CN215963495U - Gas-liquid mass transfer synthesis tower for alkali sodium methoxide production process - Google Patents
Gas-liquid mass transfer synthesis tower for alkali sodium methoxide production process Download PDFInfo
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- CN215963495U CN215963495U CN202122119706.8U CN202122119706U CN215963495U CN 215963495 U CN215963495 U CN 215963495U CN 202122119706 U CN202122119706 U CN 202122119706U CN 215963495 U CN215963495 U CN 215963495U
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- 230000015572 biosynthetic process Effects 0.000 title claims abstract description 64
- 238000003786 synthesis reaction Methods 0.000 title claims abstract description 64
- WQDUMFSSJAZKTM-UHFFFAOYSA-N Sodium methoxide Chemical compound [Na+].[O-]C WQDUMFSSJAZKTM-UHFFFAOYSA-N 0.000 title claims abstract description 40
- 239000007788 liquid Substances 0.000 title claims abstract description 38
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 22
- 239000003513 alkali Substances 0.000 title abstract description 4
- 230000007246 mechanism Effects 0.000 claims abstract description 26
- 238000005273 aeration Methods 0.000 claims abstract description 14
- 238000000034 method Methods 0.000 claims abstract description 10
- 230000008569 process Effects 0.000 claims abstract description 7
- 238000005516 engineering process Methods 0.000 claims abstract description 5
- 238000003756 stirring Methods 0.000 claims description 16
- 238000007599 discharging Methods 0.000 claims description 6
- 238000011084 recovery Methods 0.000 claims description 4
- 238000006243 chemical reaction Methods 0.000 abstract description 18
- 239000002585 base Substances 0.000 abstract description 7
- 238000010276 construction Methods 0.000 abstract 2
- 239000000463 material Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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Abstract
The utility model relates to a gas-liquid mass transfer synthesis tower for the alkali sodium methoxide production process, which comprises a bearing base and a synthesis tower positioned at the top of the bearing base, wherein an aeration mechanism is fixedly arranged inside the synthesis tower, a mixing mechanism for mixing synthesis is fixedly arranged on one side of the synthesis tower, a circulating structure for collecting energy is arranged at the top of the synthesis tower, and the aeration mechanism comprises a pump positioned inside the inner wall of the synthesis tower and gas guide pipes uniformly distributed on the inner bottom wall of the synthesis tower. This vapour liquid mass transfer synthetic tower for alkaline process sodium methoxide production technology, aeration mechanism evenly sets up on the diapire of synthetic tower, can make gaseous even react and exchange with liquid, improves reaction efficiency, and mixing mechanism can break up gas bubble, forms more compact bubble and the liquid production efficient reaction of inside, collects through loop construction, can make other reentrant equipment with loop construction and intake-tube connection simultaneously, improves the utilization efficiency.
Description
Technical Field
The utility model relates to the technical field of synthesis towers, in particular to a gas-liquid mass transfer synthesis tower for an alkaline sodium methoxide production process.
Background
The synthesis tower is a gas-liquid mass transfer device widely used in the production of oil refining, chemical industry, petrochemical industry, biochemical industry, pharmacy and the like, and can be divided into a plate tower and a packed tower according to the structural form of a part in contact with gas and liquid in the tower.
When the existing synthesis tower is used, the internal raw materials can not react fully and quickly, the efficiency is low, and an improved space exists, so that the gas-liquid mass transfer synthesis tower for the alkaline sodium methoxide production process is provided to solve the problems in the prior art.
SUMMERY OF THE UTILITY MODEL
Aiming at the defects of the prior art, the utility model provides the gas-liquid mass transfer synthesis tower for the alkaline sodium methoxide production process, which has the advantages of high reaction efficiency and the like, and solves the problems that the internal raw materials can not be fully and quickly reacted, the efficiency is low, and the improved space exists.
In order to achieve the purpose of high reaction efficiency, the utility model provides the following technical scheme: a gas-liquid mass transfer synthesis tower for an alkaline sodium methoxide production process comprises a bearing base and a synthesis tower positioned at the top of the bearing base, wherein an aeration mechanism is fixedly installed inside the synthesis tower, a mixing mechanism for mixing synthesis is fixedly installed on one side of the synthesis tower, and a circulating structure for collecting and saving energy is arranged at the top of the synthesis tower;
the aeration mechanism comprises a pump positioned inside the inner wall of the synthesis tower and air guide pipes uniformly distributed on the inner bottom wall of the synthesis tower, and the air guide pipes are provided with exhaust ports;
in order to improve the vapor-liquid mass transfer efficiency, the mixing mechanism comprises a hybrid power box positioned on one side of the synthesis tower, a stirring frame extending to the inside of the synthesis tower is fixedly installed at the output end of the hybrid power box, and a bearing seat corresponding to the stirring frame is fixedly installed on the inner wall of one side of the synthesis tower, which is far away from the hybrid power box.
Furthermore, the output end of the pump is fixedly provided with a check valve communicated with the air duct.
Furthermore, the circulating structure comprises a gas-collecting hood positioned at the top of the synthesis tower, and a fan bracket and a recovery fan which correspond to the gas-collecting hood are fixedly installed in the synthesis tower.
Further, the input fixed mounting of pump machine has the intake pipe, one side fixed mounting of synthetic tower has the inlet pipe.
Furthermore, a circulating pipe is fixedly installed on one side of the gas-collecting hood, and the inner wall of the gas-collecting hood is conical.
Furthermore, a discharge pipe for discharging is fixedly arranged on one side of the synthesis tower, and a control valve is arranged on the discharge pipe.
Furthermore, a movable bearing extending into the bearing seat is fixedly mounted at one end of the stirring frame close to the bearing seat.
Furthermore, stirring support rods are uniformly and fixedly installed on the outer surface of the stirring frame.
Compared with the prior art, the utility model provides the gas-liquid mass transfer synthesis tower for the alkaline sodium methoxide production process, which has the following beneficial effects:
this vapour liquid mass transfer synthetic tower is used in alkaline process sodium methoxide production technology, aeration mechanism evenly sets up on the diapire of synthetic tower, can make gaseous even react and exchange with liquid, improve reaction efficiency, mixing mechanism can break up the gas bubble, form more compact bubble and inside liquid and produce the efficient reaction, collect through loop configuration, simultaneously can be with loop configuration and intake-tube connection, can make other equipment that gets into again, improve the utilization efficiency, perhaps be connected other and other equipment and handle inside the reentrant reaction equipment, it can not be abundant with quick reaction to have solved inside raw materials, efficiency is lower, there is the problem in modified space.
Drawings
FIG. 1 is a schematic structural view of the present invention;
fig. 2 is a schematic perspective view of the present invention.
In the figure: 1 bearing base, 2 synthetic towers, 3 hybrid power boxes, 4 stirring frames, 5 gas collecting hoods, 6 circulating pipes, 7 fan supports, 8 recovery fans, 9 feeding pipes, 10 bearing seats, 11 pump machines, 12 check valves, 13 gas guide pipes, 14 gas inlet pipes, 15 gas inlet pipes and 16 discharge pipes.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1-2, a vapor-liquid mass transfer synthesis tower for alkali sodium methoxide production process comprises a bearing base 1 and a synthesis tower 2 positioned at the top of the bearing base 1, wherein an aeration mechanism is fixedly installed inside the synthesis tower 2, a mixing mechanism for mixing synthesis is fixedly installed at one side of the synthesis tower 2, and a circulating structure for collecting and saving energy is arranged at the top of the synthesis tower 2;
the aeration mechanism comprises a pump 11 positioned in the inner wall of the synthesis tower 2 and gas guide pipes 13 uniformly distributed on the inner bottom wall of the synthesis tower 2, wherein the gas guide pipes 13 are provided with gas outlets 14, the aeration mechanism is uniformly arranged on the bottom wall of the synthesis tower 2, so that gas can uniformly react and exchange with liquid, and the reaction efficiency is improved;
wherein, the output fixed mounting of pump machine 11 has the check valve 12 with air duct 13 intercommunication, can effectually avoid pump machine 11 when not running, and inside liquid backward flow enters into pump machine 11's inside, causes equipment damage, influences the phenomenon of normal use.
In order to improve the vapor-liquid mass transfer efficiency, the mixing mechanism comprises a hybrid power box 3 positioned on one side of the synthesis tower 2, an output end of the hybrid power box 3 is fixedly provided with a stirring frame 4 extending to the inside of the synthesis tower 2, and a bearing seat 10 corresponding to the stirring frame 4 is fixedly arranged on the inner wall of one side, far away from the hybrid power box 3, of the synthesis tower 2.
It should be noted that, one end of the stirring frame 4 close to the receiving seat 10 is fixedly provided with a movable bearing extending to the inside of the receiving seat 10, and the outer surface of the stirring frame 4 is uniformly and fixedly provided with a stirring support rod.
Meanwhile, a reaction partition plate can be arranged at the top of the mixing mechanism in the synthesis tower 2, so that the effect of gas-liquid contact area is improved, heating equipment can be arranged, the reaction rate is improved, and the structures are the prior art, so that special description is not given.
In this embodiment, circulation structure is including the gas collecting channel 5 that is located 2 tops of synthetic tower, the inside fixed mounting of synthetic tower 2 has fan support 7 and recovery fan 8 corresponding with gas collecting channel 5, the input fixed mounting of pump 11 has intake pipe 15, one side fixed mounting of synthetic tower 2 has inlet pipe 9, through having set up circulation structure, gaseous entering synthetic tower 2 inside through aeration mechanism and reacting with liquid after, there is the partial gas that does not completely react, collect through circulation structure, can be connected circulation structure and intake pipe 15 simultaneously, can make other equipment that reenters, the efficiency of utilization is improved, or be connected other and other equipment and handle the back and get into inside the reaction equipment once more.
In order to improve the gas collection efficiency, a circulating pipe 6 is fixedly installed on one side of the gas collecting hood 5, and the inner wall of the gas collecting hood 5 is conical, so that the use of a user can be facilitated.
In this embodiment, a material discharging pipe 16 for discharging material is fixedly installed at one side of the synthesis tower 2, and a control valve is arranged on the material discharging pipe 16, so that the raw material enters the inside of the apparatus from the material feeding pipe 9 to complete vapor-liquid mass transfer, and then is discharged through the material discharging pipe 16.
This embodiment is when using, aeration mechanism evenly sets up on the diapire of synthetic tower 2, can make gaseous even react with liquid and exchange, improve reaction efficiency, mixing mechanism can break up gaseous bubble, form more fine and close bubble and inside liquid and produce the efficient reaction, collect through loop configuration, can be connected loop configuration and intake pipe 15 simultaneously, can make other equipment that reenters, improve the utilization efficiency, perhaps with other equipment connection handle the back reentrant reaction equipment inside.
The beneficial effects of the above embodiment are as follows:
this vapour liquid mass transfer synthetic tower for alkaline process sodium methoxide production technology, aeration mechanism evenly sets up on the diapire of synthetic tower 2, can make gaseous even react and exchange with liquid, improve reaction efficiency, mixing mechanism can break up the gas bubble, form more compact bubble and the liquid of inside and produce the efficient reaction, collect through loop configuration, can be connected loop configuration and intake pipe 15 simultaneously, can make other equipment that gets into again, improve utilization efficiency, perhaps with other inside getting into reaction equipment after being connected with other equipment and handling once more.
The electrical components shown herein are electrically connected to a main controller and a power supply, the main controller can be a conventional known device controlled by a computer, and the conventional power connection technology disclosed in the prior art is not described in detail herein.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation, an element defined by the phrase "comprising an … …" does not exclude the presence of other identical elements in a process, method, article, or apparatus that comprises the element.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the utility model, the scope of which is defined in the appended claims and their equivalents.
Claims (8)
1. The utility model provides a vapour liquid mass transfer synthetic tower for alkaline process sodium methoxide production technology, includes bearing base (1) and synthetic tower (2) that are located bearing base (1) top, its characterized in that: an aeration mechanism is fixedly arranged in the synthesis tower (2), a mixing mechanism for mixing synthesis is fixedly arranged on one side of the synthesis tower (2), and a circulating structure for collecting and saving energy is arranged at the top of the synthesis tower (2);
the aeration mechanism comprises a pump (11) positioned inside the inner wall of the synthesis tower (2) and air guide pipes (13) uniformly distributed on the inner bottom wall of the synthesis tower (2), and the air guide pipes (13) are provided with exhaust ports (14);
in order to improve the vapor-liquid mass transfer efficiency, the mixing mechanism comprises a hybrid power box (3) positioned on one side of the synthesis tower (2), a stirring frame (4) extending into the synthesis tower (2) is fixedly installed at the output end of the hybrid power box (3), and a bearing seat (10) corresponding to the stirring frame (4) is fixedly installed on the inner wall of one side, away from the hybrid power box (3), of the synthesis tower (2).
2. The gas-liquid mass transfer synthesis tower for the alkaline sodium methoxide production process according to claim 1, which is characterized in that: the output end of the pump (11) is fixedly provided with a check valve (12) communicated with the air duct (13).
3. The gas-liquid mass transfer synthesis tower for the alkaline sodium methoxide production process according to claim 2, which is characterized in that: the circulating structure comprises a gas-collecting hood (5) positioned at the top of the synthesis tower (2), and a fan bracket (7) and a recovery fan (8) which correspond to the gas-collecting hood (5) are fixedly installed in the synthesis tower (2).
4. The gas-liquid mass transfer synthesis tower for the alkaline sodium methoxide production process according to claim 3, which is characterized in that: the input fixed mounting of pump machine (11) has intake pipe (15), one side fixed mounting of synthetic tower (2) has inlet pipe (9).
5. The gas-liquid mass transfer synthesis tower for the alkaline sodium methoxide production process according to claim 4, which is characterized in that: one side of the gas-collecting hood (5) is fixedly provided with a circulating pipe (6), and the inner wall of the gas-collecting hood (5) is conical.
6. The gas-liquid mass transfer synthesis tower for the alkaline sodium methoxide production process according to claim 5, which is characterized in that: one side of the synthesis tower (2) is fixedly provided with a discharge pipe (16) for discharging, and the discharge pipe (16) is provided with a control valve.
7. The gas-liquid mass transfer synthesis tower for the alkaline sodium methoxide production process according to claim 6, which is characterized in that: one end of the stirring frame (4) close to the bearing seat (10) is fixedly provided with a movable bearing extending into the bearing seat (10).
8. The gas-liquid mass transfer synthesis tower for the alkaline sodium methoxide production process according to claim 7, which is characterized in that: stirring support rods are uniformly and fixedly arranged on the outer surface of the stirring frame (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122119706.8U CN215963495U (en) | 2021-09-03 | 2021-09-03 | Gas-liquid mass transfer synthesis tower for alkali sodium methoxide production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122119706.8U CN215963495U (en) | 2021-09-03 | 2021-09-03 | Gas-liquid mass transfer synthesis tower for alkali sodium methoxide production process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215963495U true CN215963495U (en) | 2022-03-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122119706.8U Active CN215963495U (en) | 2021-09-03 | 2021-09-03 | Gas-liquid mass transfer synthesis tower for alkali sodium methoxide production process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215963495U (en) |
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2021
- 2021-09-03 CN CN202122119706.8U patent/CN215963495U/en active Active
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A vapor-liquid mass transfer synthesis tower for sodium methoxide production process by alkali method Effective date of registration: 20220706 Granted publication date: 20220308 Pledgee: Ningxia East Guarantee Co.,Ltd. Pledgor: NINGXIA HENGHUI LUFENG TECHNOLOGY Co.,Ltd. Registration number: Y2022640000012 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20230625 Granted publication date: 20220308 Pledgee: Ningxia East Guarantee Co.,Ltd. Pledgor: NINGXIA HENGHUI LUFENG TECHNOLOGY Co.,Ltd. Registration number: Y2022640000012 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A Vapor Liquid Mass Transfer Synthesis Tower for Alkali Sodium methoxide Production Process Effective date of registration: 20230713 Granted publication date: 20220308 Pledgee: Ningxia East Guarantee Co.,Ltd. Pledgor: NINGXIA HENGHUI LUFENG TECHNOLOGY Co.,Ltd. Registration number: Y2023640000022 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Granted publication date: 20220308 Pledgee: Ningxia East Guarantee Co.,Ltd. Pledgor: NINGXIA HENGHUI LUFENG TECHNOLOGY Co.,Ltd. Registration number: Y2023640000022 |