CN219849552U - Double-tank self-heat-exchange biological reaction kettle system - Google Patents
Double-tank self-heat-exchange biological reaction kettle system Download PDFInfo
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- CN219849552U CN219849552U CN202321295182.0U CN202321295182U CN219849552U CN 219849552 U CN219849552 U CN 219849552U CN 202321295182 U CN202321295182 U CN 202321295182U CN 219849552 U CN219849552 U CN 219849552U
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- reaction kettle
- biological reaction
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 61
- 238000012423 maintenance Methods 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000012530 fluid Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 5
- 239000000126 substance Substances 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- 239000003595 mist Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000005686 electrostatic field Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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Abstract
The utility model provides a double-tank self-heat-exchange biological reaction kettle system which comprises a first biological reaction kettle and a second biological reaction kettle, wherein an outlet of the first biological reaction kettle is communicated with an inlet of the second biological reaction kettle through a first circulating pipeline, and an inlet of the first biological reaction kettle is communicated with an outlet of the second biological reaction kettle through a second circulating pipeline. The double-tank self-heat-exchange biological reaction kettle system has the advantages of simple pipeline structure and low maintenance cost, and the fluids in the two biological reaction kettles can exchange heat with each other, so that the energy consumption is reduced, and the environment is protected.
Description
Technical Field
The utility model relates to the technical field of energy conservation and environmental protection, in particular to a double-tank self-heat-exchange biological reaction kettle system.
Background
The biological reaction kettle is a container for carrying out chemical or physical reaction, and the functions of heating, cooling, mixing and the like required by chemical or biological technology are realized through the reaction kettle.
The application of the biological reaction kettle is wider, the biological reaction kettle is used for realizing specific technological requirements in the technical processes of petroleum, chemical industry, biology, medicine, food processing and the like, and in the prior art, the biological reaction kettle is often required to be externally connected with a plurality of pipelines for meeting the requirements of feeding and discharging, mixing and heat exchange, and the biological reaction kettle has the advantages of complex pipelines, huge maintenance cost and poor heat exchange effect.
In view of this, the present utility model has been made.
Disclosure of Invention
The utility model aims to provide a double-tank self-heat-exchange biological reaction kettle system, which has the advantages of simple pipeline structure, low maintenance cost and good heat exchange effect.
In order to solve the technical problems, the utility model provides a double-tank self-heat-exchange biological reaction kettle system, which comprises a first biological reaction kettle and a second biological reaction kettle, wherein an outlet of the first biological reaction kettle is communicated with an inlet of the second biological reaction kettle through a first circulating pipeline, and an inlet of the first biological reaction kettle is communicated with an outlet of the second biological reaction kettle through a second circulating pipeline.
Further, the outlets of the first biological reaction kettle and the second biological reaction kettle are respectively provided with a demisting device.
Further, the demisting device comprises a primary demister and a secondary demister, wherein the primary demister and the secondary demister are respectively located below and above an outlet of the reaction kettle, and the primary demister and the secondary demister are electrically connected.
Further, spiral heat exchange pipelines are arranged in the first biological reaction kettle and the second biological reaction kettle, and the outer walls of the spiral heat exchange pipelines are connected with the inner wall of the reaction kettle through ribs respectively.
Further, the first circulating pipeline and the second circulating pipeline are respectively provided with a flow rate and flow velocity controller.
Further, the first circulating pipeline and the second circulating pipeline are respectively provided with a circulating valve and a circulating pump.
Compared with the prior art, the utility model has the beneficial effects that:
1. the double-tank self-heat-exchange biological reaction kettle system has the advantages that the pipeline structure is simple, the overhaul cost is low, and the fluids in the two biological reaction kettles can exchange heat with each other, so that the energy consumption is reduced, and the environment is protected;
2. according to the double-tank self-heat-exchange biological reaction kettle system, the demisting device is arranged at the outlet of the reaction kettle, so that fog and peculiar smell can be eliminated;
3. the double-tank self-heat-exchange biological reaction kettle system can further strengthen the heat exchange effect and utilize waste heat by arranging the spiral heat exchange pipeline in the reaction kettle.
Drawings
In order to more clearly illustrate the embodiments of the present utility model or the technical solutions in the prior art, the drawings that are needed in the description of the embodiments or the prior art will be briefly described, and it is obvious that the drawings in the description below are some embodiments of the present utility model, and other drawings can be obtained according to the drawings without inventive effort for a person skilled in the art.
FIG. 1 is a schematic diagram of the overall structure of a double-tank self-heat-exchanging bioreactor system according to the present utility model;
FIG. 2 is a schematic view of the structure of the fin according to the present utility model;
FIG. 3 is a schematic view of a demister according to the present utility model;
FIG. 4 is a longitudinal sectional view of the double-tank self-heat-exchanging bioreactor system provided by the utility model.
Reference numerals illustrate:
1-a first biological reaction kettle; 2-a second biological reaction kettle;
11-a first circulation line; 12-a second circulation line;
3-defogging; 31-a primary demister;
a 32-secondary mist eliminator; 4-spiral heat exchange pipeline;
5-ribs; 6-a flow rate and flow velocity controller;
7-a circulation valve; 8-a circulating pump.
Detailed Description
The technical solutions of the present utility model will be clearly and completely described in connection with the embodiments, and it is apparent that the described embodiments are some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
In the description of the present utility model, it should be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", etc. indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings are merely for convenience in describing the present utility model and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, be configured and operated in a specific orientation, and thus should not be construed as limiting the present utility model.
Furthermore, the terms "first," "second," and the like, are used for descriptive purposes only and are not to be construed as indicating or implying a relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defining "a first" or "a second" may explicitly or implicitly include one or more of the described features. In the description of the present utility model, the meaning of "a plurality" is two or more, unless explicitly defined otherwise. Furthermore, the terms "mounted," "connected," "coupled," 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 will be understood in specific cases by those of ordinary skill in the art.
Referring to fig. 1-4, a double-tank self-heat-exchanging bioreactor system provided by the utility model comprises a first bioreactor 1 and a second bioreactor 2, wherein an outlet of the first bioreactor 1 is communicated with an inlet of the second bioreactor through a first circulating pipeline 11, and an inlet of the first bioreactor 1 is communicated with an outlet of the second bioreactor 2 through a second circulating pipeline 12. The double-tank self-heat-exchange biological reaction kettle system pipeline has the advantages of simple structure and low maintenance cost, and the fluids in the first biological reaction kettle 1 and the second biological reaction kettle 2 can exchange heat with each other through the circulating pipeline, so that the energy consumption is reduced, and the environment is protected.
In this embodiment, the exit of first biological reation kettle 1 and second biological reation kettle 2 all is provided with defogging device 3, can eliminate fog and peculiar smell through setting up defogging device 3. Specifically, defogging is adorned 3 and is included one-level defroster 31 and second grade defroster 32, and one-level defroster 31 is located the below of reation kettle export, and second grade defroster 32 is located the top of reation kettle export, is connected through the electricity between one-level defroster 31 and the second grade defroster 32. An electrostatic field is formed through an external power supply, and water mist entering the demister is adsorbed and recovered through an electric effect.
In addition, all be provided with heliciform heat transfer pipeline 4 in the inside of first biological reation kettle 1 and second biological reation kettle 2, the outer wall of heliciform heat transfer pipeline 4 is connected through fin 5 and reation kettle's inner wall respectively, sets up like this and can further strengthen the heat transfer effect, carries out waste heat utilization.
On the basis of the scheme, the first circulating pipeline 11 and the second circulating pipeline 12 are respectively provided with a flow rate and flow velocity controller 6, a circulating valve 7 and a circulating pump 8.
Finally, it should be noted that: the above embodiments are only for illustrating the technical solution of the present utility model, and not for limiting the same; although the utility model has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical scheme described in the foregoing embodiments can be modified or some or all of the technical features thereof can be replaced by equivalents; such modifications and substitutions do not depart from the spirit of the utility model.
Claims (6)
1. The double-tank self-heat-exchange biological reaction kettle system is characterized by comprising a first biological reaction kettle and a second biological reaction kettle, wherein an outlet of the first biological reaction kettle is communicated with an inlet of the second biological reaction kettle through a first circulating pipeline, and an inlet of the first biological reaction kettle is communicated with an outlet of the second biological reaction kettle through a second circulating pipeline.
2. The double-tank self-heat-exchange biological reaction kettle system according to claim 1, wherein demisting devices are arranged at the outlets of the first biological reaction kettle and the second biological reaction kettle.
3. The double-tank self-heat-exchange biological reaction kettle system according to claim 2, wherein the demisting device comprises a primary demister and a secondary demister, the primary demister and the secondary demister are respectively located above and below an outlet of the reaction kettle, and the primary demister and the secondary demister are electrically connected.
4. The double-tank self-heat-exchange biological reaction kettle system according to claim 1, wherein spiral heat exchange pipelines are arranged in the first biological reaction kettle and the second biological reaction kettle, and the outer walls of the spiral heat exchange pipelines are connected with the inner wall of the reaction kettle through ribs respectively.
5. The double-tank self-heat-exchanging bioreactor system as set forth in claim 1, wherein the first circulation pipe and the second circulation pipe are provided with flow rate controllers.
6. The double-tank self-heat-exchange biological reaction kettle system according to claim 1, wherein a circulation valve and a circulation pump are arranged on the first circulation pipeline and the second circulation pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321295182.0U CN219849552U (en) | 2023-05-26 | 2023-05-26 | Double-tank self-heat-exchange biological reaction kettle system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321295182.0U CN219849552U (en) | 2023-05-26 | 2023-05-26 | Double-tank self-heat-exchange biological reaction kettle system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219849552U true CN219849552U (en) | 2023-10-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321295182.0U Active CN219849552U (en) | 2023-05-26 | 2023-05-26 | Double-tank self-heat-exchange biological reaction kettle system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219849552U (en) |
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2023
- 2023-05-26 CN CN202321295182.0U patent/CN219849552U/en active Active
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