Fractionating tower for refining chlorocyclohexane
By introducing movable scraper and nozzle into the fractionation column, efficient cleaning and heating uniformity of the inner wall of the fractionation column is achieved, and the problems of impurities accumulation and uneven stirring in the prior art are solved, which reduces wear and simplifies the structure , improves fractionation efficiency and convenience of use.
Patent Information
- Application Number
- CN202420973149.7
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-05-07
- Publication Date
- 2025-01-03
- Estimated Expiration
- 2034-05-07
AI Technical Summary
The existing fractionation towers are difficult to clean after use, and the uneven stirring during fractionation process leads to low efficiency, and complex structure increases wear and maintenance difficulty.
A fractionation tower consisting of a movable scraper and nozzle is designed. By driving the motor to drive the gears and scrapers to rotate, pressurized water to push the piston and scrapers to clean the inner wall of the fractionation tower, and back-flushing is performed through the nozzle and nozzle. Simplify the structure and avoid long-term contact between the scraper and the fractionation tower.
Improves the cleaning efficiency and heating uniformity of the fractionation column, reduces wear, extends service life, and simplifies the structure for easy maintenance.
Smart Images

Figure CN222286432U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of chlorocyclohexane fractionation, in particular to a fractionation tower used for refining chlorocyclohexane. Background Art
[0002] Chlorocyclohexane is a chemical with the molecular formula C6H11Cl. It is a colorless liquid with a suffocating odor. It is insoluble in water but soluble in ethanol. It is used as a pharmaceutical intermediate and is used to prepare the anti-epileptic and anti-convulsant drug benzhexol hydrochloride. Chlorocyclohexane can be obtained by the cyclohexanol chlorination method. When using the cyclohexanol chlorination method to produce chlorocyclohexane, it needs to undergo a distillation operation, and can be produced using a traditional distillation tower.
[0003] After searching, it was found that the publication number is CN219897098U, and the name is a distillation tower. The application proposes that after the existing distillation tower is used, a lot of impurities will accumulate on the inner wall, which is inconvenient to clean the inner wall, and a lot of impurities will accumulate on the inner walls of multiple oil outlet pipes on one side of the distillation tower, which is difficult to clean. The half-face gear is driven by the starting motor to rotate, and then the L-shaped rod and the scraper are driven to rotate. When the detergent scraper rotates, the inner wall of the distillation tower body can be cleaned, and the L-shaped rod can wipe the bottom of the distillation tower body. When the half-face gear rotates, it will drive the gear ring to move back and forth, and then drive the cleaning rod to move back and forth. Movement, when the cleaning rod moves, it can be inserted into the oil outlet pipe to clean the inner wall of the oil outlet pipe. However, when the application is in use, if it is not rotated during distillation, the fraction cannot be stirred, and uneven heating is likely to occur, affecting the distillation efficiency. If it is rotated during distillation, although it can play a stirring role, it will aggravate the wear of the scraper and the inner wall of the distillation tower. The scraper is in contact with the inner wall of the distillation tower body for a long time, affecting the life of the distillation tower body. It is impossible to ensure the uniformity of heating while reducing wear, and further improvements can be made. At the same time, the application adopts a complex reciprocating gear meshing structure, the structure is relatively complex, and further improvements can be made.
[0004] Currently, no effective solution has been proposed for the problems in the related technologies. Utility Model Content
[0005] 1. Technical issues to be resolved
[0006] In view of the deficiencies in the prior art, the utility model provides a distillation tower for refining chlorocyclohexane, which has the advantages of reducing wear, improving work efficiency and convenience of use, and simplifying the structure, thereby solving the problems in the above-mentioned background technology.
[0007] (II) Technical solution
[0008] In order to achieve the above advantages of reducing wear, improving work efficiency and convenience of use, and simplifying the structure, the specific technical solutions adopted by the utility model are as follows:
[0009] A fractionating tower for refining chlorocyclohexane comprises a fractionating tower body and a water tank, wherein a main shaft tube is rotatably connected to the top surface of the fractionating tower body, and a shunt pipe is rotatably connected to the surface of the main shaft tube located inside the fractionating tower body, and a piston is slidably connected to the shunt pipe, and a guide rod is fixedly connected to the other end of the piston, and a scraper is fixedly connected to the other end of the guide rod, an oil outlet pipe is rotatably connected to the surface of one side of the fractionating tower body, and a water tank is installed on one side of the fractionating tower body, and a dual-purpose water pump for pumping and draining is fixedly installed on the top surface of the water tank, a water pipe is rotatably connected to the output end of the dual-purpose water pump for pumping and draining, and the other end of the water pipe is rotatably connected to the main shaft tube through a water rotary connector, and a driven gear is fixedly sleeved on the outer surface of the top of the main shaft tube, a driving motor is fixedly installed on the top surface of the fractionating tower body, and a driving gear is installed on the output end of the driving motor, and the driving gear is meshed with the driven gear, a nozzle is rotatably connected to the outer surface of the main shaft tube corresponding to the height of the oil outlet pipe, and a nozzle is rotatably connected to the other end of the nozzle.
[0010] Furthermore, a sewage pipe is connected through the bottom surface of the distillation tower body, and a switch valve is installed on the surface of the sewage pipe.
[0011] Furthermore, a valve is installed on the surface of the water pipe.
[0012] Furthermore, the diverter pipes and guide rods are arranged obliquely, and there are multiple groups of diverter pipes and guide rods distributed from top to bottom.
[0013] Furthermore, a one-way valve is installed on the surface of the nozzle, and the installation direction of the one-way valve is the direction in which water flows out of the nozzle.
[0014] Furthermore, a feed inlet is connected through the top surface of the distillation tower body, and a sealing cover is installed on the top surface of the feed inlet.
[0015] Furthermore, the input end of the dual-purpose water pump for extraction and drainage is connected to the inside of the water tank through a water suction pipe.
[0016] (III) Beneficial effects
[0017] Compared with the prior art, the utility model provides a fractionation tower for refining chlorocyclohexane, which has the following beneficial effects:
[0018] (1) The utility model adopts a movable scraper. Chlorocyclohexane is fractionated inside the main body of the distillation tower. The fractionated components flow out along the oil outlet pipe. After the fractionation is completed, when it is necessary to clean the main body of the distillation tower, the driving motor and the dual-purpose water pump for pumping and discharging can be started to extract water from the water tank. The driving motor drives the driving gear to rotate, thereby driving the driven gear to rotate, thereby driving the main shaft pipe to rotate. The dual-purpose water pump for pumping and discharging draws water from the water tank through the water pipe and injects it into the main shaft pipe. The pressurized water enters the diversion pipe, pushing the piston to move, thereby pushing the scraper to abut against the inner wall of the main body of the distillation tower. The inner wall of the main body of the distillation tower is scraped and cleaned by the rotation of the scraper, which is convenient for cleaning the inner wall of the main body of the distillation tower and improves the cleaning efficiency. After cleaning, start the dual-purpose water pump to extract the water inside the main shaft pipe, reset the piston, and pull the scraper away from the main body of the distillation tower to avoid long-term scraping against the inner wall of the main body of the distillation tower and causing wear. This makes it easier for the main shaft pipe to rotate during distillation to drive the diverter pipe and the guide rod to rotate to stir the chlorocyclohexane fraction, thereby improving the uniformity of heating and the distillation efficiency. The device stirs during the distillation process to improve the uniformity of heating and the distillation efficiency. During the heating and stirring process, the scraper does not contact the main body of the distillation tower, thereby reducing wear and extending the service life. At the same time, the scraper can also scrape the inner wall of the main body of the distillation tower during the cleaning process, thereby improving the cleaning efficiency, enriching the use function, and improving work efficiency.
[0019] (2) The utility model adopts a nozzle and a nozzle. When water is injected into the main shaft pipe, a part of the pressurized water enters the nozzle and is sprayed out along the nozzle to spray water on the inner wall of the distillation tower body, thereby further improving the cleaning efficiency. At the same time, the nozzle and the oil outlet pipe are located at the same height. During the rotation of the nozzle, the nozzle can spray water into the inside of the oil outlet pipe for backwashing and simultaneously clean the inside of the oil outlet pipe. Compared with the complex gear reciprocating structure, the structure of the device is simpler and more convenient to use. BRIEF DESCRIPTION OF THE DRAWINGS
[0020] In order to more clearly illustrate the embodiments of the utility model or the technical solutions in the prior art, the drawings required for use in the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments of the utility model. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying creative work.
[0021] Figure 1 This is a schematic diagram of the structure of a fractionation tower for refining chlorocyclohexane proposed by the utility model;
[0022] Figure 2 It is a schematic diagram of the internal structure of the distillation tower body proposed by the utility model;
[0023] Figure 3This is a front view of a fractionation tower for refining chlorocyclohexane proposed by the utility model;
[0024] Figure 4 It is a schematic diagram of the external structure of the main shaft tube proposed by the utility model.
[0025] In the figure:
[0026] 1. The main body of the distillation tower; 2. The oil outlet pipe; 3. The driving motor; 4. The driving gear; 5. The main shaft tube; 6. The driven gear; 7. The water rotary connector; 8. The feed port; 9. The diverter pipe; 10. The scraper; 11. The water pipe; 12. The piston; 13. The valve; 14. The guide rod; 15. The dual-purpose water pump for extraction and drainage; 16. The water tank; 17. The sewage pipe; 18. The nozzle; 19. The nozzle; 20. The one-way valve. DETAILED DESCRIPTION
[0027] To further illustrate each embodiment, the present invention provides drawings, which are part of the disclosure of the present invention and are mainly used to illustrate the embodiments. They can be used in conjunction with the relevant descriptions in the specification to explain the operating principles of the embodiments. With reference to these contents, ordinary technicians in the field should be able to understand other possible implementation methods and advantages of the present invention. The components in the figures are not drawn to scale, and similar component symbols are generally used to represent similar components.
[0028] According to an embodiment of the utility model, a fractionation tower for refining chlorocyclohexane is provided.
[0029] The present invention is now further described in conjunction with the accompanying drawings and specific implementation methods. Figure 1-4As shown, according to an embodiment of the utility model, a distillation tower for refining chlorocyclohexane includes a distillation tower body 1 and a water tank 16. A main shaft tube 5 is rotatably connected to the top surface of the distillation tower body 1, and the main shaft tube 5 is coaxially arranged with the distillation tower body 1. The main shaft tube 5 is rotatably connected to the distillation tower body 1 through a sealed bearing, and the surface of the main shaft tube 5 is located inside the distillation tower body 1 and is connected with a bypass pipe 9, and a piston 12 is slidably connected inside the bypass pipe 9, and the other end of the piston 12 is fixedly connected to a guide rod 14, and the other end of the guide rod 14 is fixedly connected to a scraper 10, and the scraper 10 is an L-shaped structure. An oil outlet pipe 2 is connected to the surface of one side of the distillation tower body 1, and a plurality of oil outlet pipes 2 are arranged from top to bottom, and a water tank 16 is installed on one side of the distillation tower body 1, and the water tank 16 A dual-purpose water pump 15 for pumping and draining is fixedly installed on the top surface, which is a common device. The output end of the dual-purpose water pump 15 is connected with a water pipe 11, and the other end of the water pipe 11 is connected with the main shaft pipe 5 through a water rotary connector 7 for rotation, which does not affect the rotation of the main shaft pipe 5. It is a common device, and a driven gear 6 is fixedly sleeved on the top outer surface of the main shaft pipe 5. A driving motor 3 is fixedly installed on the top surface of the distillation tower body 1, and a driving gear 4 is installed on the output end of the driving motor 3, and the driving gear 4 is meshed with the driven gear 6. A nozzle 19 is connected to the outer surface of the main shaft pipe 5 at a height corresponding to the oil outlet pipe 2, and a nozzle 18 is connected to the other end of the nozzle 19. Chlorocyclohexane is fractionated inside the distillation tower body 1, and the fractionated components flow out along the oil outlet pipe 2. After the fractionation is completed, it needs to be cleaned. When the distillation tower body 1 is in operation, the driving motor 3 and the dual-purpose water pump 15 can be started to extract water from the water tank 16. The driving motor 3 drives the driving gear 4 to rotate, thereby driving the driven gear 6 to rotate, and then driving the main shaft tube 5 to rotate. The dual-purpose water pump 15 extracts water from the water tank 16 and injects it into the main shaft tube 5 through the water pipe 11. The pressurized water enters the diverter pipe 9, pushing the piston 12 to move, thereby pushing the scraper 10 to abut against the inner wall of the distillation tower body 1. The inner wall of the distillation tower body 1 is scraped and cleaned by the rotation of the scraper 10, which is convenient for cleaning the inner wall of the distillation tower body 1 and improves the cleaning efficiency. After cleaning, the dual-purpose water pump 15 is started to extract the water inside the main shaft tube 5, the piston 12 is reset, and the scraper 10 is pulled away from the distillation tower body 1 to avoid long-term contact with the distillation tower body 1. The inner wall of the tower body 1 is scraped and worn, so that the main shaft tube 5 rotates to drive the diverter tube 9 and the guide rod 14 to rotate and stir the chlorocyclohexane fraction during distillation, thereby improving the uniformity of heating and the distillation efficiency. The device stirs during the distillation process to improve the uniformity of heating and the distillation efficiency, and the scraper 10 does not contact the distillation tower body 1 during the heating and stirring process, thereby reducing wear and extending the service life. At the same time, the scraper 10 can also scrape the inner wall of the distillation tower body 1 during the cleaning process, thereby improving the cleaning efficiency, enriching the use function, and improving the work efficiency. At the same time, when the main shaft tube 5 is filled with water, a part of the pressure water enters the nozzle 19 and is sprayed along the nozzle 18 to spray and rinse the inner wall of the distillation tower body 1, thereby further improving the cleaning efficiency. At the same time,The nozzle 19 and the oil outlet pipe 2 are located at the same height. During the rotation of the nozzle 19, the nozzle 18 can spray water into the oil outlet pipe 2 to perform backwash cleaning and simultaneously clean the inside of the oil outlet pipe 2. Compared with the complex gear reciprocating structure, the structure of this device is simpler and more convenient to use.
[0030] In one embodiment, a sewage pipe 17 is connected through the bottom surface of the distillation tower body 1, and a switch valve is installed on the surface of the sewage pipe 17 to facilitate sewage discharge.
[0031] In one embodiment, a valve 13 is installed on the surface of the water pipe 11 to facilitate opening and closing of the water pipe 11 .
[0032] In one embodiment, the shunt pipes 9 and the guide rods 14 are arranged obliquely, and there are multiple groups of shunt pipes 9 and guide rods 14 distributed from top to bottom, and the shunt pipes 9 and the guide rods 14 play a stirring role synchronously.
[0033] In one embodiment, a one-way valve 20 is installed on the surface of the nozzle 19 , and the one-way valve 20 is installed in the direction of water flowing out of the nozzle 18 to prevent the fractionated components from entering the nozzle 19 along the nozzle 18 .
[0034] In one embodiment, a feed port 8 is connected through the top surface of the fractionation tower body 1, and a sealing cover is installed on the top surface of the feed port 8 to facilitate feeding.
[0035] In one embodiment, the input end of the dual-purpose water pump 15 is connected to the inside of the water tank 16 through a suction pipe to facilitate water pumping and water return. This is a common structure and is not shown in detail in the figure.
[0036] Working principle:
[0037] Chlorocyclohexane is fractionated inside the fractionation tower body 1, and the fractionated components flow out along the oil outlet pipe 2. After the fractionation is completed, when the fractionation tower body 1 needs to be cleaned, the driving motor 3 and the dual-use pump 15 can be started to extract water from the water tank 16. The driving motor 3 drives the driving gear 4 to rotate, and then drives the driven gear 6 to rotate, and then drives the main shaft pipe 5 to rotate. The dual-use pump 15 extracts water from the water tank 16 and injects it into the main shaft pipe 5 through the water pipe 11. The pressurized water enters the diversion pipe 9. In the process, the piston 12 is pushed to move, and then the scraper 10 is pushed to abut against the inner wall of the fractionation tower body 1. The inner wall of the fractionation tower body 1 is scraped and cleaned by the rotation of the scraper 10, which is convenient for cleaning the inner wall of the fractionation tower body 1 and improving the cleaning efficiency. After the cleaning is completed, the dual-purpose water pump 15 is started to extract the water inside the main shaft pipe 5, and the piston 12 is reset to pull the scraper 10 away from the fractionation tower body 1 to avoid long-term scraping with the inner wall of the fractionation tower body 1 and causing wear, so as to facilitate the rotation of the main shaft pipe 5 during fractionation. The diverter pipe 9 and the guide rod 14 are driven to rotate to stir the chlorocyclohexane fraction, thereby improving the uniformity of heating and the efficiency of fractionation. The device stirs during the fractionation process to improve the uniformity of heating and the efficiency of fractionation. During the heating and stirring process, the scraper 10 does not contact the distillation tower body 1, thereby reducing wear and extending the service life. At the same time, the scraper 10 can also scrape the inner wall of the distillation tower body 1 during the cleaning process to improve the cleaning efficiency, enrich the use function, and improve the work efficiency. At the same time, when the main shaft tube 5 is injected with water, a part of the pressure water enters the nozzle 19 and is sprayed along the nozzle 18 to spray and flush the inner wall of the distillation tower body 1, thereby further improving the cleaning efficiency. At the same time, the nozzle 19 is located at the same height as the oil outlet pipe 2. During the rotation of the nozzle 19, the nozzle 18 can spray water into the inside of the oil outlet pipe 2 for backwashing and synchronously cleaning the inside of the oil outlet pipe 2. Compared with the complex gear reciprocating structure, the device has a simpler structure and is more convenient to use.
[0038] In the present utility model, unless otherwise clearly stipulated and limited, the terms such as "installation", "setting", "connection", "fixation" and "screw-on" should be understood in a broad sense. For example, it can be a fixed connection, a detachable connection, or an integrated connection; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediate medium, it can be the internal connection of two elements or the interaction relationship between two elements. Unless otherwise clearly defined, ordinary technicians in this field can understand the specific meanings of the above terms in the utility model according to the specific circumstances.
[0039] The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principles of the present invention should be included in the protection scope of the present invention.
Claims
1. A fractionation tower for refining chlorocyclohexane, characterized in that: The invention comprises a fractionation tower body (1) and a water tank (16), wherein a main shaft tube (5) is rotatably connected to the top surface of the fractionation tower body (1), and a shunt tube (9) is connected to the surface of the main shaft tube (5) located inside the fractionation tower body (1), and a piston (12) is slidably connected to the inside of the shunt tube (9), and a guide rod (14) is fixedly connected to the other end of the piston (12), and a scraper (10) is fixedly connected to the other end of the guide rod (14), and an oil outlet pipe (2) is connected to the surface of one side of the fractionation tower body (1), and a water tank (16) is installed on one side of the fractionation tower body (1), and a dual-purpose water pump (15) for pumping and exhausting is fixedly installed on the top surface of the water tank (16). ), the output end of the dual-purpose water pump (15) is connected to a water pipe (11), and the other end of the water pipe (11) is connected to the main shaft pipe (5) through a water rotary connector (7), and a driven gear (6) is fixedly sleeved on the top outer surface of the main shaft pipe (5), a driving motor (3) is fixedly installed on the top surface of the fractionation tower body (1), and a driving gear (4) is installed on the output end of the driving motor (3), and the driving gear (4) is meshed with the driven gear (6), and a nozzle (19) is connected to the outer surface of the main shaft pipe (5) at a height corresponding to the oil outlet pipe (2), and a nozzle (18) is connected to the other end of the nozzle (19).
2. A fractionation tower for refining chlorocyclohexane according to claim 1, characterized in that: A sewage pipe (17) is connected through the bottom surface of the distillation tower body (1), and a switch valve is installed on the surface of the sewage pipe (17).
3. A fractionation tower for refining chlorocyclohexane according to claim 1, characterized in that: A valve (13) is installed on the surface of the water delivery pipe (11).
4. A fractionation tower for refining chlorocyclohexane according to claim 1, characterized in that: The shunt pipes (9) and guide rods (14) are arranged obliquely, and there are multiple groups of shunt pipes (9) and guide rods (14) distributed from top to bottom.
5. A fractionation tower for refining chlorocyclohexane according to claim 1, characterized in that: A one-way valve (20) is installed on the surface of the nozzle (19), and the installation direction of the one-way valve (20) is the direction in which water flows out of the nozzle (18).
6. A fractionation tower for refining chlorocyclohexane according to claim 1, characterized in that: The top surface of the fractionation tower body (1) is connected through a feed inlet (8), and a sealing cover is installed on the top surface of the feed inlet (8).
7. A fractionation tower for refining chlorocyclohexane according to claim 1, characterized in that: The input end of the dual-purpose water pump (15) is connected to the interior of the water tank (16) via a water suction pipe.
Citation Information
Patent Citations
Fractionating tower
CN219897098U