CN221155407U - Organic silicon liquid distillation device - Google Patents
Organic silicon liquid distillation device Download PDFInfo
- Publication number
- CN221155407U CN221155407U CN202322744653.8U CN202322744653U CN221155407U CN 221155407 U CN221155407 U CN 221155407U CN 202322744653 U CN202322744653 U CN 202322744653U CN 221155407 U CN221155407 U CN 221155407U
- Authority
- CN
- China
- Prior art keywords
- treatment
- cooling
- cylinder
- output
- processing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000004821 distillation Methods 0.000 title claims abstract description 43
- 239000007788 liquid Substances 0.000 title claims abstract description 37
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 title abstract description 24
- 229910052710 silicon Inorganic materials 0.000 title abstract description 24
- 239000010703 silicon Substances 0.000 title abstract description 24
- 238000001816 cooling Methods 0.000 claims description 77
- 238000012545 processing Methods 0.000 claims description 61
- 238000010438 heat treatment Methods 0.000 claims description 20
- 238000004140 cleaning Methods 0.000 claims description 16
- 229920001296 polysiloxane Polymers 0.000 claims description 16
- 239000004065 semiconductor Substances 0.000 claims description 13
- 239000012530 fluid Substances 0.000 claims description 11
- 230000008878 coupling Effects 0.000 claims description 6
- 238000010168 coupling process Methods 0.000 claims description 6
- 238000005859 coupling reaction Methods 0.000 claims description 6
- 238000009434 installation Methods 0.000 claims description 2
- 230000000712 assembly Effects 0.000 claims 2
- 238000000429 assembly Methods 0.000 claims 2
- 230000000694 effects Effects 0.000 abstract description 9
- 239000002245 particle Substances 0.000 abstract description 6
- 239000013078 crystal Substances 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract 1
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 22
- 235000017491 Bambusa tulda Nutrition 0.000 description 22
- 241001330002 Bambuseae Species 0.000 description 22
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 22
- 239000011425 bamboo Substances 0.000 description 22
- 239000000243 solution Substances 0.000 description 8
- 238000007790 scraping Methods 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 230000003993 interaction Effects 0.000 description 4
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 239000000839 emulsion Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000005057 refrigeration Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000002178 crystalline material Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses an organic silicon liquid distillation device, which comprises a treatment cylinder, wherein one end of the treatment cylinder is provided with a treatment component, one end of the treatment component extends from one end of the treatment cylinder to the other end of the treatment cylinder, the top of the treatment cylinder is connected with a feed pipe, and the treatment cylinder can be internally and externally heated, so that the treatment cylinder can be contained in distillation efficiency and the inner wall of the treatment cylinder can be cleaned, crystalline substances can be prevented from adhering, and meanwhile, through the mutual matching with an auxiliary component, crystal particles after distillation can be output after the distillation is finished, so that the subsequent treatment effect is ensured.
Description
Technical Field
The utility model relates to the technical field of organosilicon liquid processing, in particular to an organosilicon liquid distillation device.
Background
The silicone emulsion (abbreviated as silicone emulsion) is an emulsion composed of oil-in-water type silicone oil, water, a surfactant, and the like, and when the silicone liquid is distilled, a silicone liquid distillation apparatus is required.
Through retrieving organosilicon liquid distillation plant that chinese patent publication CN 214913453U discloses, can the organosilicon liquid in the regular container of different height be carried to the device body inside, and carry out quick cooling to the gas that distills in the outlet duct, improve work efficiency, the scraper blade rotation axis on the utility model can clear up the liquid that remains on the device body inner wall, and has certain stirring effect to organosilicon liquid, improves distillation efficiency, collet convenient to detach and installation, conveniently clear up the impurity and the waste residue that leave in the collet.
However, the above patent has a certain disadvantage in practical use, and in use, although the distillation efficiency of the organosilicon liquid can be improved, the condensation efficiency of the gaseous organosilicon is lower in the condensation treatment, and the liquid organosilicon in condensation has one end impurity, so that the distillation purity of the organosilicon liquid is lower.
For the problems in the related art, no effective solution has been proposed at present.
Disclosure of utility model
(One) solving the technical problems
Aiming at the defects of the prior art, the utility model provides the organic silicon liquid distillation device which has the advantages of the technical problems, thereby solving the problems in the prior art.
(II) technical scheme
In order to realize the advantages of the technical problems, the utility model adopts the following specific technical scheme:
the utility model provides an organosilicon liquid distillation plant, includes a processing section of thick bamboo, processing section of thick bamboo one end is equipped with the processing subassembly, and processing subassembly one end extends to the processing section of thick bamboo other end by processing section of thick bamboo one end, and processing section of thick bamboo top is connected with the inlet pipe, and processing section of thick bamboo outer wall both sides are connected with cooling module, and cooling module is linked together with processing section of thick bamboo is inside, and processing section of thick bamboo inner wall one end sets up temperature sensor.
Further, for better assurance organosilicon liquid treatment effeciency, the processing subassembly includes first motor, and first motor passes through the bolt mounting and handles a section of thick bamboo one end, and first motor output has the dwang through the coupling joint, and dwang one end is provided with the processing blade by handling a section of thick bamboo outside extension to handling a section of thick bamboo inside, dwang outer wall, and the processing blade is crisscross setting.
Further, in order to better guarantee organic silicon liquid distillation efficiency, the first chamber of placing is offered at processing blade middle part, and the first intracavity of placing is provided with first heating pipe, and the chamber is placed to the second of seting up in processing section of thick bamboo middle part, and the intracavity is placed to the second is provided with the second heating pipe.
Further, in order to better guarantee the cleaning effect of the inner wall of the treatment cylinder, a cleaning scraping plate is arranged on one side of the treatment blade, cleaning brushes are arranged on two sides of the cleaning scraping plate, an auxiliary part is arranged at one end of the rotating rod, and an auxiliary part is arranged at one end of the bottom of the treatment cylinder.
Further, in order to better guarantee that solid particles that organosilicon liquid distillation produced are exported, auxiliary component includes output blade, and output blade sets up in dwang one end, is provided with first output under the output blade and fights, and first output fights to connect in handling a section of thick bamboo one end, and first output fights one end and is provided with the output tube, and output tube one end is equipped with the second and exports fights.
Further, in order to better guarantee output effect, the second output hopper is inside to be provided with the second motor through the support frame, and the second motor output is connected with helical blade through the shaft coupling.
Further, for better assurance organosilicon liquid distillation cooling effect, the cooling module includes the cooling treatment tube, and cooling treatment tube connects in handling a section of thick bamboo outer wall both sides, and cooling treatment tube outer wall is provided with the cooling tube, and one of them end of cooling tube is provided with miniature delivery pump, and the cooling tube both ends are connected with the cooling tank, and the cooling tank setting is in handling a section of thick bamboo outer wall one side, and the semiconductor refrigeration piece is installed to the cooling tank both sides, and the conduction board is installed to semiconductor refrigeration piece one side, and conduction board one side extends to the cooling tank inside by cooling tank one side.
Further, for better assurance distillation gaseous organosilicon conveying effect and organosilicon body edulcoration effect's advantage, cooling module still includes the storage section of thick bamboo, and the storage section of thick bamboo is installed in cooling treatment pipe one end, and cooling treatment pipe is linked together with the storage section of thick bamboo, and cooling treatment pipe one end is provided with the direction cover, and the direction cover is inside to be provided with the conveyor fan through the mounting bracket, is provided with a plurality of filter screens under the conveyor fan, and storage section of thick bamboo one side is provided with the drain pipe.
(III) beneficial effects
Compared with the prior art, the utility model has the following beneficial effects: through setting up processing component, be convenient for carry out distillation processing at organosilicon liquid, can carry out internal and external heating to processing section of thick bamboo, thereby can contain and can also clear up processing section of thick bamboo inner wall at distillation efficiency, and then avoid crystalline material to adhere to, simultaneously through mutually supporting with auxiliary assembly, can export the crystallization granule after the distillation, thereby guarantee follow-up treatment effect, be convenient for through setting up cooling module at organosilicon liquid distillation in-process, can collect gasified organosilicon from processing section of thick bamboo both sides, thereby guarantee distillation collection effect, and can also carry out multiple times filtration with gaseous organosilicon that converts into liquid, and then can guarantee distilled organosilicon's purity, help guaranteeing the result of use of distillation.
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 embodiments will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present utility model, and other drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
FIG. 1 is a schematic view of a silicone fluid distillation apparatus according to an embodiment of the present utility model;
FIG. 2 is a schematic view showing a bottom view of a silicone liquid distillation apparatus according to an embodiment of the present utility model;
FIG. 3 is a schematic cross-sectional structural view of a silicone fluid distillation apparatus processing assembly in accordance with an embodiment of the present utility model;
FIG. 4 is a schematic view showing a partial structure of a processing assembly of a silicone fluid distillation apparatus according to an embodiment of the present utility model;
FIG. 5 is a schematic view showing a structure of a cooling module of a liquid distillation apparatus for organic silicon according to an embodiment of the present utility model;
Fig. 6 is a schematic structural view of an auxiliary component of a silicone fluid distillation apparatus according to an embodiment of the present utility model.
In the figure:
1. A treatment cylinder; 2. a processing assembly; 201. a first motor; 202. a rotating lever; 203. treating the blade; 204. a first heating pipe; 205. a second heating pipe; 206. an auxiliary member; 2061. an output blade; 2062. a first output hopper; 2063. an output pipe; 2064. a second output hopper; 2065. a second motor; 2066. a helical blade; 3. a feed pipe; 4. a cooling assembly; 401. a cooling treatment tube; 402. a cooling tube; 403. a micro-delivery pump; 404. a cooling box; 405. a semiconductor refrigeration sheet; 406. a conductive plate; 407. a storage cylinder; 408. a guide cover; 409. a conveying fan; 410. a filter screen; 5. a first placement cavity; 6. a second placement cavity; 7. cleaning a scraping plate; 8. cleaning a hairbrush; 9. a drain pipe; 10. a temperature sensor.
Detailed Description
For the purpose of further illustrating the concepts of the utility model, there is provided in the drawings, which are a part of the disclosure of the present utility model and are primarily intended to illustrate embodiments and, together with the description, serve to explain the principles of the embodiments, with reference to these, it will be understood by those skilled in the art that other possible embodiments and advantages of the utility model may be made, the components in the drawings not being drawn to scale, and that like reference numerals will generally be used to designate like components.
Referring to fig. 1-6, a distillation apparatus for organic silicon liquid according to an embodiment of the present utility model includes a processing cylinder 1 having a cylindrical structure, a processing component 2 is disposed at one end of the processing cylinder 1 for performing distillation processing on the organic silicon liquid, one end of the processing component 2 extends from one end of the processing cylinder 1 to the other end of the processing cylinder 1, a feeding pipe 3 is connected to the top of the processing cylinder 1, the feeding pipe 3 is electrically connected to an external metering pump in actual use, cooling components 4 are connected to two sides of an outer wall of the processing cylinder 1 for condensing distilled gaseous organic silicon, the cooling components 4 are communicated with the inside of the processing cylinder 1, a temperature sensor 10 is disposed at one end of an inner wall of the processing cylinder 1 for monitoring an internal temperature of the processing cylinder 1, and the temperature sensor 10 is electrically connected to an external controller and an external power supply in actual use.
As shown in fig. 1-6, the processing assembly 2 includes a first motor 201, the first motor 201 is mounted at one end of the processing cylinder 1 through a bolt, the output end of the first motor 201 is connected with a rotating rod 202 through a coupling, one end of the rotating rod 202 extends from the outside of the processing cylinder 1 to the inside of the processing cylinder 1, three groups of processing blades 203 are arranged on the outer wall of the rotating rod 202, four processing blades 203 are arranged on each group, the processing blades 203 and the rotating rod 202 are arranged in an integrated structure, the processing blades 203 are staggered, two groups of processing blades 203 are located in the same direction, a first placing cavity 5 is arranged in the middle of the processing blades 203, a first heating pipe 204 in an S-shaped structure is arranged in the first placing cavity 5, a second placing cavity 6 is arranged in the middle of the processing cylinder 1, a second heating pipe 205 in an S-shaped structure is arranged in the second placing cavity 6, a cleaning scraper 7 is arranged on one side of the processing blades 203, a cleaning scraper 8 is arranged on two sides of the cleaning scraper 7, an auxiliary part 206 is arranged on one end of the rotating rod 202, and the auxiliary part 206 is arranged at one end of the bottom of the processing cylinder 1, and in actual use, the first motor, the first heating pipe 204, the second heating pipe 204 and the second heating pipe are electrically connected with an external power supply.
Specifically, when the organic silicon liquid needs to be distilled, the organic silicon liquid is conveyed into the treatment cylinder 1 through the interaction of the external metering pump and the feeding pipe 3, then the first motor 201 is started and the first heating pipe 204 and the second heating pipe 205 are started through the external controller, then the output end of the first motor 201 drives the rotating rod 202 and the treatment blade 203 to rotate, the organic silicon liquid in the treatment cylinder 1 is distilled through the interaction of the rotating rod 202 and the first heating pipe 204 and the second heating pipe 205, the inner wall of the treatment cylinder 1 can be cleaned through the interaction of the cleaning scraping plate 7 and the cleaning brush 8 in the rotation process of the rotating rod 202, and therefore the phenomenon that the crystallization position is attached to the inner wall of the treatment cylinder 1 in the distillation process of the organic silicon liquid is avoided.
As shown in fig. 1-6, the cooling component 4 comprises a cooling treatment tube 401 with an L-shaped structure, the cooling treatment tube 401 is connected to two sides of the outer wall of the treatment cylinder 1, the outer wall of the cooling treatment tube 401 is provided with a cooling tube 402, one end of the cooling tube 402 is provided with a micro-delivery pump 403, two ends of the cooling tube 402 are connected with a cooling box 404, the solution in the cooling box 404 is aqueous solution, a water level observation port and a filling port are arranged on one side and one end of the outer wall of the cooling box 404 for observing the solution in actual use, the cooling box 404 is arranged on one side of the outer wall of the treatment cylinder 1 through a mounting frame, semiconductor refrigerating pieces 405 are arranged on two sides of the cooling box 404, the types of the semiconductor refrigerating pieces 405 are TEC1-24106, in actual use, a conducting plate 406 is arranged on one side of the semiconductor refrigerating pieces 405, the conducting plate 406 is made of copper metal with good conductivity, the surface of the conducting plate 406 is equidistantly separated from the cooling holes arranged on one side of the cooling box 404, and the conducting plate 406 extends into the cooling box 404;
The cooling module 4 further comprises a storage cylinder 407 in a cylindrical structure, the storage cylinder 407 is arranged at one end of the cooling treatment pipe 401, the cooling treatment pipe 401 is communicated with the storage cylinder 407 and the cooling box 404, a guide cover 408 in a round table-shaped structure is arranged at one end of the cooling treatment pipe 401, a conveying fan 409 is arranged inside the guide cover 408 through a mounting frame, a waterproof treatment is arranged on the conveying fan 409 in actual use, three filter screens 410 are arranged under the conveying fan 409, a drain pipe 9 is arranged on one side of the storage cylinder 407, and the micro conveying pump 403, the semiconductor refrigerating sheet 405 and the conveying fan 409 are electrically connected with an external controller and an external power supply in actual use, and a control valve is arranged at one end of the drain pipe 9.
Specifically, when the organic silicon is distilled to generate a gas state, the micro-pump 403, the conveying fan 409 and the semiconductor refrigerating sheet 405 are started by the external controller, then the conveying fan 409 rotates to form a low-pressure area and a high-pressure area, the low-pressure area sucks the gaseous organic silicon in the treatment cylinder 1 into the cooling treatment tube 401, the sucked gaseous organic silicon circularly flows through the micro-pump 403, the cooling tube 402, the cooling box 404 and the semiconductor refrigerating sheet 405 and the conducting plate 406 to cool the surface of the cooling treatment tube 401 by the cooling solution in the cooling box 404, so that the gaseous organic silicon is converted into a liquid state, then the organic silicon converted into the liquid state is guided and discharged through the guide cover 408 in the high-pressure area, then filtered through the three filter screens 410 and then discharged through the drain tube 9, and the purity of the organic silicon distillation can be ensured.
As shown in fig. 1 to 6, the auxiliary member 206 includes an output blade 2061, the output blade 2061 is disposed at one end of the rotating rod 202, a first output bucket 2062 having a circular truncated cone structure is disposed under the output blade 2061, the first output bucket 2062 is connected to one end of the processing cylinder 1, an output pipe 2063 is disposed at one end of the first output bucket 2062, a control valve is disposed at one end of the output pipe 2063 in actual use, a second output bucket 2064 having a circular truncated cone structure is disposed at one end of the output pipe 2063, a second motor 2065 is disposed inside the second output bucket 2064 via a support frame, an output end of the second motor 2065 is connected to a screw blade 2066 via a coupling, and the second motor 2065 is electrically connected to an external controller and an external power supply in actual use.
Specifically, after the distillation is completed, the first motor 201 and the second motor 2065 are started by the external controller, then the output end of the first motor 201 drives the rotating rod 202 and the output blade 2061 to rotate, so that the distilled and crystallized particles are conveyed into the first output hopper 2062, then the output end of the second motor 2065 drives the spiral blade 2066 to rotate, and then the crystallized particles in the first output hopper 2062 are conveyed into the output pipe 2063, and then are guided to be discharged by the second output hopper 2064.
In order to facilitate understanding of the above technical solutions of the present utility model, the following describes in detail the working principle or operation manner of the present utility model in the actual process.
Working principle: in summary, by means of the above technical solution of the present utility model, when the distillation treatment is required to be performed on the silicone fluid, the silicone fluid is delivered to the inside of the treatment cylinder 1 through the cooperation of the external metering pump and the feed pipe 3, then the first motor 201 is started and the first heating pipe 204 and the second heating pipe 205 are started by the external controller, then the output end of the first motor 201 drives the rotating rod 202 and the treatment blade 203 to rotate, the distillation treatment is performed on the silicone fluid in the treatment cylinder 1 through the cooperation of the rotating rod 202 with the first heating pipe 204 and the second heating pipe 205, the inner wall of the treatment cylinder 1 can be cleaned through the cooperation of the cleaning scraping plate 7 and the cleaning brush 8 during the rotation of the rotating rod 202, so that the crystal position is prevented from adhering to the inner wall of the treatment cylinder 1 during the distillation process of the silicone fluid, and when the distillation of the silicone fluid generates a gaseous state, the micro-delivery pump 403, the delivery fan 409 and the semiconductor refrigerating sheet 405 are started by an external controller, then the delivery fan 409 rotates to form a low pressure area and a high pressure area, the low pressure area sucks the gaseous organic silicon in the treatment cylinder 1 into the cooling treatment pipe 401, the sucked gaseous organic silicon circularly flows with the cooling solution in the cooling tank 404 through the micro-delivery pump 403, the cooling tank 404 and the semiconductor refrigerating sheet 405 and the conducting plate 406 to cool the surface of the cooling treatment pipe 401, so that the gaseous organic silicon is converted into a liquid state, then the organic silicon converted into the liquid state is guided and discharged through the guide cover 408 through the high pressure area, then filtered through the three filter screens 410 and then discharged through the drain pipe 9, thereby ensuring the purity of the organic silicon distillation, the first motor 201 and the second motor 2065 are started by an external controller, then the output end of the first motor 201 drives the rotating rod 202 and the output blade 2061 to rotate, so that the distilled and crystallized particles are conveyed into the first output hopper 2062, then the output end of the second motor 2065 drives the spiral blade 2066 to rotate, and then the crystallized particles in the first output hopper 2062 are conveyed into the output pipe 2063, and then are guided and discharged through the second output hopper 2064.
In the present utility model, unless explicitly specified and limited otherwise, the terms "mounted," "configured," "connected," "secured," "screwed," and the like are to be construed broadly and may be, for example, fixedly connected, detachably connected, or integrally formed; can be mechanically or electrically connected; either directly or indirectly through intermediaries, or in communication with each other or in interaction with each other, unless explicitly defined otherwise, the meaning of the terms described above in this application will be understood by those of ordinary skill in the art in view of the specific circumstances.
The foregoing description of the preferred embodiments of the utility model is not intended to be limiting, but rather is intended to cover all modifications, equivalents, alternatives, and improvements that fall within the spirit and scope of the utility model.
Claims (6)
1. An organosilicon liquid distillation device, comprising a treatment cylinder (1), characterized in that: one end of the treatment cylinder (1) is provided with a treatment assembly (2), one end of the treatment assembly (2) extends from one end of the treatment cylinder (1) to the other end of the treatment cylinder (1), the top of the treatment cylinder (1) is connected with a feeding pipe (3), two sides of the outer wall of the treatment cylinder (1) are connected with cooling assemblies (4), the cooling assemblies (4) are communicated with the inside of the treatment cylinder (1), and one end of the inner wall of the treatment cylinder (1) is provided with a temperature sensor (10);
The cooling assembly (4) comprises cooling treatment pipes (401), the cooling treatment pipes (401) are connected to two sides of the outer wall of the treatment cylinder (1), the cooling pipes (402) are arranged on the outer wall of the cooling treatment pipes (401), a micro conveying pump (403) is arranged at one end of each cooling pipe (402), cooling boxes (404) are connected to two ends of each cooling pipe (402), the cooling boxes (404) are arranged on one side of the outer wall of the treatment cylinder (1), semiconductor refrigerating sheets (405) are arranged on two sides of each cooling box (404), a conducting plate (406) is arranged on one side of each semiconductor refrigerating sheet (405), and one side of each conducting plate (406) extends from one side of each cooling box (404) to the inside of each cooling box (404);
The cooling assembly (4) further comprises a storage cylinder (407), the storage cylinder (407) is arranged at one end of the cooling treatment pipe (401), the cooling treatment pipe (401) is communicated with the storage cylinder (407), a guide cover (408) is arranged at one end of the cooling treatment pipe (401), a conveying fan (409) is arranged inside the guide cover (408) through an installation frame, a plurality of filter screens (410) are arranged under the conveying fan (409), and a drain pipe (9) is arranged at one side of the storage cylinder (407).
2. The device according to claim 1, wherein the processing assembly (2) comprises a first motor (201), the first motor (201) is mounted at one end of the processing cylinder (1) through a bolt, the output end of the first motor (201) is connected with a rotating rod (202) through a coupling, one end of the rotating rod (202) extends from the outside of the processing cylinder (1) to the inside of the processing cylinder (1), processing blades (203) are arranged on the outer wall of the rotating rod (202), and the processing blades (203) are arranged in an staggered mode.
3. An organosilicon liquid distillation apparatus according to claim 2, wherein a first placing cavity (5) is provided in the middle of the processing blade (203), a first heating pipe (204) is provided in the first placing cavity (5), a second placing cavity (6) is provided in the middle of the processing cylinder (1), and a second heating pipe (205) is provided in the second placing cavity (6).
4. A silicone fluid distillation apparatus as claimed in claim 3, wherein a cleaning blade (7) is provided on one side of the processing blade (203), cleaning brushes (8) are provided on both sides of the cleaning blade (7), an auxiliary member (206) is provided on one end of the rotating lever (202), and the auxiliary member (206) is partially provided on one end of the bottom of the processing cylinder (1).
5. The device according to claim 4, wherein the auxiliary member (206) comprises an output blade (2061), the output blade (2061) is disposed at one end of the rotating rod (202), a first output hopper (2062) is disposed under the output blade (2061), the first output hopper (2062) is connected to one end of the processing cylinder (1), an output pipe (2063) is disposed at one end of the first output hopper (2062), and a second output hopper (2064) is disposed at one end of the output pipe (2063).
6. A device for distilling a silicone fluid according to claim 5, wherein the second output hopper (2064) is internally provided with a second motor (2065) through a support frame, and the output end of the second motor (2065) is connected with a spiral blade (2066) through a coupling.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322744653.8U CN221155407U (en) | 2023-10-13 | 2023-10-13 | Organic silicon liquid distillation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322744653.8U CN221155407U (en) | 2023-10-13 | 2023-10-13 | Organic silicon liquid distillation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221155407U true CN221155407U (en) | 2024-06-18 |
Family
ID=91458974
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322744653.8U Active CN221155407U (en) | 2023-10-13 | 2023-10-13 | Organic silicon liquid distillation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221155407U (en) |
-
2023
- 2023-10-13 CN CN202322744653.8U patent/CN221155407U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN221155407U (en) | Organic silicon liquid distillation device | |
| CN216571585U (en) | Constant-temperature circulating distillation device for producing beer | |
| CN113976001B (en) | Hydrogen storage material canning and recycling device and recycling method for hydrogen storage tank | |
| CN115999179A (en) | Natural hexanoic acid purification equipment | |
| CN213556595U (en) | Thermal technology device for polydextrose production | |
| CN212236024U (en) | Environment-friendly chemical distillation plant | |
| CN216323734U (en) | Raw materials belt cleaning device is used in rice wine processing | |
| CN220265338U (en) | Distillation plant is used in industry spent acid treatment | |
| CN215975719U (en) | Biofuel refines production facility | |
| CN220070742U (en) | Plant extract purifying device | |
| CN214971798U (en) | Prevent levogyration carnitine production of caking and use concentrated jar | |
| CN219744758U (en) | Organosilicon schizolysis material recovery processing device | |
| CN217437793U (en) | Low-temperature vacuum evaporator capable of being rapidly preheated | |
| CN218741920U (en) | Oligosaccharide desalination enrichment facility of plant source | |
| CN221206831U (en) | Liquid negative pressure low-temperature distillation equipment | |
| CN211050939U (en) | Continuous rectification device for recovering propylene glycol and dipropylene glycol from waste liquid | |
| CN217773271U (en) | Automatic chinese mugwort grass liquid extraction element of feeding | |
| CN220834230U (en) | Reflux extraction device | |
| CN217340167U (en) | Circulating decoloration device of glycerine production usefulness | |
| CN220555658U (en) | Industrial circulating cooling water descaling equipment | |
| CN220676804U (en) | Chemical distillation device | |
| CN220047830U (en) | New energy battery silicon negative electrode raw material concentration device | |
| CN219880862U (en) | Milk storage tank's belt cleaning device is used in dairy products processing | |
| CN220012216U (en) | Concentrated evaporating kettle with pretreatment function | |
| CN215352416U (en) | Preparation barium sulfonate uses high-efficient refining plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant |