CN220496378U - Multi-connected mixed reaction device - Google Patents
Multi-connected mixed reaction device Download PDFInfo
- Publication number
- CN220496378U CN220496378U CN202322182100.8U CN202322182100U CN220496378U CN 220496378 U CN220496378 U CN 220496378U CN 202322182100 U CN202322182100 U CN 202322182100U CN 220496378 U CN220496378 U CN 220496378U
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- reaction
- aeration
- reactor
- tubes
- sampling
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 80
- 238000005273 aeration Methods 0.000 claims abstract description 39
- 230000001105 regulatory effect Effects 0.000 claims abstract description 15
- 239000007789 gas Substances 0.000 claims description 21
- 238000005070 sampling Methods 0.000 claims description 21
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 8
- 230000002572 peristaltic effect Effects 0.000 claims description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims description 4
- 239000002994 raw material Substances 0.000 abstract description 5
- 238000003760 magnetic stirring Methods 0.000 abstract description 4
- 238000010907 mechanical stirring Methods 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000000376 reactant Substances 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
Abstract
The utility model discloses a multi-connected mixed reaction device, and relates to the technical field of reaction devices. The device comprises a reactor and an aeration device, wherein the reactor comprises a plurality of reaction test tubes, the aeration device comprises aeration pipes, the quantity of the aeration pipes is equal to that of the reaction test tubes, one end of each aeration pipe can be arranged inside the corresponding aeration pipe, and the other end of each aeration pipe is connected with an air source through a flow regulating valve. According to the utility model, the reaction test tube is arranged to replace a beaker of a conventional multi-reactor, and the aeration tube is arranged to replace conventional mechanical stirring or magnetic stirring equipment, so that the reaction of a small amount of raw materials or the reaction with magnetic substances can be smoothly carried out.
Description
Technical Field
The utility model relates to the technical field of reaction devices, in particular to a multi-connected mixed reaction device.
Background
The device for mixing or reacting is usually a beaker (or a container such as a conical flask) and a six-link stirrer, and usually the reactants with required volume or mass are measured, one of the reactants is added into the container filled with the other reactant, such as a beaker, a conical flask and the like, then the mixture is placed under the six-link stirrer for reaction at a certain temperature for a certain time, and after the reaction is finished, the samples are manually sampled one by one, and then the relevant indexes of the samples are detected to evaluate the reaction condition. The device is more suitable for the reaction with larger solution volume and smaller influence of reaction time on experimental results, and when the solution volume is smaller, containers such as a beaker and the like can shake, float and even turn over in a water bath kettle, so that the problems of uneven heating and the like exist, and the experimental failure can be directly caused; meanwhile, in many experiments at present, stirring is required in the reaction process, but mechanical stirring or magnetic stirring is difficult to apply to reactions with fewer reaction raw materials or reactions with magnetic substances. Obviously, the conventional six-link mixing reaction device has great inconvenience and defects in use, and needs to be further improved.
Disclosure of Invention
In order to solve at least one of the problems described above, the present utility model provides a multiple mixing reaction apparatus that can be adapted to a reaction of a small amount of solution or a reaction involving a magnetic substance by using aeration instead of conventional mechanical stirring or magnetic stirring and using a reaction tube instead of a beaker.
The technical scheme of the utility model is as follows: the utility model provides a ally oneself with mixed reaction unit more, includes reactor and aeration equipment, wherein, the reactor includes many reaction test tubes, aeration equipment includes the aeration pipe, the quantity of aeration pipe with the quantity of reaction test tube equals, aeration pipe one end can be located inside the reaction test tube, the other end passes through the flow control valve and connects the air supply.
One embodiment of the utility model is that the reactor further comprises a constant temperature reactor, wherein a plurality of openings are arranged on the top of the constant temperature reactor, and the reaction test tube is arranged inside the constant temperature reactor through the openings.
Furthermore, the lower part of the constant temperature reactor is also provided with grooves which are in one-to-one correspondence with the openings and are arranged under the openings.
Furthermore, the constant temperature reactor is provided with a working medium outlet, and meanwhile, the constant temperature reactor is also internally provided with a heater and a temperature sensor.
One embodiment of the utility model is characterized in that a gas distribution pipe is further arranged between the flow regulating valve and the gas source, the gas distribution pipe is connected with the gas source through a pipeline, and a plurality of flow regulating valves are respectively connected with the gas distribution pipe.
One embodiment of the utility model is that the air source is one of an air pump or a nitrogen cylinder.
One embodiment of the utility model is characterized by further comprising a sampling device, wherein the sampling device comprises a plurality of sampling hoses, one ends of the sampling hoses can be arranged in the reaction test tube, and the other ends of the sampling hoses are arranged in the sampling tube through a multichannel peristaltic pump.
Compared with the prior art, the utility model has the following beneficial effects:
according to the utility model, the reaction test tube is arranged to replace a beaker of a conventional multi-reactor, and the aeration tube is arranged to replace conventional mechanical stirring or magnetic stirring equipment, so that the reaction with only a small amount of raw materials or magnetic raw materials can be smoothly carried out.
Drawings
FIG. 1 is a schematic view of the overall structure of the present utility model, wherein the reactor is a perspective view.
Detailed Description
The present utility model will be described in further detail with reference to examples and drawings, but embodiments of the present utility model are not limited thereto.
In the description of the present utility model, it should be noted that the azimuth or positional relationship indicated by the terms "upper", "lower", "inner", 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 are not indicative or implying that the apparatus or element in question must have a specific azimuth, be constructed and operated in a specific azimuth, and are not to be construed as limiting the present utility model.
Referring to fig. 1, a multi-connected mixing reaction device comprises a reactor 100 and an aeration device 200, wherein the reactor 100 comprises a plurality of reaction test tubes 101, the aeration device 200 comprises aeration pipes 204, the number of the aeration pipes 204 is equal to that of the reaction test tubes 101, one end of each aeration pipe 204 can be arranged inside the corresponding reaction test tube 101, and the other end of each aeration pipe 204 is connected with an air source 201 through a flow regulating valve 203.
Specifically, in fig. 1, the reactor 100 is shown in perspective, with the broken line portion being a blocked structure and the solid line portion being a unblocked structure. The reaction test tubes 101 may be set to conventional test tubes such as test tubes with a diameter of 16mm or 25mm, the number of the reaction test tubes 101 may be set according to actual demands such as 3, 5 or 8, and the size of each reaction test tube 101 may be set according to actual conditions such as setting the diameter of 2 reaction test tubes 101 to 16mm and the diameter of 3 reaction test tubes 101 to 25mm.
The aeration device 200 includes a plurality of aeration tubes 204 and a gas source 201, wherein the number of aeration tubes 204 is the same as the number of reaction tubes 101, and the ends of the aeration tubes 204 need to be disposed at the bottom of the reaction tubes 101 when in use, so that the aeration tubes 204 are required to have a sufficient length. Meanwhile, as for the air source 201, it is mainly to provide the gas required for aeration, so in the case that the reaction has no special requirement on the conditions, an air pump may be used as the air source 201; however, in some cases, the reaction requires a specific atmosphere, for example, some polymerization reactions require the removal of oxygen from the reaction solution, and therefore, a nitrogen bottle may be used as the gas source 201.
Meanwhile, for the aeration pipe 204, since the reaction test tube 101 is small, a proper aeration amount is required in the reaction, and for this purpose, a corresponding flow rate regulating valve 203 is further provided between the gas source 201 and the aeration pipe 204, and the flow rate of the gas entering the reaction test tube 101 is controlled by the flow rate regulating valve 203 so that the reaction is not affected.
From the viewpoint of use, the difficulty in setting the plurality of flow regulating valves 203 directly connected to the air source 201 is relatively high and difficult to manage, so in this embodiment, a gas distribution pipe 202 is further disposed between the flow regulating valves 203 and the air source 201, the gas distribution pipe 202 is transversely disposed, and the plurality of flow regulating valves 203 are connected to the gas distribution pipe 202 in parallel through a pipeline, and meanwhile, the gas distribution pipe 202 is connected to the air source 201. By arranging the air distribution pipe 202, the connection between the aeration pipe 204 and the air source 201 is more convenient and reasonable.
For many experiments, the reaction needs to be performed under a certain temperature condition, so in this embodiment, the reactor 100 further includes a constant temperature reactor 105, and the internal temperature of the constant temperature reactor 105 can be maintained under a certain temperature condition, so that a relatively common water bath pot, an oil bath pot, etc. can be selected, which are the same as the common water bath pot, etc., and in this embodiment, a corresponding heater and a temperature sensor are also disposed in the constant temperature reactor 105. The top of the constant temperature reactor 105 is provided with a cover plate 104, the cover plate 104 is provided with a plurality of openings 102, and the reaction test tube 101 can be arranged in the constant temperature reactor 105 through the openings 102, so that the reaction can be smoothly carried out, and meanwhile, the diameter of the opening 102 is equal to or slightly larger than the diameter of the reaction test tube 101 for the stability of the reaction test tube 101, so that the problem that the stability of the reaction test tube 101 is poor due to the overlarge size difference of the opening and the reaction test tube is avoided.
Further, in some cases, even if the diameter of the opening 102 is defined, the stability of the reaction tube 101 is still not very good, for this purpose, in this embodiment, a plurality of grooves 103 are further provided at the bottom of the isothermal reactor 105, these grooves 103 and the opening 102 are in one-to-one correspondence, and the corresponding grooves 103 and the opening 102 are on the same vertical line, and in use, the bottom of the reaction tube 101 may be provided inside the grooves 103, increasing its stability.
For the isothermal reactor 105, such as an oil bath or a water bath, it is necessary to provide a corresponding working medium, such as oil or water, and the working medium in the isothermal reactor 105 needs to be replaced during long-term use, so that a corresponding working medium outlet 106 is further provided at the bottom of the isothermal reactor 105, and the working medium in the isothermal reactor 105 can be discharged to replace a new working medium.
In the reaction process, the product after the reaction is usually required to be sampled and analyzed, and for the reaction with strict requirements on the reaction time, the sampling time is related to the level of the final product and the formation of byproducts, so in this embodiment, a new sampling device 300 is also designed. The sampling device 300 comprises a plurality of sampling hoses 303 and a multi-channel peristaltic pump 301, wherein one end of each sampling hose 303 penetrates through the pump head of the multi-channel peristaltic pump 301 and is connected with the sampling tube 302, the other end of each sampling hose 303 can be arranged inside the reaction test tube 101, and when sampling is required, the plurality of sampling hoses 303 are arranged inside the reaction test tube 101, and the multi-channel peristaltic pump 301 is started, so that a plurality of samples are taken out simultaneously.
When the device is used, the constant temperature reactor is regulated to the reaction temperature, after corresponding raw materials are injected into a plurality of reaction test tubes, all the reaction test tubes are placed into the constant temperature reactor, then the aeration tubes are placed into the reaction test tubes, according to actual conditions, an air source is selected as an air pump or a nitrogen cylinder, the flow rate of the air is regulated to a proper flow rate by utilizing a flow regulating valve, and then the air source is started to enable the aeration amount in each reaction tube to be the same. After reacting for a certain time, placing the sampling tube into a reaction test tube to be sampled, and starting a multichannel peristaltic pump.
The foregoing is only a preferred embodiment of the present utility model, but the scope of the present utility model is not limited thereto, and any changes or substitutions easily contemplated by those skilled in the art within the technical scope of the present utility model disclosed in the embodiments of the present utility model should be covered by the present utility model. Therefore, the protection scope of the present utility model should be subject to the protection scope of the claims.
Claims (5)
1. The multi-connected mixed reaction device is characterized by comprising a reactor and an aeration device, wherein the reactor comprises a plurality of reaction test tubes, the aeration device comprises aeration tubes, the number of the aeration tubes is equal to that of the reaction test tubes, one end of each aeration tube can be arranged in each reaction test tube, and the other end of each aeration tube is connected with an air source through a flow regulating valve;
a gas distribution pipe is further arranged between the flow regulating valve and the gas source, the gas distribution pipe is connected with the gas source through a pipeline, and a plurality of flow regulating valves are respectively connected with the gas distribution pipe;
still include sampling device, sampling device includes many sampling hoses, sampling hose one end can be located inside the reaction test tube, the other end is located inside the sampling tube through multichannel peristaltic pump.
2. The multiple hybrid reaction device of claim 1, wherein the reactor further comprises a isothermal reactor, wherein a plurality of openings are provided on top of the isothermal reactor, and wherein the reaction tubes are provided inside the isothermal reactor through the openings.
3. The multiple mixing reaction device according to claim 2, wherein the lower part of the constant temperature reactor is further provided with grooves, which are in one-to-one correspondence with the openings and are provided directly below the openings.
4. The multi-connected mixed reaction device according to claim 2, wherein the constant temperature reactor is provided with a working medium outlet, and a heater and a temperature sensor are also arranged inside the constant temperature reactor.
5. The multiple hybrid reaction device of claim 1, wherein the gas source is one of a gas pump or a nitrogen cylinder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202322182100.8U CN220496378U (en) | 2023-08-15 | 2023-08-15 | Multi-connected mixed reaction device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202322182100.8U CN220496378U (en) | 2023-08-15 | 2023-08-15 | Multi-connected mixed reaction device |
Publications (1)
Publication Number | Publication Date |
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CN220496378U true CN220496378U (en) | 2024-02-20 |
Family
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Family Applications (1)
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CN202322182100.8U Active CN220496378U (en) | 2023-08-15 | 2023-08-15 | Multi-connected mixed reaction device |
Country Status (1)
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CN (1) | CN220496378U (en) |
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2023
- 2023-08-15 CN CN202322182100.8U patent/CN220496378U/en active Active
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