CN220919222U - Novel reactor with spray heat exchange function - Google Patents
Novel reactor with spray heat exchange function Download PDFInfo
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- CN220919222U CN220919222U CN202322752437.8U CN202322752437U CN220919222U CN 220919222 U CN220919222 U CN 220919222U CN 202322752437 U CN202322752437 U CN 202322752437U CN 220919222 U CN220919222 U CN 220919222U
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- heat exchange
- equipment body
- liquid
- novel reactor
- fixedly arranged
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- 239000007921 spray Substances 0.000 title claims abstract description 18
- 239000007788 liquid Substances 0.000 claims abstract description 38
- 239000007791 liquid phase Substances 0.000 claims abstract description 23
- 239000012071 phase Substances 0.000 claims abstract description 21
- 239000000945 filler Substances 0.000 claims abstract description 15
- 238000012856 packing Methods 0.000 claims description 7
- 238000012546 transfer Methods 0.000 claims description 7
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- 230000000149 penetrating effect Effects 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 abstract description 37
- 230000000694 effects Effects 0.000 abstract description 8
- 238000012824 chemical production Methods 0.000 abstract description 3
- 239000006260 foam Substances 0.000 abstract description 2
- 238000000034 method Methods 0.000 abstract description 2
- 239000000463 material Substances 0.000 description 22
- 239000007789 gas Substances 0.000 description 12
- 239000007792 gaseous phase Substances 0.000 description 5
- 230000008676 import Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
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- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model relates to the technical field of chemical production and discloses a novel reactor with spray heat exchange, which comprises an equipment body, wherein a gas phase outlet is fixedly formed in the upper end face of the equipment body, a foam remover is fixedly arranged on the upper part of the inner wall of the equipment body, a liquid phase inlet is formed in the upper part of one side of the equipment body, a pipeline penetrates into the equipment body and is fixedly provided with a liquid distributor, a filler is fixedly arranged in the middle of the inner wall of the equipment body, a first liquid collector is fixedly arranged on the lower end face of the filler, a liquid redistributor is fixedly arranged on the lower end face of the first liquid collector, and a gas phase inlet is formed in the lower part of the other side of the equipment body. According to the utility model, the heat exchange and the reaction are integrated, so that the problem of space occupation of equipment is effectively solved, the heat exchange effect is effectively increased, and the method has wide applicability and is easy to popularize.
Description
Technical Field
The utility model relates to the technical field of chemical production, in particular to a novel reactor with spray heat exchange.
Background
Chemical reactions refer to the process of converting raw materials into desired products by chemical reactions during chemical production. In chemical reactions, where one or more substances (reactants) undergo a series of chemical changes to form new compounds (products), the chemical reaction needs to meet certain reaction conditions, such as appropriate temperature, pressure and reaction time, and at the same time, catalyst may need to be added or reaction conditions may need to be adjusted to promote the reaction, and the chemical reaction is usually performed in a reaction vessel, which may be a closed reaction vessel, a reaction tower or a tubular reactor, etc.
The chemical reaction belongs to an endothermic reaction at the initial stage of the production process, and part of the chemical reaction belongs to an endothermic reaction and part of the chemical reaction belongs to an exothermic reaction in the reaction process, so that the problems of insufficient space, uneven equipment arrangement and the like can exist in the aspects of heat integration recovery, heat exchange equipment space arrangement and the like, and inconvenience is brought to production and overhaul.
Accordingly, one skilled in the art would provide a novel reactor with spray heat exchange to address the problems set forth in the background above.
Disclosure of utility model
The utility model aims to solve the defects in the prior art, and provides the novel reactor with the spray heat exchange, which integrates the heat exchange and the reaction, effectively solves the problem of occupied space of equipment, effectively increases the heat exchange effect, has wide applicability and is easy to popularize.
In order to achieve the above purpose, the present utility model provides the following technical solutions:
The novel reactor with the spraying heat exchange comprises an equipment body, wherein a gas phase outlet is fixedly formed in the upper end face of the equipment body, a foam remover is fixedly arranged at the upper part of the inner wall of the equipment body, a liquid phase inlet is formed in the upper part of one side of the equipment body, a pipeline penetrates into the equipment body and is fixedly provided with a liquid distributor, a filler is fixedly arranged in the middle of the inner wall of the equipment body, a first liquid collector is fixedly arranged on the lower end face of the filler, a liquid redistributor is fixedly arranged on the lower end face of the first liquid collector, a gas phase inlet is formed in the lower part of the other side of the equipment body, a pipeline is arranged at the gas phase inlet, a liquid phase outlet is formed in the lower side of the gas phase inlet, the pipeline penetrates into the equipment body and is fixedly provided with a heat exchange pipe, one end of the heat exchange pipe penetrates into the filler after penetrating into the equipment body, the second liquid collector is fixedly arranged at the lower part of the inner wall of the equipment body, and the pipeline penetrates into the liquid phase outlet is fixedly arranged on the lower end face of the second liquid collector;
Through above-mentioned technical scheme, this reactor is through having set up the filler, and the filler can be according to material component and characteristic selection corresponding filler and react, carries out the heat transfer in the bottom of equipment again, combines heat transfer and reaction an organic wholely, has effectively solved equipment occupation space problem, has effectively increased the heat transfer effect simultaneously, has extensive suitability, easily promotes.
Further, flanges are arranged at the positions of the liquid phase inlet, the liquid phase outlet, the gas phase inlet and the gas phase outlet;
Through above-mentioned technical scheme, through setting up the ring flange for the pipeline passes through the flange to be connected, and pipeline and flange select the type according to the standard, make to dismantle the convenience when overhauing.
Further, a check valve is fixedly arranged on the whole body of the heat exchange tube positioned outside the equipment body;
Through above-mentioned technical scheme, check valve aim at carries gaseous phase material, prevents liquid phase material refluence.
Further, the heat exchange tube is arranged in a sinuous coil shape;
Through above-mentioned technical scheme, through setting up the heat exchange tube that the sinuously winding made the heat transfer effect better.
Further, the heat exchange tube is a seamless steel tube;
Through the technical scheme, the materials are selected according to the material properties, the pressure, the temperature and the like, and the purpose is to convey gas-phase materials and exchange heat materials.
Further, the packing is disposed between the liquid distributor and the liquid redistributor;
Through the technical scheme, the liquid distributor and the liquid redistributor uniformly distribute the liquid phase materials, so that the reaction or heat exchange is more sufficient.
Further, the pipelines are all connected through flanges;
Through above-mentioned technical scheme, the pipeline all adopts flange joint, and pipeline and flange are according to standard selection, dismantle convenient when overhauling.
The utility model has the following beneficial effects:
The novel reactor with spray heat exchange, provided by the utility model, integrates heat exchange and reaction, the top of the equipment belongs to a reaction stage, corresponding materials and types of filling equipment are selected according to material properties, reaction pressure, temperature and the like in the reaction stage, the bottom of the equipment belongs to a heat exchange stage, and the heat exchange area is optimized according to the reaction condition (temperature) at the time and the reaction condition (temperature) at the next stage, so that the heat exchange effect is improved, the equipment occupation space problem is effectively solved, and the reactor has wide applicability and is easy to popularize.
Drawings
FIG. 1 is a schematic axial view of a novel reactor with spray heat exchange according to the present utility model;
FIG. 2 is a schematic illustration of a front cross-section of a novel reactor with spray heat exchange according to the present utility model;
fig. 3 is an enlarged view of a portion a of a novel reactor with spray heat exchange according to the present utility model.
Legend description:
1. A gas phase outlet; 2. a demister; 3. a liquid phase inlet; 4. a liquid distributor; 5. a filler; 6. a check valve; 7. a first liquid collector; 8. a liquid redistributor; 9. a heat exchange tube; 10. a second liquid collector; 11. a gas phase inlet; 12. a liquid phase outlet; 13. an apparatus body.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only 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.
Examples
Referring to fig. 1-3, one embodiment provided by the present utility model is: the novel reactor with spray heat exchange comprises a device body 13, wherein a gas phase outlet 1 is fixedly arranged on the upper end surface of the device body 13, a demister 2 is fixedly arranged on the upper part of the inner wall of the device body 13, liquid phase inlet 3 is arranged on the upper part of one side of the device body 13, a pipeline penetrates into the device body 13 and is fixedly provided with a liquid distributor 4, a filler 5 is fixedly arranged in the middle of the inner wall of the device body 13, the filler 5 has a wide application range, corresponding fillers 5 are selected according to the components and characteristics of the materials, the lower end surface of the filler 5 is fixedly provided with a first liquid collector 7, the first liquid collector 7 collects liquid phase materials, the lower end surface of the first liquid collector 7 is fixedly provided with a liquid redistributor 8 for facilitating liquid redistributing and conveying, the gas phase inlet 11 is arranged at the lower part of the other side of the equipment body 13, a pipeline is arranged at the gas phase inlet 11, a liquid phase outlet 12 is arranged at the lower side of the gas phase inlet 11 at one side of the equipment body 13, the pipeline penetrates through the inside of the equipment body 13 and is fixedly provided with a heat exchange tube 9, one end of the heat exchange tube 9 penetrates through the outside of the equipment body 13 to the outside of the equipment body 13 and then penetrates through the inside of the packing 5, a second liquid collector 10 is fixedly arranged at the lower part of the inner wall of the equipment body 13, the lower end surface of the second liquid collector 10 is fixedly provided with the pipeline and penetrates through the liquid phase outlet 12, the packing 5 is arranged in the reactor, the packing 5 can select corresponding packing for reaction according to material components and characteristics, and then heat exchange is carried out at the bottom of the equipment, so that the heat exchange and the reaction are combined into a whole, the space occupation problem of the equipment is effectively solved, the heat exchange effect is effectively increased at the same time, has wide applicability and is easy to popularize.
The liquid phase import 3, the liquid phase export 12, gaseous phase import 11 and gaseous phase export 1 department all is provided with the ring flange, through setting up the ring flange, make the pipeline connect through the flange, and pipeline and flange are according to standard selection type, it is convenient to dismantle during the maintenance, the fixed check valve 6 that is provided with of heat exchange tube 9 whole body in the equipment body 13 outside, check valve 6 aim at carries gaseous phase material, prevent liquid phase material refluence, heat exchange tube 9 sets up to the sinuous coil form, make heat transfer effect better through setting up sinuously coiled heat exchange tube 9, heat exchange tube 9 is seamless steel pipe, the material is according to material property and selection types such as pressure, temperature, the purpose is in carrying gaseous phase material, the heat exchange material, packing 5 sets up between liquid distributor 4 and liquid redistributor 8, liquid distributor 4 and liquid redistributor 8 equally divide the liquid phase material distribute, make the reaction or heat transfer more abundant, the pipeline all adopts flange connection through the pipeline, pipeline all adopts flange connection, pipeline and flange select according to standard, it is convenient to dismantle during the maintenance.
Working principle: the top of the equipment body 13 is provided with a reaction stage, the reaction stage selects corresponding materials and filling 5 devices of the types according to material properties, reaction pressure, temperature and the like to carry out chemical reaction, and the bottom is provided with a heat exchange stage, and the heat exchange area is optimized according to the reaction condition (temperature) of the time and the reaction condition (temperature) of the next stage, so that the heat exchange effect is improved, the equipment occupation space problem is effectively solved, and the equipment has wide applicability and easy popularization.
Finally, it should be noted that: the foregoing description is only illustrative of the preferred embodiments of the present utility model, and although the present utility model has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments described, or equivalents may be substituted for elements thereof, and any modifications, equivalents, improvements or changes may be made without departing from the spirit and principles of the present utility model.
Claims (7)
1. The utility model provides a novel reactor with spray heat transfer, includes equipment body (13), its characterized in that: the utility model discloses a foam-removing device, which is characterized in that a gas-phase outlet (1) is fixedly arranged on the upper end face of an equipment body (13), a foam-removing device (2) is fixedly arranged on the upper part of the inner wall of the equipment body (13), a liquid-phase inlet (3) is arranged on one side of the equipment body (13), a pipeline penetrates into the equipment body (13) and is fixedly provided with a liquid distributor (4), a filler (5) is fixedly arranged in the middle of the inner wall of the equipment body (13), a first liquid collector (7) is fixedly arranged on the lower end face of the filler (5), a liquid redistributor (8) is fixedly arranged on the lower end face of the first liquid collector (7), a gas-phase inlet (11) is arranged on the lower part of the other side of the equipment body (13), a pipeline is arranged on the lower part of the gas-phase inlet (11), a liquid-phase outlet (12) is arranged on one side of the equipment body (13), the lower side of the gas-phase inlet (11) penetrates into the equipment body (13) and is fixedly provided with a heat exchange tube (9), one end of the heat exchange tube (9) penetrates into the inside the equipment body (13) and is fixedly provided with a second liquid collector (10) after penetrating into the equipment body (13), the lower end face of the second liquid collector (10) is fixedly provided with a pipeline and penetrates through the liquid phase outlet (12).
2. The novel reactor with spray heat exchange of claim 1, wherein: the flange plates are arranged at the positions of the liquid phase inlet (3), the liquid phase outlet (12), the gas phase inlet (11) and the gas phase outlet (1).
3. The novel reactor with spray heat exchange of claim 1, wherein: the whole body of the heat exchange tube (9) positioned at the outer side of the equipment body (13) is fixedly provided with a check valve (6).
4. The novel reactor with spray heat exchange of claim 1, wherein: the heat exchange tube (9) is arranged in a sinuous coil shape.
5. The novel reactor with spray heat exchange of claim 1, wherein: the heat exchange tube (9) is a seamless steel tube.
6. The novel reactor with spray heat exchange of claim 1, wherein: the packing (5) is arranged between the liquid distributor (4) and the liquid redistributor (8).
7. The novel reactor with spray heat exchange of claim 1, wherein: the pipelines are all connected through flanges.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322752437.8U CN220919222U (en) | 2023-10-13 | 2023-10-13 | Novel reactor with spray heat exchange function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322752437.8U CN220919222U (en) | 2023-10-13 | 2023-10-13 | Novel reactor with spray heat exchange function |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220919222U true CN220919222U (en) | 2024-05-10 |
Family
ID=90939090
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322752437.8U Active CN220919222U (en) | 2023-10-13 | 2023-10-13 | Novel reactor with spray heat exchange function |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220919222U (en) |
-
2023
- 2023-10-13 CN CN202322752437.8U patent/CN220919222U/en active Active
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