of the overall structure of the present invention;
FIG. 2 is a schematic view of the structure of FIG. 1 from another perspective according to the present invention;
FIG. 3 is a schematic top view of the structure of FIG. 2 of the present invention;
fig. 4 is a schematic view of the internal structure of the heat exchange housing 11 of the present invention;
FIG. 5 is a schematic view of the structure of the fixing plate of the present invention;
FIG. 6 is a schematic view of the rotating plate member of the present invention;
FIG. 7 is a schematic view showing the internal structure of the heat exchange shell 11 with the inner tube for regulation according to the present invention;
FIG. 8 is a schematic view of the present invention in a configuration for adjusting the contraction of the inner tube;
FIG. 9 is a schematic view of the present invention adjusting the expansion of the inner tube.
In the figure: 1. an outer support; 11. a heat exchange housing; 12. a first liquid inlet; 13. a first liquid outlet; 14. a second liquid inlet; 15. a second liquid outlet; 16. a support table; 2. a first divider member; 21. a first region; 22. a regulatory region; 23. a second region; 3. a second divider member; 4. a metering member; 5. a heat exchange assembly; 51. a liquid inlet valve; 52. a first connecting pipe; 53. a second connecting pipe; 54. a third connecting pipe; 55. a liquid outlet valve; 6. adjusting the plate; 61. fixing a plate; 62. a first runner component; 63. a core tube; 64. rotating the plate; 65. a second runner component; 66. a drive member; 67. a drive motor; 7. adjusting the inner pipe; 71. a hard plate; 72. a soft plate; 73. a pulling member; 74. a telescopic rod member; 75. a clamping member.
Detailed Description
The present application will now be described in further detail with reference to the drawings, it should be noted that the following detailed description is given for illustrative purposes only and is not to be construed as limiting the scope of the present application, as those skilled in the art will be able to make numerous insubstantial modifications and adaptations to the present application based on the above disclosure.
Example 1
As shown in fig. 1 to 4, a corrugated tube heat exchanger with a heat transfer enhancement effect includes a heat exchange housing 11, the heat exchange housing 11 is connected to an outer support member 1, a first liquid inlet 12, a first liquid outlet 13, a second liquid inlet 14 and a second liquid outlet 15 are connected to a surface of the heat exchange housing 11, the first liquid inlet 12 is communicated with the first liquid outlet 13, a liquid a is input into the first liquid inlet 12, the second liquid inlet 14 is communicated with the second liquid outlet 15, a liquid B is input into the second liquid inlet 14, two sets of first partition plates 2 are disposed inside the heat exchange housing 11, a connecting pipe is disposed between the two sets of first partition plates 2, a metering member 4 and a heat exchange assembly 5 are further disposed inside the two sets of first partition plates 2, the metering member 4 collects a volume of the liquid a in the two sets of first partition plates 2, the heat exchange assembly 5 includes a liquid inlet valve 51 and a liquid outlet valve 55, the liquid inlet valve 51 and the liquid outlet valve 55 are respectively connected to two ends of the connecting pipe, the liquid inlet valve 51 and the liquid outlet valve 55 are respectively connected to the first partition plate 2, the liquid inlet 12 and the liquid outlet valve 55 are connected to the liquid outlet valve 13, and the liquid valve 55 are connected to the liquid outlet valve 5, and the liquid inlet valve 13 and the liquid valve 5 is connected to the liquid outlet valve 5, and the liquid valve 5.
It should be noted that, in the above solution, the amount of the liquid a entering the first partition member 2 is measured by the metering member 4, specifically, the amount of the liquid a may be measured by providing a flow meter in the first liquid inlet 12, or by providing a flow meter in the first liquid outlet 13, corresponding flow conversion is performed based on the liquid inlet and the liquid outlet, so as to obtain the amount of the liquid a remaining in the casing, and then the volume of the liquid a is obtained based on the space in the casing.
Furthermore, the housing is connected with a control module, the control module controls and connects the metering member 4, the liquid inlet valve 51 and the liquid outlet valve 55, and controls the liquid inlet and outlet amounts of the first liquid inlet 12, the first liquid outlet 13, the second liquid inlet 14 and the second liquid outlet 15.
It should be noted that the control module may be configured by a processor (C6 a816X processor) with a DSP or an ARM architecture, a memory cell, a memory disc, and a controller single chip microcomputer (AT 89C51 single chip microcomputer), and is disposed outside the housing.
Further, first inlet 12 sets up in the upper portion of heat transfer shell 11, first liquid outlet 13 sets up in the lower part of heat transfer shell 11, the play liquid end below of first inlet 12 is provided with second partition plate spare 3, the side cross-section of second partition plate spare 3 is the arc, second partition plate spare 3 is located the top of all connecting pipes, the A liquid of first inlet 12 output is guided to the bottom by second partition plate spare 3, and is upwards stretched by the bottom.
In this embodiment, set up first inlet 12 in the top, be in order to prevent that the advanced interior liquid of income casing from leading to the fact the influence to the follow-up feed liquor of first inlet 12, can effectually prevent through setting up second partition plate spare 3 that liquid whereabouts from leading to the fact the influence to the pipeline of top, this embodiment has changed the mode of full liquid heat transfer in the past, adopts the mode of hydrops heat transfer, has improved the suitability of heat exchanger itself.
Further, the second liquid outlet 15 is disposed outside the heat exchange housing 11 and near the bottom.
Example 2
As shown in fig. 1 to 6, a corrugated tube heat exchanger with a heat transfer enhancement effect includes a heat exchange housing 11, the heat exchange housing 11 is connected to an outer support member 1, a first liquid inlet 12, a first liquid outlet 13, a second liquid inlet 14 and a second liquid outlet 15 are connected to a surface of the heat exchange housing 11, the first liquid inlet 12 is communicated with the first liquid outlet 13, a liquid a is input into the first liquid inlet 12, the second liquid inlet 14 is communicated with the second liquid outlet 15, a liquid B is input into the second liquid inlet 14, two sets of first partition plates 2 are disposed inside the heat exchange housing 11, a connecting pipe is disposed between the two sets of first partition plates 2, a metering member 4 and a heat exchange assembly 5 are further disposed inside the two sets of first partition plates 2, the metering member 4 collects a volume of the liquid a in the two sets of first partition plates 2, the heat exchange assembly 5 includes a liquid inlet valve 51 and a liquid outlet valve 55, the liquid inlet valve 51 and the liquid outlet valve 55 are respectively connected to two ends of the connecting pipe, the liquid inlet valve 51 and the liquid outlet valve 55 are respectively connected to the first partition plate 2, the liquid inlet 12 and the liquid outlet valve 55 are connected to the liquid outlet valve 13, and the liquid valve 55 are connected to the liquid outlet valve 5, and the liquid inlet valve 13 and the liquid valve 5 is connected to the liquid outlet valve 5, and the liquid valve 5.
It should be noted that, in the above solution, the amount of the liquid a entering the first partition member 2 is measured by the metering member 4, specifically, the amount of the liquid a may be measured by providing a flow meter in the first liquid inlet 12, or by providing a flow meter in the first liquid outlet 13, corresponding flow conversion is performed based on the liquid inlet and the liquid outlet, so as to obtain the amount of the liquid a remaining in the casing, and then the volume of the liquid a is obtained based on the space in the casing.
Further, the housing is connected with a control module, the control module controls and connects the metering member 4, the liquid inlet valve 51 and the liquid outlet valve 55, and controls the liquid inlet and outlet amounts of the first liquid inlet 12, the first liquid outlet 13, the second liquid inlet 14 and the second liquid outlet 15.
It should be noted that the control module may be implemented by using a processor (C6 a816X processor) with a DSP or ARM architecture, a memory cell, a memory disc, and a controller single chip microcomputer (AT 89C51 single chip microcomputer), and is disposed outside the housing.
Further, the first liquid inlet 12 is arranged at the upper part of the heat exchange shell 11, the first liquid outlet 13 is arranged at the lower part of the heat exchange shell 11, a second partition plate 3 is arranged below the liquid outlet end of the first liquid inlet 12, the side section of the second partition plate 3 is arc-shaped, the second partition plate 3 is positioned above all the connecting pipes, and the liquid a output by the first liquid inlet 12 is guided to the bottom by the second partition plate 3 and spreads upwards from the bottom; the second liquid outlet 15 is disposed outside the heat exchange housing 11 and near the bottom.
Further, the two groups of first partition plate members 2 are sequentially divided into a first area 21, an adjusting area 22 and a second area 23, an adjusting plate member 6 is disposed at the head end and the tail end of the adjusting area 22, a connecting pipe in the first area 21 is a first connecting pipe 52, a connecting pipe in the adjusting area 22 is a second connecting pipe 53, a connecting pipe in the second area 23 is a third connecting pipe 54, the first connecting pipe 52 and the third connecting pipe 54 are hoses, the second connecting pipe 53 is a hard pipe, and the adjusting plate member 6 adjusts the distance between the second connecting pipes 53.
Wherein, the second connecting pipe 53 is divided into an adjustable connecting pipe and a fixed core pipe 63, the adjustable connecting pipe is arranged around the fixed core pipe 63, and the adjusting plate 6 adjusts the distance between the adjustable connecting pipe and the fixed core pipe 63.
It should be noted that, in the use of this scheme in practice, the distance between adjustable connecting pipe and fixed core pipe 63 can be adjusted to the structure of arbitrary regulation plate 6, through adjusting the distance between the two, promptly in the actual use, can be located the quantity below the A liquid level through the adjustable connecting pipe, adjusts heat exchange efficiency and heat transfer effect.
In this embodiment, the adjustable connecting pipe is the multilayer and encircles the formula and distributes, and the multilayer mode is convenient for adjust the multilayer and is located the adjustable connecting pipe of bottom, and it is still required to explain, adjusts plate 6 in the accommodation process of reality, needs to ensure to adjust controllable to the actual position of each connecting pipe of better understanding is convenient for based on actual position and actual A liquid volume, selects corresponding connecting pipe to use.
Further, in this embodiment, the adjusting plate 6 has a structure that the adjusting plate 6 includes a fixed plate 61 and a rotating plate 64, a first sliding groove 62 is disposed on a surface of the fixed plate 61, a second sliding groove 65 is disposed on a surface of the rotating plate 64, the second connecting pipe 53 slides in the second sliding groove 65, the second connecting pipe 53 penetrates through the first sliding groove 62 and slides in the first sliding groove 62, a driving component is disposed in the heat exchange housing 11, the driving component drives the rotating plate 64 to rotate, and the second connecting pipe 53 moves toward the center or away from the center along the first sliding groove 62 and the second sliding groove 65.
It should be noted that, in this embodiment, the driving assembly includes a driving member 66 and a driving motor 67, the output end of the driving motor 67 is connected to the driving member 66, the driving member 66 is a gear member, the driving member 66 is driven by the driving motor 67 to rotate, so as to drive the rotating plate member 64 to rotate, and the second connecting pipe 53 is driven to move along the first chute member 62 and the second chute member 65 by the rotation of the rotating plate member 64, and it should be further noted that, in this embodiment, the form as shown in fig. 5 and fig. 6 is adopted, but in practical use, the form as shown in fig. 5 may be set as a rotating part, the form as shown in fig. 6 is set as a fixed part, and the driving member 66 and the corresponding tooth part are moved into the form as shown in fig. 5, in this embodiment, the form of the first chute member 62 and the second chute member 65 does not make much requirement, and the two grooves are matched to make the second connecting pipe 53 slide inwards or outwards, and in this embodiment, the first chute member 62 is a curved groove, and the second chute member 65 is a straight groove, and the distance between the second connecting pipe 53 can be adjusted to a certain extent.
In fact, the second partition member 3 may be selected to be a two-plate combination, so that the two second partition members 3 and the rotating plate member 64 are dynamically sealed.
It should be noted that, in this embodiment, the second connecting pipe 53 is adjusted to a certain degree, so that the connecting pipes can be integrally gathered or dispersed to a certain degree, and the heat exchange of the accumulated liquid can be performed by selecting a part of the connecting pipes at the bottom through the dispersion and the gathering; in this embodiment, the driving motor 67 may be a waterproof type sealed motor, and the heat exchanger in this embodiment is mostly used for heat dissipation.
Example 3
On the basis of the foregoing embodiments 1 and 2, as shown in fig. 1 to 9, a corrugated tube heat exchanger with a heat transfer enhancement effect includes a heat exchange housing 11, the heat exchange housing 11 is connected to an outer support 1, a first liquid inlet 12, a first liquid outlet 13, a second liquid inlet 14 and a second liquid outlet 15 are connected to a surface of the heat exchange housing 11, the first liquid inlet 12 and the first liquid outlet 13 are communicated with each other, a liquid a is input into the first liquid inlet 12, the second liquid inlet 14 and the second liquid outlet 15 are communicated with each other, a liquid B is input into the second liquid inlet 14, two groups of first partition plate members 2 are disposed inside the heat exchange housing 11, a connecting pipe is disposed between the two groups of first partition plate members 2, a metering member 4 and a heat exchange member 5 are further disposed inside the two groups of first partition plate members 2, the volume of the A liquid in the first partition plate piece 2 is gathered to the measurement piece 4, heat exchange assembly 5 includes feed liquor valve 51 and goes out liquid valve 55, feed liquor valve 51 is connected respectively in the both ends of connecting pipe with going out liquid valve 55, just feed liquor valve 51 is connected with corresponding first partition plate piece 2 respectively with going out liquid valve 55, first inlet 12 sets up between two sets of first partition plate pieces 2 with first liquid outlet 13, second inlet 14 sets up outside two sets of first partition plate pieces 2 with second liquid outlet 15, heat exchange assembly 5 is based on the A liquid volume between two sets of first partition plate pieces 2, and the feed liquor valve 51 of control corresponding height opens and close with going out liquid valve 55, makes B liquid get into to carrying out the heat transfer in the connecting pipe in the A liquid volume.
Further, the housing is connected with a control module, the control module controls and connects the metering member 4, the liquid inlet valve 51 and the liquid outlet valve 55, and controls the liquid inlet and outlet amounts of the first liquid inlet 12, the first liquid outlet 13, the second liquid inlet 14 and the second liquid outlet 15.
It should be noted that the control module may be configured by a processor (C6 a816X processor) with a DSP or an ARM architecture, a memory cell, a memory disc, and a controller single chip microcomputer (AT 89C51 single chip microcomputer), and is disposed outside the housing.
Further, the first liquid inlet 12 is arranged at the upper part of the heat exchange shell 11, the first liquid outlet 13 is arranged at the lower part of the heat exchange shell 11, a second partition plate 3 is arranged below the liquid outlet end of the first liquid inlet 12, the side section of the second partition plate 3 is arc-shaped, the second partition plate 3 is positioned above all the connecting pipes, and the liquid a output by the first liquid inlet 12 is guided to the bottom by the second partition plate 3 and spreads upwards from the bottom; the second liquid outlet 15 is disposed outside the heat exchange housing 11 and near the bottom.
Further, the two groups of first partition plate members 2 are sequentially divided into a first area 21, an adjusting area 22 and a second area 23, an adjusting plate member 6 is disposed at the head end and the tail end of the adjusting area 22, a connecting pipe in the first area 21 is a first connecting pipe 52, a connecting pipe in the adjusting area 22 is a second connecting pipe 53, a connecting pipe in the second area 23 is a third connecting pipe 54, the first connecting pipe 52 and the third connecting pipe 54 are hoses, the second connecting pipe 53 is a hard pipe, and the adjusting plate member 6 adjusts the distance between the second connecting pipes 53.
Wherein, the second connecting pipe 53 is divided into an adjustable connecting pipe and a fixed core pipe 63, the adjustable connecting pipe is arranged around the fixed core pipe 63, and the adjusting plate 6 adjusts the distance between the adjustable connecting pipe and the fixed core pipe 63.
In this embodiment, the adjustable connecting pipe is the multilayer and encircles the formula and distributes, and the multilayer mode is convenient for adjust the multilayer and is located the adjustable connecting pipe of bottom, and it is still required to explain, adjusts plate 6 in the accommodation process of reality, needs to ensure to adjust controllable to the actual position of each connecting pipe of better understanding is convenient for based on actual position and actual A liquid volume, selects corresponding connecting pipe to use.
Further, in this embodiment, the adjusting plate 6 has a structure that the adjusting plate 6 includes a fixed plate 61 and a rotating plate 64, a first sliding groove 62 is disposed on a surface of the fixed plate 61, a second sliding groove 65 is disposed on a surface of the rotating plate 64, the second connecting pipe 53 slides in the second sliding groove 65, the second connecting pipe 53 penetrates through the first sliding groove 62 and slides in the first sliding groove 62, a driving component is disposed in the heat exchange housing 11, the driving component drives the rotating plate 64 to rotate, and the second connecting pipe 53 moves toward the center or away from the center along the first sliding groove 62 and the second sliding groove 65.
It should be noted that, in this embodiment, the driving assembly includes a driving member 66 and a driving motor 67, the output end of the driving motor 67 is connected with the driving member 66, the driving member 66 is a gear member, the driving member 66 is driven by the driving motor 67 to rotate, so as to drive the rotating plate member 64 to rotate, and the second connecting pipe 53 is driven to move along the first chute member 62 and the second chute member 65 by the rotation of the rotating plate member 64.
Further, heat exchange housing 11's inside is provided with adjusts inner tube 7, first inlet 12 and first liquid outlet 13 all insert in adjusting inner tube 7, it includes a plurality of hard plate 71 and the soft plate 72 of a plurality of groups to adjust inner tube 7, hard plate 71 with soft plate 72 interval sets up, and the two encircles the setting, is the tubular structure, adjust inner tube 7 still includes adjusting part, adjusting part adjusts hard plate 71 or/and soft plate 72 and is close to or keeps away from to the tubulose center.
Preferably, and optionally, the inner tube 7 is also adapted to be connected in a multi-stage manner in a dynamic seal with the rotating plate member 64.
Specifically, the adjusting assembly comprises a pulling piece 73 and a telescopic rod piece 74, the telescopic end of the telescopic rod piece 74 is fixedly connected with the outer surface of the hard plate 71, and the pulling end of the pulling piece 73 is connected with the outer center of the soft plate 72.
As shown in fig. 8 and fig. 9, the pulling element 73 is a combination of a rotating wheel, a pulling rope and a winding device, and the winding device winds and unwinds the pulling rope, so that the soft plate 72 can be loosened and diffused, and the telescopic rod 74 is an electrically controlled telescopic component, and is controlled by the control module; generally, some clamping members 75 can be additionally arranged at the edge of the soft plate 72 for matching, the clamping members 75 adopt electrically controlled or passive telescopic assemblies, the moving ends of the clamping members are connected with large rotating wheels, the soft plate 72 is extruded into a shape like a Chinese character 'ji' through the large rotating wheels, and the volume space in the whole adjusting inner tube 7 is determined based on the height of the vertical part of the shape like the Chinese character 'ji'.
In this embodiment, the space in the adjusting inner tube 7 is increased or decreased by adjusting the hard plate 71 and the soft plate 72, so that the density of the adjusting connecting tubes can be controlled by the adjusting inner tube 7 under full load based on the volume of the liquid a, thereby improving the corresponding heat exchange efficiency; typically, a support base 16 may be added to support and connect the lowest rigid plate 71, and preferably, the rigid plate 71 has an arc-shaped structure.
The above-mentioned embodiments only express several embodiments of the present invention, and the description thereof is more specific and detailed, but not construed as limiting the scope of the present invention. It should be noted that, for a person skilled in the art, several variations and modifications can be made without departing from the inventive concept, which falls within the scope of the present invention.
Claims (10)
1. The utility model provides a bellows heat exchanger with effect is reinforceed in heat transfer which characterized in that, this casing includes heat transfer shell, heat transfer shell connects on outer support piece, heat transfer shell's surface is connected with first inlet, first liquid outlet, second inlet and second liquid outlet, first inlet and first liquid outlet intercommunication each other, and first inlet input A liquid, second inlet and second liquid outlet intercommunication each other, and second inlet input B liquid, heat transfer shell's inside is provided with two sets of first baffle spare, and is two sets of be provided with the connecting pipe between the first baffle spare, and is two sets of still be provided with measurement piece and heat transfer assembly in the first baffle spare, the measurement piece gathers two sets of the volume of A liquid in the first baffle spare, heat transfer assembly includes feed liquor valve and liquid outlet valve, feed liquor valve and liquid outlet valve are connected respectively in the both ends of connecting pipe, just feed liquor valve and liquid outlet valve are connected with corresponding first baffle spare respectively, first inlet and first liquid outlet set up between first baffle spare, second inlet and second baffle spare set up outside the first baffle spare, liquid outlet valve and liquid outlet valve are based on the volume of the corresponding first baffle spare between A liquid inlet and liquid outlet valve carry out the corresponding liquid volume of a, make liquid volume of liquid and liquid inlet and liquid inlet connect the corresponding liquid inlet of two sets of liquid outlet valve, and make the corresponding liquid inlet and liquid inlet of liquid inlet and liquid in the corresponding liquid inlet of liquid inlet.
2. The corrugated tube heat exchanger with heat transfer enhancement effect as claimed in claim 1, wherein: the shell is connected with a control module, the control module controls and connects the metering piece, the liquid inlet valve and the liquid outlet valve, and the liquid inlet and outlet amounts of the first liquid inlet, the first liquid outlet, the second liquid inlet and the second liquid outlet can be controlled.
3. A bellows heat exchanger with heat transfer enhancement effect according to claim 2, wherein: the first liquid inlet is arranged on the upper portion of the heat exchange shell, the first liquid outlet is arranged on the lower portion of the heat exchange shell, a second partition plate is arranged below the liquid outlet end of the first liquid inlet, the side cross section of the second partition plate is arc-shaped, the second partition plate is located above all connecting pipes, and A liquid output by the first liquid inlet is guided to the bottom by the second partition plate and is stretched upwards by the bottom.
4. A bellows heat exchanger with heat transfer enhancement effect according to claim 3, wherein: the second liquid outlet is arranged on the outer side of the heat exchange shell and is close to the bottom.
5. The bellows heat exchanger with the heat transfer enhancement effect according to claim 4, wherein: the first partition plate pieces are divided into a first area, an adjusting area and a second area in sequence, the adjusting plate pieces are arranged at the head end and the tail end of the adjusting area, the connecting pipe in the first area is a first connecting pipe, the connecting pipe in the adjusting area is a second connecting pipe, the connecting pipe in the second area is a third connecting pipe, the first connecting pipe and the third connecting pipe are hoses, the second connecting pipe is a hard pipe, and the adjusting plate pieces adjust the distance between the second connecting pipes.
6. The corrugated tube heat exchanger with the heat transfer enhancement effect as claimed in claim 5, wherein: the second connecting pipe divide into adjustable connecting pipe and fixed core tube spare, the adjustable connecting pipe encircles fixed core tube spare setting, adjust the plate and adjust the distance between adjustable connecting pipe and the fixed core tube spare.
7. The corrugated tube heat exchanger with the heat transfer enhancement effect as claimed in claim 6, wherein: the adjustable connecting pipes are distributed in a multi-layer surrounding mode.
8. The corrugated tube heat exchanger with the heat transfer enhancement effect as claimed in claim 7, wherein: the adjusting plate comprises a fixing plate and a rotating plate, a first sliding groove piece is arranged on the surface of the fixing plate, a second sliding groove piece is arranged on the surface of the rotating plate, a second connecting pipe slides in the second sliding groove piece, the second connecting pipe penetrates out of the first sliding groove piece and slides in the first sliding groove piece, a driving assembly is arranged in the heat exchange shell and drives the rotating plate to rotate, and the second connecting pipe moves towards the center or moves away from the center along the first sliding groove piece and the second sliding groove piece.
9. The bellows heat exchanger with the heat transfer enhancement effect according to claim 8, wherein: the inside of heat transfer housing is provided with adjusts the inner tube, first inlet and first liquid outlet all insert in adjusting the inner tube, it includes a plurality of hard plates of group and the soft plate of a plurality of groups to adjust the inner tube, hard plate with soft plate interval sets up, and the two encircles the setting, is the tubular structure, it still includes adjusting part to adjust the inner tube, adjusting part adjusts hard plate or/and soft plate and is close to or keeps away from to the tubulose center.
10. A bellows heat exchanger with heat transfer enhancement effect according to claim 9, wherein: the adjusting part pulls and draws piece and flexible member including drawing, the flexible end of flexible member is connected with the surface fixed of stereoplasm plate, draw pulling of pulling to draw the end and be connected with the outside center of soft plate.
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