CN219983928U - Equipment for chemical distillation and purification - Google Patents
Equipment for chemical distillation and purification Download PDFInfo
- Publication number
- CN219983928U CN219983928U CN202321038522.1U CN202321038522U CN219983928U CN 219983928 U CN219983928 U CN 219983928U CN 202321038522 U CN202321038522 U CN 202321038522U CN 219983928 U CN219983928 U CN 219983928U
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- CN
- China
- Prior art keywords
- distillation
- chamber
- fixedly connected
- retort
- pipe
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- 238000004821 distillation Methods 0.000 title claims abstract description 77
- 239000000126 substance Substances 0.000 title claims abstract description 24
- 238000000746 purification Methods 0.000 title claims abstract description 21
- 238000003756 stirring Methods 0.000 claims abstract description 18
- 239000011521 glass Substances 0.000 claims abstract description 15
- 239000000428 dust Substances 0.000 claims abstract description 10
- 239000000110 cooling liquid Substances 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 33
- 238000001816 cooling Methods 0.000 claims description 17
- 238000007789 sealing Methods 0.000 claims description 13
- 238000009833 condensation Methods 0.000 claims description 10
- 230000005494 condensation Effects 0.000 claims description 10
- 230000017525 heat dissipation Effects 0.000 claims description 9
- 238000012856 packing Methods 0.000 claims description 6
- 239000010410 layer Substances 0.000 claims description 5
- 239000011229 interlayer Substances 0.000 claims description 2
- 239000002994 raw material Substances 0.000 abstract description 11
- 230000009471 action Effects 0.000 abstract description 6
- 239000012535 impurity Substances 0.000 abstract description 4
- 238000000034 method Methods 0.000 description 7
- 238000005457 optimization Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 239000010865 sewage Substances 0.000 description 4
- 238000011049 filling Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000004321 preservation Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 210000003437 trachea Anatomy 0.000 description 2
- 238000010977 unit operation Methods 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000013064 chemical raw material Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses equipment for chemical distillation and purification, which comprises a distillation tank, wherein the bottom of the distillation tank is fixedly connected with a distillation chamber, the top of the distillation chamber is fixedly connected with a motor box, the top of the inner wall of the motor box is fixedly connected with a motor, the output end of the motor penetrates into the distillation chamber and is fixedly connected with a main rod, and the surface of the main rod is fixedly connected with a stirring blade. According to the utility model, through the arrangement of the motor and the condensing chamber, the main rod is driven to rotate by the starting motor, and the stirring blade is driven by the main rod to sufficiently stir, so that chemical raw materials are uniformly heated and evaporated, evaporated gas enters the dust fall chamber through the air pipe to generate flow, so that impurities in the gas cannot rise and fall, and the remaining clean gas rises into the guide pipe and then enters the spiral glass pipe to be condensed, so that the condensing speed is increased under the action of cooling liquid, the working efficiency is improved, the use of a user is facilitated, and the practicability of distillation and purification equipment is improved.
Description
Technical Field
The utility model relates to the technical field of distillation purification, in particular to equipment for chemical distillation purification.
Background
The distillation purification is a thermodynamic separation and purification process, and the unit operation process of utilizing different boiling points of all components in mixed liquid or liquid-solid system to evaporate low boiling point components and then condensing to separate the whole components is the combination of evaporation and condensation unit operation.
However, the existing distillation and purification equipment is not heated uniformly enough in the process of distilling and extracting chemical raw materials, and the condensation speed is too slow, so that the working efficiency is reduced, the use of users is inconvenient, and the practicability of the distillation and purification equipment is reduced.
Disclosure of Invention
In order to solve the problems in the prior art, the utility model aims to provide equipment for chemical distillation and purification, which has the advantages of uniform heating and high condensation speed, and solves the problems of low heating and condensation speed and reduced working efficiency in the process of distilling and extracting chemical raw materials by using the existing distillation and purification equipment.
In order to achieve the above purpose, the present utility model provides the following technical solutions: the utility model provides a chemical industry distillation purification is with equipment, includes the retort, the bottom fixedly connected with distillation chamber of retort, the top fixedly connected with motor box of distillation chamber, the top fixedly connected with motor of motor box inner wall, the output of motor runs through to the distillation chamber inside and fixedly connected with mobile jib, the fixed surface of mobile jib is connected with the stirring leaf, the top of distillation chamber is provided with the trachea, the top of retort is provided with the dust fall room, the trachea runs through distillation chamber and motor box in proper order and extends to the inside of dust fall room, the top intercommunication of retort has the pipe;
the cooling tank is arranged on the right side of the distillation tank, a condensing chamber is arranged at the top of the cooling tank, cooling liquid is arranged in the condensing chamber, the output end of the guide pipe penetrates through the condensing chamber and is communicated with a spiral glass tube, a finished product chamber is arranged at the bottom of the cooling tank, the output end of the spiral glass tube penetrates through the finished product chamber, and a first water pump is communicated with the bottom of the right side of the cooling tank.
As the preferable mode of the utility model, the front side of the distillation tank is provided with the filling port, the front side of the filling port is fixedly connected with the sealing ring, the front side of the filling port is in threaded connection with the sealing cover, and the front side of the sealing cover is provided with the glass window.
Preferably, the interlayer of the distillation pot and the distillation chamber is provided with an insulating layer.
As the preferable mode of the utility model, the left side of the distillation tank is provided with the pure water tank, the output end of the pure water tank is communicated with the second water pump, the output end of the second water pump is communicated with the water pipe, the water pipe penetrates into the distillation chamber, the bottoms of the back surfaces of the distillation tank and the cooling tank are respectively provided with a through hole, the through holes are communicated with a connecting pipe, and the two ends of the connecting pipe are respectively provided with an electric valve.
Preferably, heat dissipation pits are arranged on the periphery of the condensation chamber, and the number of the heat dissipation pits is a plurality of.
As the preferable mode of the utility model, the surface of the stirring blade is fixedly connected with a tooth block, and the front surface of the stirring blade is provided with a plurality of through holes with uniform size.
Compared with the prior art, the utility model has the following beneficial effects:
1. according to the utility model, through the arrangement of the motor and the condensing chamber, the main rod is driven to rotate by the starting motor, and the stirring blade is driven by the main rod to sufficiently stir, so that chemical raw materials are uniformly heated and evaporated, evaporated gas enters the dust fall chamber through the air pipe to generate flow, so that impurities in the gas cannot rise and fall, and the remaining clean gas rises into the guide pipe and then enters the spiral glass pipe to be condensed, so that the condensing speed is increased under the action of cooling liquid, the working efficiency is improved, the use of a user is facilitated, and the practicability of distillation and purification equipment is improved.
2. The utility model is convenient to observe distillation conditions when the equipment works by arranging the sealing ring and the glass window, and simultaneously avoids leakage of distillation gas.
Drawings
FIG. 1 is a schematic view of a front cross-section of the structure of the present utility model;
FIG. 2 is a schematic elevational view of the structure of the present utility model;
fig. 3 is a schematic top view of the structure of the present utility model.
In the figure: 1. a distillation pot; 2. a distillation chamber; 3. a motor box; 4. a motor; 5. a main rod; 6. stirring the leaves; 7. an air pipe; 8. a dust fall room; 9. a conduit; 10. a cooling tank; 11. a condensing chamber; 12. a cooling liquid; 13. a spiral glass tube; 14. a finished product chamber; 15. a first water pump; 16. a filler port; 17. a seal ring; 18. sealing cover; 19. a glazing; 20. a heat preservation layer; 21. a pure water tank; 22. a second water pump; 23. a water pipe; 24. a through port; 25. a connecting pipe; 26. an electric valve; 27. a heat dissipation pit; 28. tooth blocks; 29. and a through hole.
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.
As shown in fig. 1 to 3, the chemical distillation purification equipment comprises a distillation tank 1, wherein the bottom of the distillation tank 1 is fixedly connected with a distillation chamber 2, the top of the distillation chamber 2 is fixedly connected with a motor box 3, the top of the inner wall of the motor box 3 is fixedly connected with a motor 4, the output end of the motor 4 penetrates into the distillation chamber 2 and is fixedly connected with a main rod 5, the surface of the main rod 5 is fixedly connected with a stirring blade 6, the top of the distillation chamber 2 is provided with an air pipe 7, the top of the distillation tank 1 is provided with a dust fall chamber 8, the air pipe 7 sequentially penetrates through the distillation chamber 2 and the motor box 3 and extends into the dust fall chamber 8, and the top of the distillation tank 1 is communicated with a guide pipe 9;
the right side of retort 1 is provided with cooling tank 10, and cooling tank 10's top is provided with condensation chamber 11, and the inside of condensation chamber 11 is provided with coolant liquid 12, and the output of pipe 9 runs through to condensation chamber 11's inside and communicates there is spiral glass pipe 13, and cooling tank 10's bottom is provided with finished product room 14, and spiral glass pipe 13's output runs through to the inside of finished product room 14, and cooling tank 10 right side's bottom communicates there is first water pump 15.
Referring to fig. 2 and 3, a packing port 16 is formed in the front of the distillation tank 1, a sealing ring 17 is fixedly connected to the front of the packing port 16, a sealing cover 18 is in threaded connection with the front of the packing port 16, and a glass window 19 is arranged on the front of the sealing cover 18.
As a technical optimization scheme of the utility model, the arrangement of the sealing ring 17 and the glass window 19 facilitates the observation of distillation conditions during the operation of the equipment, and simultaneously avoids the leakage of distilled gas.
Referring to fig. 1, the distillation tank 1 and the distillation chamber 2 are each provided with an insulating layer 20.
As a technical optimization scheme of the utility model, the heat in the distillation chamber 2 can not be lost in a large amount through the arrangement of the heat preservation layer 20, and the working efficiency is improved more quickly by heating.
Referring to fig. 1, 2 and 3, a pure water tank 21 is disposed at the left side of the distillation tank 1, an output end of the pure water tank 21 is communicated with a second water pump 22, an output end of the second water pump 22 is communicated with a water pipe 23, the water pipe 23 penetrates into the distillation chamber 2, through holes 24 are formed in bottoms of the back surfaces of the distillation tank 1 and the cooling tank 10, the through holes 24 are communicated with a connecting pipe 25, and electric valves 26 are disposed at two ends of the connecting pipe 25.
As a technical optimization scheme of the utility model, the distillation chamber 2 can be cleaned without impurities through the arrangement of the pure water tank 21 and the second water pump 22, so that dangerous accidents caused by chemical reaction of residual chemical raw materials and another chemical raw material are avoided.
Referring to fig. 1 and 2, heat dissipation pits 27 are provided around the condensation chamber 11, and the number of heat dissipation pits 27 is a plurality.
As a technical optimization scheme of the utility model, the cooling liquid 12 increases the contact area with air by arranging the heat dissipation pits 27, so that the heat dissipation efficiency is improved.
Referring to fig. 1, a tooth block 28 is fixedly connected to the surface of the stirring blade 6, and a plurality of through holes 29 with uniform size are formed in the front surface of the stirring blade 6.
As a technical optimization scheme of the utility model, through the arrangement of the tooth blocks 28 and the through holes 29, the chemical raw materials of liquid and solid can be fully stirred, and the temperature rising distillation speed is improved.
The working principle and the using flow of the utility model are as follows: when the device is used, a user inputs chemical raw materials from a filler port 16, the chemical raw materials are tightly connected with a sealing cover 18 through threads, a motor 4 is started to enable the motor 4 to drive stirring blades 6 at two sides of a main rod 5 to rotate at a constant speed, the chemical raw materials are uniformly heated, the temperature of the chemical raw materials is quickly increased, evaporation gas is enabled to flow into a dust fall chamber 8 through a gas pipe 7, impurities in the gas cannot rise and fall down, the remaining clean gas rises into a guide pipe 9 and then enters a spiral glass pipe 13 to be condensed, the cooled gas is quickly condensed under the action of a cooling liquid 12, the cooled gas drops into a finished product chamber 14, a first water pump 15 is started after the purified finished product is collected, purified finished product is fed into a required pipeline, when the chemical raw materials are required to be replaced, a second water pump 22 is started to pump pure water from a pure water tank 21 into a distillation chamber 2, the stirring blades 6 are started to stir and clean the distillation chamber 2, an electric valve 26 is opened at the same time, sewage is enabled to enter the interior of the finished product chamber 14 through a port 24 to be washed, the sewage is pressed into a sewage pipe 23 to be discharged, and the second water pump 22, the electric valve 26 and the first water pump 15 are sequentially closed after the sewage is washed for later use.
It is noted that relational terms such as first and second, and the like are 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. Moreover, 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.
Although embodiments of the present utility model have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made therein 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 (6)
1. The utility model provides a chemical industry distillation purification is with equipment, includes retort (1), its characterized in that: the utility model discloses a distillation retort, including distillation retort, motor box, air pipe (7) are provided with distillation retort (1), motor box (3) are fixedly connected with in the bottom of distillation retort (1), motor box (3) are fixedly connected with in the top of inner wall of motor box (3), the output of motor (4) runs through to distillation retort (2) inside and fixedly connected with mobile jib (5), stirring leaf (6) are fixedly connected with on the surface of mobile jib (5), the top of distillation retort (2) is provided with air pipe (7), the top of distillation retort (1) is provided with dust fall room (8), air pipe (7) run through distillation retort (2) and motor box (3) in proper order and extend to the inside of dust fall room (8), the top intercommunication of distillation retort (1) has pipe (9);
the cooling tank is characterized in that a cooling tank (10) is arranged on the right side of the distillation tank (1), a condensing chamber (11) is arranged at the top of the cooling tank (10), cooling liquid (12) is arranged in the condensing chamber (11), an output end of the guide pipe (9) penetrates through the condensing chamber (11) and is communicated with a spiral glass pipe (13), a finished product chamber (14) is arranged at the bottom of the cooling tank (10), an output end of the spiral glass pipe (13) penetrates through the finished product chamber (14), and a first water pump (15) is communicated with the bottom of the right side of the cooling tank (10).
2. The apparatus for chemical distillation purification according to claim 1, wherein: the distillation retort is characterized in that a packing opening (16) is formed in the front face of the distillation retort (1), a sealing ring (17) is fixedly connected to the front face of the packing opening (16), a sealing cover (18) is connected to the front face of the packing opening (16) in a threaded mode, and a glass window (19) is arranged on the front face of the sealing cover (18).
3. The apparatus for chemical distillation purification according to claim 1, wherein: the interlayer of the distillation pot (1) and the distillation chamber (2) is provided with an insulating layer (20).
4. The apparatus for chemical distillation purification according to claim 1, wherein: the left side of retort (1) is provided with pure water tank (21), the output intercommunication of pure water tank (21) has second water pump (22), the output intercommunication of second water pump (22) has water pipe (23), inside to distillation chamber (2) is run through to water pipe (23), vent (24) have all been seted up to the bottom at retort (1) and cooling tank (10) back, vent (24) intercommunication has connecting pipe (25), the both ends of connecting pipe (25) all are provided with motorised valve (26).
5. The apparatus for chemical distillation purification according to claim 1, wherein: and heat dissipation pits (27) are formed in the periphery of the condensation chamber (11), and the number of the heat dissipation pits (27) is a plurality of.
6. The apparatus for chemical distillation purification according to claim 1, wherein: the surface of stirring leaf (6) is fixedly connected with tooth piece (28), a plurality of through-holes (29) of even size have been seted up in the front of stirring leaf (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321038522.1U CN219983928U (en) | 2023-04-26 | 2023-04-26 | Equipment for chemical distillation and purification |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321038522.1U CN219983928U (en) | 2023-04-26 | 2023-04-26 | Equipment for chemical distillation and purification |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219983928U true CN219983928U (en) | 2023-11-10 |
Family
ID=88606580
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321038522.1U Active CN219983928U (en) | 2023-04-26 | 2023-04-26 | Equipment for chemical distillation and purification |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219983928U (en) |
-
2023
- 2023-04-26 CN CN202321038522.1U patent/CN219983928U/en active Active
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| GR01 | Patent grant | ||
| GR01 | Patent grant |