CN219714114U - Kitchen organic slurry spiral plate type heat exchange device - Google Patents
Kitchen organic slurry spiral plate type heat exchange device Download PDFInfo
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- CN219714114U CN219714114U CN202320209021.9U CN202320209021U CN219714114U CN 219714114 U CN219714114 U CN 219714114U CN 202320209021 U CN202320209021 U CN 202320209021U CN 219714114 U CN219714114 U CN 219714114U
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- heat exchange
- fixedly arranged
- barrel
- kitchen organic
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- 239000002002 slurry Substances 0.000 title claims abstract description 23
- 239000012530 fluid Substances 0.000 claims abstract description 49
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 30
- 239000010959 steel Substances 0.000 claims abstract description 30
- 238000007789 sealing Methods 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 5
- 238000005096 rolling process Methods 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 8
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 238000009434 installation Methods 0.000 description 5
- 239000000126 substance Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 230000002708 enhancing effect Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000012824 chemical production Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model relates to the technical field of mechanical devices, in particular to a kitchen organic slurry spiral plate type heat exchange device which comprises a cylinder body, wherein two connecting pipes are fixedly arranged on the front surface of the cylinder body, a cold fluid inlet and a hot fluid outlet are fixedly arranged on the front surfaces of the two connecting pipes respectively, the two connecting pipes are communicated with the inside of the cylinder body, mounting strips are fixedly arranged on the front side and the rear side of the inside of the cylinder body, two steel plates are arranged on the cylinder body through the two mounting strips, the two steel plates are parallel to each other and are in spiral coil shapes, a top plate and a bottom plate are fixedly arranged on the top and the bottom of the cylinder body respectively, the top ends and the bottom ends of the two steel plates are fixedly connected with the bottom surface of the top plate and the top surface of the bottom plate respectively, and a fixing plate is fixedly arranged on one side of the inside of the two steel plates. The utility model has good heat exchange effect, can effectively avoid the phenomenon of blockage of the heat exchanger, can be used in combination with multiple units, and meets the production requirement.
Description
Technical Field
The utility model relates to the technical field of mechanical devices, in particular to a spiral plate type heat exchange device for kitchen organic slurry.
Background
The heat exchanger is an indispensable device for realizing heat exchange and transfer in the chemical production process. The heat exchanger has important roles in chemical industry, petroleum, power, food and other industrial production, and can be used as a heater, a cooler, a condenser, an evaporator, a reboiler and the like in chemical industry, and the application is wide. There are often materials in the heat exchange that are very corrosive and oxidizing, and therefore, materials for making up the heat exchanger are required to have strong corrosion resistance.
At present, most heat exchange devices are parallel plate heat exchangers and tubular heat exchangers, and the heat exchange device is characterized by being mainly used for the liquid with high purity, and has remarkable heat exchange effect, larger heat exchange area by using the same material and wide application in industrial heat exchange systems. But the disadvantages are more obvious:
(1) The sealing periphery of the parallel plate heat exchanger is long, and the rubber sealing element is easy to oxidize and damage, so that leakage is caused;
(2) However, for heat exchange liquid containing a large amount of impurities (such as suspended particle impurities of silt, small shells and the like), the phenomenon that the parallel plate type heat exchanger and the tubular heat exchanger are easy to be blocked is caused, the heat exchange liquid is difficult to clean, the heat exchange efficiency is greatly reduced, and the normal and stable operation is influenced;
(3) The kitchen organic slurry has low applicability, and when the kitchen organic slurry is heated, the slurry contains more solid substances, so that the blocking condition can be easily caused.
Therefore, in order to solve the problems, the spiral plate type heat exchange device for kitchen organic slurry is improved.
Disclosure of Invention
In order to solve the technical problems, the utility model provides the following technical scheme:
the utility model provides a technical scheme that: the utility model provides a kitchen organic thick liquid spiral plate heat transfer device, includes the barrel, the front fixed mounting of barrel has two takeovers, two the front of takeovers respectively fixed mounting have cold fluid entry and hot fluid export, two the takeovers all with the inside intercommunication of barrel, the inside front and back both sides of barrel all fixed mounting has the installation strip, the barrel passes through two steel sheets are installed to the installation strip, two the steel sheets are parallel to each other and are the spiral form of rolling up, the top and the bottom of barrel respectively fixed mounting have roof and bottom plate, two the top and the bottom of steel sheet respectively with the bottom surface of roof with the top surface welded connection of bottom plate, two the inside one side fixed mounting of steel sheet has the fixed plate.
As a preferable technical scheme of the utility model, the bottom surface of the top plate and the top surface of the bottom plate are fixedly provided with sealing gaskets, the top and the bottom of the cylinder body are respectively provided with a convex edge, and one side of each convex edge, which is far away from the two steel plates, is fixedly provided with a sealing ring.
As a preferable technical scheme of the utility model, a cold fluid outlet is fixedly arranged at the middle position of the top plate, and a hot fluid inlet is fixedly arranged at the middle position of the bottom plate.
As a preferable technical scheme of the utility model, the left side and the right side of the cylinder are fixedly provided with the fixing frames, and one side of each fixing frame is fixedly provided with the supporting leg.
As a preferable technical scheme of the utility model, the upper part of the right side and the lower part of the left side of the fixed plate are fixedly provided with the plugging plates, and the two plugging plates are of semicircular structures.
As a preferable technical scheme of the utility model, the top ends of the two mounting bars are fixedly connected with the bottom of the top plate, and the bottom ends of the two mounting bars are fixedly connected with the top of the bottom plate.
The beneficial effects of the utility model are as follows:
1. after cold fluid and hot fluid are input into the device, the cold fluid and the hot fluid can flow in full countercurrent, so that the heat exchange effect is greatly enhanced, and the ideal heat exchange effect can be achieved even if two small temperature difference media are used.
2. The two even spiral channels formed between the two steel plates have the characteristic of no dead angle, so that solid matters cannot be deposited in the channels to be blocked when the kitchen organic slurry flows, thereby effectively exchanging heat to the kitchen organic slurry, effectively recovering waste heat through the two arranged spiral coiled steel plates, and fully utilizing low-temperature heat energy.
3. When a single device can not meet the use requirement, a plurality of devices can be combined for use, and the production requirement is met.
Drawings
The accompanying drawings are included to provide a further understanding of the utility model and are incorporated in and constitute a part of this specification, illustrate the utility model and together with the embodiments of the utility model, serve to explain the utility model. In the drawings:
FIG. 1 is a schematic diagram of the overall structure of a spiral plate type heat exchange device for kitchen organic slurry;
FIG. 2 is a schematic view of the structure of the spiral plate heat exchanger for kitchen organic slurry shown in FIG. 1 at A-A;
FIG. 3 is an enlarged schematic view of the structure of the spiral plate heat exchanger for kitchen organic slurry of the present utility model at B in FIG. 1;
in the figure: 1. a cylinder; 2. a fixing frame; 3. support legs; 4. a cold fluid inlet; 5. a hot fluid inlet; 6. a bottom plate; 7. a hot fluid outlet; 8. connecting pipe; 9. a top plate; 10. a cold fluid outlet; 11. a mounting bar; 12. a steel plate; 13. a sealing gasket; 14. a plugging plate; 15. a fixing plate; 16. a convex edge; 17. and (3) sealing rings.
Detailed Description
The preferred embodiments of the present utility model will be described below with reference to the accompanying drawings, it being understood that the preferred embodiments described herein are for illustration and explanation of the present utility model only, and are not intended to limit the present utility model.
Referring to fig. 1-3, the present utility model provides a technical solution: the technical scheme of the kitchen organic slurry spiral plate type heat exchange device comprises a barrel 1, two connecting pipes 8 are fixedly arranged on the front surface of the barrel 1, a cold fluid inlet 4 and a hot fluid outlet 7 are fixedly arranged on the front surface of each connecting pipe 8, the two connecting pipes 8 are communicated with the inside of the barrel 1, mounting strips 11 are fixedly arranged on the front side and the rear side of the inside of the barrel 1, two steel plates 12 are arranged on the barrel 1 through the two mounting strips 11, the two steel plates 12 are parallel to each other and are spiral coiled, and because the two steel plates 12 are parallel to each other and are spiral coiled, two uniform spiral channels are formed between the two steel plates 12, and the two circulating flows can flow in the two spiral channels and exchange heat respectively, and the spiral coiled steel plates 12 can effectively perform waste heat recovery, so that low-temperature heat energy can be fully utilized.
The top and the bottom of barrel 1 are fixed mounting respectively has roof 9 and bottom plate 6, and the top and the bottom of two steel sheets 12 are connected with the bottom surface of roof 9 and the top surface welding of bottom plate 6 respectively, and the steel sheet 12 can improve the leakproofness between two spiral channels with roof 9 and bottom plate 6 welding, guarantees that two media do not mix, and one side fixed mounting has fixed plate 15 inside two steel sheets 12.
The bottom surface of roof 9 and the top surface of bottom plate 6 all fixed mounting have sealed pad 13, and barrel 1 top and bottom all are provided with chimb 16, and two chimb 16 are kept away from two steel sheet 12 one side all fixed mounting have sealing washer 17, through chimb 16, sealing washer 17 and the sealed pad 13 that set up, can increase the leakproofness between roof 9, bottom plate 6 and the barrel 1.
A cold fluid outlet 10 is fixedly arranged at the middle position of the top plate 9, a hot fluid inlet 5 is fixedly arranged at the middle position of the bottom plate 6, and when the cold fluid inlet 4 is arranged at the rear end of the hot fluid outlet 7, the cold fluid inlet is tangential to the outer side of the cylinder 1, so that the tangential structure can effectively reduce local resistance;
and because the hot fluid inlet 5 is positioned at the bottom of the cylinder 1, the hot fluid outlet 7 is positioned at the front of the cylinder 1, so that the hot fluid flows from the inside of the spiral channel to the outside, and the cold fluid inlet 4 is positioned at the front of the cylinder 1, and the cold fluid outlet 10 is positioned at the top of the cylinder 1, so that the cold fluid flows from the outside of the spiral channel to the inside, thereby enabling the cold fluid and the hot fluid to flow in full countercurrent, greatly enhancing the heat exchange effect, and achieving the ideal heat exchange effect even for two small-temperature difference media.
The left and right sides of barrel 1 all fixed mounting has mount 2, and the equal fixed mounting of one side of two mounts 2 has supporting leg 3, and supporting leg 3 and mount 2 can support barrel 1 for barrel 1 keeps unsettled, is convenient for with the inside of thermal fluid input barrel 1 from thermal fluid entry 5.
The upper part on the right side and the lower part on the left side of the fixed plate 15 are fixedly provided with the plugging plates 14, the two plugging plates 14 are of semicircular structures, and the plugging plates 14 and the fixed plate 15 can avoid the mutual contact and mixing of the circulation inside the two spiral channels.
The top of two installation bars 11 all with the bottom fixed connection of roof 9, the bottom of two installation bars 11 all with the top fixed connection of bottom plate 6, installation bar 11 can seal between steel sheet 12 and the barrel 1 inboard.
Working principle: before use, the device is checked to be placed at a proper position, then cold fluid is conveyed into the cylinder 1 through the cold fluid inlet 4, and the hot fluid is input into the cylinder 1 through the hot fluid inlet 5, and two uniform spiral channels are formed between the two steel plates 12 because the two steel plates 12 are parallel to each other and are in spiral coil shapes, and at the moment, the hot fluid and the cold fluid respectively flow in the two spiral channels and exchange heat.
Since the hot fluid inlet 5 is located at the bottom of the cylinder 1, the hot fluid outlet 7 is located at the front of the cylinder 1, so that the hot fluid will flow from the inside of the spiral channel to the outside, and the cold fluid inlet 4 is located at the front of the cylinder 1, and the cold fluid outlet 10 is located at the top of the cylinder 1, so that the cold fluid will flow from the outside of the spiral channel to the inside, thereby enabling the cold fluid and the hot fluid to flow in full countercurrent, greatly enhancing the heat exchange effect, and achieving the ideal heat exchange effect even for two small temperature difference media.
When the device is applied to a kitchen organic slurry heat exchange system, two uniform spiral channels are formed between two steel plates 12 of the device, and the spiral channels have the characteristic of no dead angle, so that solid substances contained in the kitchen organic slurry are not deposited in the channels to be blocked when the kitchen organic slurry flows, and heat exchange can be effectively carried out on the kitchen organic slurry.
When a single device cannot meet the use requirement, a plurality of devices can be combined for use, but the following needs to be ensured: parallel combination, series combination, equipment and channel spacing.
In the description of the present utility model, it should be noted that the azimuth or positional relationship indicated by the terms "vertical", "upper", "lower", "horizontal", etc. are based on the azimuth or positional relationship shown in the drawings, and are merely for convenience of describing the present utility model and simplifying the description, and do not indicate or imply that the apparatus or element referred to must have a specific azimuth, be constructed and operated in a specific azimuth, and thus should not be construed as limiting the present utility model.
In the description of the present utility model, it should also be noted that, unless explicitly specified and limited otherwise, the terms "disposed," "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; can be directly connected or indirectly connected through an intermediate medium, and can be communication between two elements. The specific meaning of the above terms in the present utility model can be understood by those of ordinary skill in the art according to the specific circumstances.
Finally, it should be noted that: the foregoing description is only a preferred embodiment of the present utility model, and the present utility model is not limited thereto, but it is to be understood that modifications and equivalents of some of the technical features described in the foregoing embodiments may be made by those skilled in the art, although the present utility model has been described in detail with reference to the foregoing embodiments. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present utility model should be included in the protection scope of the present utility model.
Claims (6)
1. The utility model provides a kitchen organic thick liquid spiral plate heat transfer device, includes barrel (1), its characterized in that, the front fixed mounting of barrel (1) has two takeover (8), two the front of takeover (8) respectively fixed mounting have cold fluid entry (4) and hot fluid export (7), two takeover (8) all with the inside intercommunication of barrel (1), the inside front and back both sides of barrel (1) all fixed mounting has mounting strip (11), barrel (1) are through two mounting strip (11) install two steel sheet (12), two steel sheet (12) are parallel to each other and are the spiral form of rolling up, the top and the bottom of barrel (1) respectively fixed mounting have roof (9) and bottom plate (6), two steel sheet (12) top and bottom respectively with the bottom of roof (9) with the top welded connection of bottom plate (6), two steel sheet (12) inside one side fixed mounting has fixed plate (15).
2. The kitchen organic slurry spiral plate type heat exchange device according to claim 1, wherein sealing gaskets (13) are fixedly installed on the bottom surface of the top plate (9) and the top surface of the bottom plate (6), convex edges (16) are arranged on the top and the bottom of the cylinder (1), and sealing rings (17) are fixedly installed on one sides, far away from the two steel plates (12), of the two convex edges (16).
3. A kitchen organic slurry spiral plate type heat exchange device according to claim 1, wherein a cold fluid outlet (10) is fixedly arranged at the middle position of the top plate (9), and a hot fluid inlet (5) is fixedly arranged at the middle position of the bottom plate (6).
4. The kitchen organic slurry spiral plate type heat exchange device according to claim 1, wherein fixing frames (2) are fixedly arranged on the left side and the right side of the cylinder body (1), and supporting legs (3) are fixedly arranged on one side of each fixing frame (2).
5. The kitchen organic slurry spiral plate type heat exchange device according to claim 1, wherein a plugging plate (14) is fixedly arranged above the right side and below the left side of the fixing plate (15), and the two plugging plates (14) are of semicircular structures.
6. The kitchen organic slurry spiral plate type heat exchange device according to claim 1, wherein the top ends of the two mounting bars (11) are fixedly connected with the bottom of the top plate (9), and the bottom ends of the two mounting bars (11) are fixedly connected with the top of the bottom plate (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320209021.9U CN219714114U (en) | 2023-02-01 | 2023-02-01 | Kitchen organic slurry spiral plate type heat exchange device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320209021.9U CN219714114U (en) | 2023-02-01 | 2023-02-01 | Kitchen organic slurry spiral plate type heat exchange device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219714114U true CN219714114U (en) | 2023-09-19 |
Family
ID=88014575
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320209021.9U Active CN219714114U (en) | 2023-02-01 | 2023-02-01 | Kitchen organic slurry spiral plate type heat exchange device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219714114U (en) |
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2023
- 2023-02-01 CN CN202320209021.9U patent/CN219714114U/en active Active
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