Raw material distiller for chemical industry

By designing a multi-stage distillation zone and a chemical raw material distiller equipped with a stirring device and pressure regulator, the problem of multi-stage distillation in the prior art is solved, efficient separation and production of high-purity products are achieved, and energy consumption and environmental impact are reduced.

CN222623688UActive Publication Date: 2025-03-18TANGSHAN BAOXIANG CHEM PROD CO LTD
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Patent Information

Application Number
CN202420582632.2
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-03-25
Publication Date
2025-03-18
Estimated Expiration
2034-03-25

AI Technical Summary

Technical Problem

The existing chemical distillation technology cannot perform multi-stage distillation, resulting in the inability to effectively separate different components in the mixture, thereby limiting the distillation efficiency and product purity.

Method used

A chemical raw material distiller including primary, secondary and tertiary distillation zones is designed, and the interoperability of each distillation zone is achieved through the design of a partition plate and a U-shaped tube, and an agitator and a pressure regulator are equipped to improve separation efficiency.

Benefits of technology

Efficient separation of the components of the mixture is achieved, separation efficiency and product purity are improved, process and cost of subsequent processing is reduced, and energy consumption and environmental impact are reduced.

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Abstract

The utility model discloses a raw material distiller for chemical industry, which relates to the technical field of chemical industry and comprises a shell, a shell cover arranged at the top of the shell, a stirring device arranged in the shell, a first-stage distillation area, a second-stage distillation area and a third-stage distillation area fixedly arranged in the shell, and two partition plates fixedly arranged in the shell, and the first-stage distillation area, the second-stage distillation area and the third-stage distillation area are separated by partition plates. The first-stage distillation area, the second-stage distillation area and the third-stage distillation area are adopted to distill a mixture, the three U-shaped pipes are used for connecting the separation areas, the intercommunication of all the areas is ensured, the multi-stage distillation can be used for realizing the separation of all components of the mixture, the separation efficiency is improved, and fractions with higher purity can be obtained; meanwhile, after fractions with higher purity are obtained through multi-stage grading, the process and cost of subsequent treatment are reduced, and in the multi-stage distillation process, energy consumption is small, and the influence on the environment is small.
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Description

Technical Field

[0001] The utility model relates to the technical field of chemical industry, in particular to a raw material distiller for chemical industry. Background Art

[0002] Chemical industry refers to the chemical industry. Any use of chemical methods to change the composition or structure of substances, or to synthesize new substances, belongs to chemical production technology, that is, chemical process. The resulting products are called chemicals or chemical products. In the process of chemical production, chemical raw materials are usually distilled, and at this time a distiller is needed for distillation.

[0003] The existing distillation technology is a single distillation and cannot be multi-stage distillation. Since different components in the mixture have different boiling points, the single-stage distillation cannot obtain a fraction with a higher density from the mixture and cannot improve the distillation efficiency. Utility Model Content

[0004] In view of the above problems existing in the existing chemical distillation, the present utility model is proposed.

[0005] Therefore, the utility model aims to provide a chemical raw material distiller, which solves the problem of multi-stage distillation.

[0006] In order to achieve the above purpose, the utility model provides the following technical solutions:

[0007] A chemical raw material distiller comprises a shell, a shell cover is provided on the top of the shell, a stirring device is provided in the shell, a primary distillation zone, a secondary distillation zone and a tertiary distillation zone are fixedly provided in the shell, two partitions are fixedly provided in the shell, the primary distillation zone, the secondary distillation zone and the tertiary distillation zone are separated by the partitions, a heating plate is fixedly provided in the primary distillation zone, the secondary distillation zone and the tertiary distillation zone, three U-shaped tubes are fixedly provided on the top of the shell cover, condensers are fixedly provided on the tops of the three U-shaped tubes, and a pressure regulator is fixedly provided on the side wall of the shell.

[0008] Preferably, a motor is fixedly provided on one side of the shell, a rotating shaft is fixedly provided on the output end of the motor, the rotating shaft is rotatably connected to the shell, the rotating shaft passes through two partitions, and blades are fixedly provided on the shaft rod walls.

[0009] Preferably, a collecting pipe is fixedly provided at the bottom of the secondary distillation zone and the tertiary distillation zone, a first collecting box is provided at the bottom of the collecting pipe, a second collecting box is provided at one end of one of the U-shaped tubes, and a switch valve is fixedly provided at the bottom of the collecting pipe.

[0010] Preferably, a sealing gasket is fixedly provided on the bottom of the shell cover.

[0011] Furthermore, a feed port and a discharge port are fixedly provided on a side wall of one side of the shell.

[0012] Preferably, a base is fixedly provided at the bottom of the shell.

[0013] In the above technical solution, the technical effects and advantages provided by the utility model are:

[0014] 1. The utility model adopts a primary distillation zone, a secondary distillation zone and a tertiary distillation zone to distill the mixture, uses three U-shaped tubes to connect the separation zones to ensure that each zone is interconnected, and uses multi-stage distillation to separate the components of the mixture and improve the separation efficiency, so as to obtain a higher purity fraction. At the same time, after obtaining a higher purity fraction, the multi-stage classification reduces the process and cost of subsequent processing, and the energy consumption in the multi-stage distillation process is small and the impact on the environment is small.

[0015] 2. The utility model adopts three pressure regulators to adjust the pressure in the primary distillation zone, the secondary distillation zone and the tertiary distillation zone. The accuracy of pressure control is crucial to the separation efficiency and product quality of multi-stage distillation. At the same time, in order to ensure better gasification of the mixture, a motor-driven rotating shaft and paddles are provided on one side of the shell to stir the mixture and fractions in the primary distillation zone, the secondary distillation zone and the tertiary distillation zone to fully gasify them. BRIEF DESCRIPTION OF THE DRAWINGS

[0016] In order to more clearly illustrate the embodiments of the present application 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 recorded in the present utility model. For ordinary technicians in this field, other drawings can also be obtained based on these drawings.

[0017] Figure 1 It is a schematic diagram of the planar structure of the utility model;

[0018] Figure 2 It is a schematic cross-sectional view of the planar structure of the utility model;

[0019] Figure 3 It is a schematic diagram of the planar side view structure of the utility model;

[0020] Figure 4 For the utility model Figure 2 An enlarged schematic diagram of part A.

[0021] Description of reference numerals:

[0022] 1. Shell; 2. Shell cover; 3. Primary distillation zone; 4. Secondary distillation zone; 5. Tertiary distillation zone; 6. Partition; 7. Heating plate; 8. U-shaped tube; 9. Condenser; 10. Pressure regulator; 11. Motor; 12. Rotating shaft; 13. Paddle; 14. Collecting tube; 15. First collecting box; 16. Second collecting box; 17. Sealing gasket; 18. Feed inlet; 19. Discharge outlet; 20. Base; 21. Switch valve. DETAILED DESCRIPTION

[0023] In order to enable those skilled in the art to better understand the technical solution of the present invention, the present invention will be further described in detail below in conjunction with the accompanying drawings.

[0024] The utility model embodiment discloses a raw material distiller for chemical industry.

[0025] The utility model provides Figure 1-3 A chemical raw material distiller shown includes a shell 1, a shell cover 2 is provided on the top of the shell 1, a stirring device is provided in the shell 1, a primary distillation area 3, a secondary distillation area 4 and a tertiary distillation area 5 are fixedly provided in the shell 1, two partitions 6 are fixedly provided in the shell 1, the primary distillation area 3, the secondary distillation area 4 and the tertiary distillation area 5 are separated by the partition 6, a heating plate 7 is fixedly provided in the primary distillation area 3, the secondary distillation area 4 and the tertiary distillation area 5, three U-shaped tubes 8 are fixedly provided on the top of the shell cover 2, a condenser 9 is fixedly provided on the top of the three U-shaped tubes 8, a pressure regulator 10 is fixedly provided on the side wall of the shell 1, the raw materials are poured into the first distillation area, the pressure controller is adjusted, the heating plate 7 is turned on, and the motor 11 is started to fully stir the mixed liquid, the vaporization in the first distillation area reaches the second distillation area through one of the U-shaped tubes 8, the vaporized fraction is converted into liquefaction through the condenser 9, and the pressure controller of the second distillation area is adjusted so that the secondary distillation reaches the third distillation area to realize multi-stage distillation.

[0026] In order to fully blend the mixture, Figure 2 As shown, a motor 11 is fixedly provided on one side of the shell 1, a rotating shaft 12 is fixedly provided on the output end of the motor 11, the rotating shaft 12 is rotatably connected to the shell 1, the rotating shaft 12 passes through two partitions 6, and paddles 13 are fixedly provided on the rod walls of the rotating shaft 12. When the motor 11 is started, the motor 11 drives the rotating shaft 12 and the paddles 13 to rotate, so as to fully stir the mixed liquid.

[0027] In order to facilitate the collection of fractions from each region, Figure 1-4 As shown, a collecting pipe 14 is fixedly provided at the bottom of the secondary distillation zone 4 and the tertiary distillation zone 5, a first collecting box 15 is provided at the bottom of the collecting pipe 14, a second collecting box 16 is provided at one end of one of the U-shaped tubes 8, and a switch valve 21 is fixedly provided at the bottom of the collecting pipe 14. In order to facilitate the collection of fractions from each area, the first collecting box 15 and the second collecting box 16 are provided.

[0028] In order to prevent air leakage, Figure 2 As shown, a sealing gasket 17 is fixedly provided at the bottom of the shell cover 2 to ensure better sealing and to ensure that the shell 1 is sealed.

[0029] Finally, in order to facilitate feeding and discharging, such as Figure 1-2 As shown, a feed port 18 and a discharge port 19 are fixedly provided on a side wall of the housing 1 , and a base 20 is fixedly provided on the bottom of the housing 1 .

[0030] The above only describes some exemplary embodiments of the present invention by way of illustration. It is undoubted that those skilled in the art can modify the described embodiments in various ways without departing from the spirit and scope of the present invention. Therefore, the above drawings and descriptions are illustrative in nature and should not be construed as limiting the scope of protection of the claims of the present invention.

Claims

1. A chemical raw material distiller, comprising a housing (1), characterized in that: The shell (1) is provided with a shell cover (2) on the top, the shell (1) is provided with a stirring device, the shell (1) is provided with a primary distillation zone (3), a secondary distillation zone (4) and a tertiary distillation zone (5), two partitions (6) are fixedly provided in the shell (1), the primary distillation zone (3), the secondary distillation zone (4) and the tertiary distillation zone (5) are separated by the partitions (6), the primary distillation zone (3), the secondary distillation zone (4) and the tertiary distillation zone (5) are all fixedly provided with a heating plate (7), the shell cover (2) is provided with three U-shaped tubes (8) on the top, the three U-shaped tubes (8) are all fixedly provided with a condenser (9), and the side wall of the shell (1) is fixedly provided with a pressure regulator (10).

2. A chemical raw material distiller according to claim 1, characterized in that: A motor (11) is fixedly provided on one side of the housing (1), a rotating shaft (12) is fixedly provided on the output end of the motor (11), the rotating shaft (12) and the housing (1) are rotatably connected, the rotating shaft (12) passes through two partitions (6), and blades (13) are fixedly provided on the rod walls of the rotating shaft (12).

3. A chemical raw material distiller according to claim 1, characterized in that: A collecting pipe (14) is fixedly provided at the bottom of each of the secondary distillation zone (4) and the tertiary distillation zone (5); a first collecting box (15) is provided at the bottom of the collecting pipe (14); a second collecting box (16) is provided at one end of one of the U-shaped tubes (8); and a switch valve (21) is fixedly provided at the bottom of the collecting pipe (14).

4. A chemical raw material distiller according to claim 1, characterized in that: A sealing gasket (17) is fixedly provided on the bottom of the shell cover (2).

5. A chemical raw material distiller according to claim 1, characterized in that: A feed inlet (18) and a discharge outlet (19) are fixedly provided on a side wall of one side of the shell (1).

6. A chemical raw material distiller according to claim 1, characterized in that: A base (20) is fixedly provided at the bottom of the housing (1).