Sophorolipid raw material extraction device

Through the combination of ceramic cylindrical filter membrane and high-pressure gas-water system, the problem of low efficiency of the saccharide extraction device is solved, and the rapid and efficient raw material extraction and the stability of the filter membrane are achieved, and the service life is extended.

CN223144480UActive Publication Date: 2025-07-25SHAANXI DEGUAN BIOTECHNOLOGY CO LTD
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Patent Information

Application Number
CN202422260248.3
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-09-14
Publication Date
2025-07-25
Estimated Expiration
2034-09-14

AI Technical Summary

Technical Problem

The extraction efficiency of the existing sophora lipid extraction device is low, complex operation and long time.

Method used

The ceramic cylindrical filter membrane is used to combine with high-pressure air pipes and backwashing mechanisms, and the filter membrane is cleaned by high-pressure gas, and the fixing ring and check valve are combined to improve the stability and efficiency of the device.

Benefits of technology

The filtration speed of sophora lipid raw materials is accelerated, the extraction efficiency is improved, the service life of the filter membrane is extended, and the operating stability and operation flexibility of the device are enhanced.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model relates to the technical field of sophorolipid preparation, in particular to a sophorolipid raw material extraction device which comprises a tank body, an upper cover is connected to the upper side of the tank body in a sealed mode, a ceramic barrel-shaped filter membrane is arranged in the tank body, a sealing plug plate of a step-shaped structure is arranged at the position, corresponding to the ceramic barrel-shaped filter membrane, in the upper cover, and a hydraulic cylinder is assembled on the upper side of the upper cover. A backwashing mechanism is arranged in the tank body, a high-pressure air pump is assembled on the upper cover on the left side of the hydraulic cylinder, a high-pressure air pipe is connected to the output end of the high-pressure air pump, and the tail end of the high-pressure air pipe penetrates through the tank body and extends into the ceramic cylindrical filter membrane. According to the utility model, the ceramic barrel-shaped filter membrane is matched with the high-pressure gas pipe, and the interior of the ceramic barrel-shaped filter membrane is pressurized by utilizing high-pressure gas, so that the filtering speed of the ceramic barrel-shaped filter membrane on a sophorolipid raw material can be accelerated, the extraction efficiency of the sophorolipid raw material is improved, the time consumption is reduced, and the production efficiency is further improved.
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Description

Technical Field

[0001] The utility model relates to the technical field of sophorolipid preparation, and particularly relates to an extraction device for sophorolipid raw materials. Background Technique

[0002] Sophorolipid is a secondary metabolite of microorganisms produced by Candida yeast using sugars and vegetable oils as carbon sources through a fermentation process under certain conditions. It is a glycolipid biosurfactant and is widely used in fields such as food, cosmetics, and environmental protection. Sophorolipid has general properties such as solubilization, emulsification, wetting, foaming, dispersion, and reduction of surface tension possessed by conventional surfactants. The production process of sophorolipid includes two processes: fermentation and extraction. The fermentation process is completely a microbial metabolism process, and the raw materials are natural plant-derived raw materials. The extraction process uses a physical extraction process without organic solvents. There are no chemical reactions and chemical component additions in all process steps, ensuring the overall process is green and environmentally friendly.

[0003] After the fermentation of sophorolipid is completed, purification treatment is required to extract the sophorolipid stock solution from the raw materials. Existing extraction devices use physical extraction processes such as natural precipitation, centrifugation, and membrane filtration. However, the extraction efficiency of a single extraction method is low, and repeated operations are required, resulting in complex operations and long time consumption. There is an urgent need for a new type of extraction device to solve the above problems. Content of the Utility Model

[0004] In view of the existing deficiencies, the utility model provides an extraction device for sophorolipid raw materials, which solves the problems raised in the above background technique.

[0005] To achieve the above purpose, the technical solution adopted by the utility model is as follows:

[0006] An extraction device for sophorolipid raw materials includes a tank body and an upper cover. The upper side of the tank body is hermetically connected with the upper cover. A ceramic cylindrical filter membrane is arranged inside the tank body. A discharge pipe is fixedly arranged at the bottom of the tank body, and the upper end of the discharge pipe communicates with the bottom of the ceramic cylindrical filter membrane. A first valve is assembled on the discharge pipe. A sealing plug plate with a stepped structure is arranged at the corresponding position of the inner part of the upper cover and the ceramic cylindrical filter membrane. A hydraulic cylinder is assembled on the upper side of the upper cover. The lower end of the hydraulic cylinder extends into the inner part of the upper cover and is fixedly connected with the sealing plug plate. An anti-flushing mechanism is arranged inside the tank body. A high-pressure air pump is assembled on the upper cover on the left side of the hydraulic cylinder. The output end of the high-pressure air pump is connected with a high-pressure air pipe, and the end of the high-pressure air pipe penetrates through the tank body and extends into the ceramic cylindrical filter membrane. A material pump is assembled on the upper cover on the right side of the hydraulic cylinder. The output end of the material pump is connected with a feed hose. The input end of the material pump is connected with an external sophorolipid raw material storage device through a pipeline. A feed flow channel is opened inside the sealing plug plate, and the lower end of the feed hose is inserted into the feed flow channel.

[0007] Further, fixing rings are fixedly provided on both the upper and lower sides of the toroidal surface of the ceramic cylindrical filter membrane, and the fixing rings are fixedly connected to the inner wall of the tank body through a plurality of radially structured support rods.

[0008] Further, the bottom of the tank body is arranged in an upwardly convex arc structure, a discharge pipe is fixedly provided near the left edge of the bottom of the tank body, and a second valve is assembled on the discharge pipe.

[0009] Further, a check valve is assembled on the high-pressure air pipe, and an electromagnetic valve is assembled on the feed hose.

[0010] Further, the backwashing mechanism includes a washing assembly, an electric push rod, a bottom plate, a high-pressure water pump, a high-pressure water pipe and a water inlet hose. There are two groups of the washing assemblies and they are symmetrically arranged on the left and right sides of the ceramic cylindrical filter membrane inside the tank body. Electric push rods are symmetrically assembled on both the left and right sides of the toroidal surface of the tank body, and the output ends of the electric push rods extend into the tank body and are fixedly connected to the washing assemblies. A bottom plate is fixedly provided on the rear side of the toroidal surface of the tank body, a high-pressure water pump is installed on the bottom plate, a high-pressure water pipe is connected to the output end of the high-pressure water pump, and water inlet hoses are provided on both the left and right sides of the high-pressure water pipe and are connected to the washing assemblies.

[0011] Further, the washing assembly includes an enclosing plate, a buffer chamber, high-pressure nozzles and grooves. The enclosing plate is arranged in a semi-cylindrical tubular structure. After the two enclosing plates are closed and connected, a tubular structure with a closed side is formed. Grooves are opened on the inner side surface of the enclosing plate, a plurality of high-pressure nozzles are evenly provided at the bottom of the grooves, a buffer chamber is opened inside the enclosing plate, and the high-pressure nozzles and the water inlet hose are both communicated with the buffer chamber.

[0012] Further, a layer of sealing gasket is pasted on the opposite surfaces of the two enclosing plates.

[0013] Compared with the prior art, the utility model has the following beneficial effects:

[0014] 1. By means of the ceramic cylindrical filter membrane and the high-pressure air pipe, the utility model pressurizes the inside of the ceramic cylindrical filter membrane by using high-pressure gas, which can accelerate the filtration speed of the ceramic cylindrical filter membrane for the sophorolipid raw material, improve the extraction efficiency of the sophorolipid raw material, reduce the time consumption, and thus improve the production efficiency.

[0015] 2. In the utility model, the backwashing mechanism directly washes the surface of the ceramic cylindrical filter membrane with high-pressure water flow, which can quickly remove the residues on the ceramic cylindrical filter membrane, restore the filtration performance of the ceramic cylindrical filter membrane, reduce the risk of blockage and wear of the ceramic cylindrical filter membrane, and thus extend the service life of the ceramic cylindrical filter membrane.

[0016] 3. In the utility model, fixing rings are fixed on both the upper and lower sides of the ceramic cylindrical filter ring, and the fixing rings are fixedly connected to the inner wall of the tank through multiple groups of radial support rods. The two groups of fixing rings are used to fix the ceramic cylindrical filter, enhance the stability of the ceramic cylindrical filter in the tank, and prevent the ceramic cylindrical filter from deflecting and shaking.

[0017] 4. In the utility model, the bottom of the tank body is set as an upwardly protruding arc structure, which is conducive to the flow and discharge of the material at the bottom of the tank body, reduces the accumulation and retention of the material at the bottom, and helps to improve the extraction efficiency. A discharge pipe is fixed near the left edge of the bottom of the tank body, and a second valve is installed on the discharge pipe. The discharge pipe is used to discharge the material at the bottom of the tank body. The second valve realizes precise control of the discharge process. By opening or closing the valve, the discharge speed and discharge amount can be flexibly adjusted.

[0018] 5. In the utility model, a check valve is installed on the medium and high pressure air pipe, which can prevent the backflow of the sophorolipid raw material inside the ceramic cylindrical filter membrane, which helps to maintain the stability of the internal pressure of the ceramic cylindrical filter membrane and improve the operating stability of the entire device. The feed hose is equipped with a solenoid valve, which is used to accurately control the delivery of the raw materials. By adjusting the opening and closing state of the solenoid valve, the flow rate and flow velocity of the raw materials can be accurately controlled. At the same time, the feed hose can be closed by the solenoid valve to prevent the gas in the ceramic cylindrical filter membrane from leaking out of the feed hose, which is conducive to maintaining the internal pressure of the ceramic cylindrical filter membrane. BRIEF DESCRIPTION OF THE DRAWINGS

[0019] Figure 1 It is a schematic diagram of the overall structure of the utility model.

[0020] Figure 2 It is a schematic diagram of the rear structure of the utility model.

[0021] Figure 3 It is a schematic diagram of the internal structure of the tank body in the utility model.

[0022] Figure 4 It is a cross-sectional view of the utility model.

[0023] Figure 5 It is a structural schematic diagram of the backwashing mechanism in the utility model.

[0024] Figure 6 It is a cross-sectional view of the flushing component in the utility model.

[0025] In the figure: 1. Hydraulic cylinder; 2. High-pressure air pump; 3. High-pressure air pipe; 4. Check valve; 5. Backwashing mechanism; 51. Flushing assembly; 511. Enclosure plate; 512. Buffer chamber; 513. High-pressure nozzle; 514. Sealing gasket; 515. Groove; 52. Electric push rod; 53. Bottom plate; 54. High-pressure water pump; 55. High-pressure water pipe; 56. Water inlet hose; 6. Material pump; 7. Upper cover; 8. Tank body; 9. First valve; 10. Discharge pipe; 11. Drain pipe; 12. Second valve; 13. Sealing plug plate; 14. Feed hose; 15. Solenoid valve; 16. Fixed ring; 17. Ceramic cylindrical filter membrane; 18. Feed flow channel. Detailed implementation manner

[0026] Next, the technical solutions in the embodiments of the present invention will be clearly and completely described in conjunction with the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

[0027] Embodiment:

[0028] As Figures 1 to 6 shown, a sophorolipid raw material extraction device includes a tank body 8 and an upper cover 7. The upper cover 7 is hermetically connected to the upper side of the tank body 8. A ceramic cylindrical filter membrane 17 is provided inside the tank body 8. A discharge pipe 10 is fixedly provided at the bottom of the tank body 8, and the upper end of the discharge pipe 10 communicates with the bottom of the ceramic cylindrical filter membrane 17. A first valve 9 is assembled on the discharge pipe 10. A sealing plug plate 13 with a stepped structure is provided inside the upper cover 7 corresponding to the ceramic cylindrical filter membrane 17. A hydraulic cylinder 1 is assembled on the upper side of the upper cover 7. The lower end of the hydraulic cylinder 1 extends into the upper cover 7 and is fixedly connected to the sealing plug plate 13. A backwashing mechanism 5 is provided inside the tank body 8. A high-pressure air pump 2 is assembled on the upper cover 7 on the left side of the hydraulic cylinder 1. The output end of the high-pressure air pump 2 is connected with a high-pressure air pipe 3, and the end of the high-pressure air pipe 3 penetrates through the tank body 8 and extends into the ceramic cylindrical filter membrane 17. A material pump 6 is assembled on the upper cover 7 on the right side of the hydraulic cylinder 1. The output end of the material pump 6 is connected with a feed hose 14. The input end of the material pump 6 is connected to an external sophorolipid raw material storage device through a pipeline. A feed flow channel 18 is opened inside the sealing plug plate 13, and the lower end of the feed hose 14 is inserted into the feed flow channel 18. This design solves the problems that the existing extraction devices usually adopt a single physical extraction process, the single extraction method has low extraction efficiency, requires repeated operations, is complex in operation, and takes a long time.

[0029] In this embodiment, fixing rings 16 are fixedly arranged on both the upper and lower sides of the circumferential surface of the ceramic cylindrical filter membrane 17. The fixing rings 16 are fixedly connected to the inner wall of the tank body 8 through multiple groups of radially structured support rods. The two sets of fixing rings 16 provided realize the fixation of the ceramic cylindrical filter membrane 17, enhance the stability of the ceramic cylindrical filter membrane 17 in the tank body 8, and prevent the ceramic cylindrical filter membrane 17 from shifting and shaking.

[0030] In this embodiment, the bottom of the tank body 8 is arranged as an upwardly convex arc structure. The upwardly convex arc structure is beneficial to the flow and discharge of the materials at the bottom of the tank body 8, reduces the accumulation and retention of the materials at the bottom, and helps to improve the extraction efficiency. A discharge pipe 11 is fixedly arranged near the left edge of the bottom of the tank body 8. A second valve 12 is assembled on the discharge pipe 11. The discharge pipe 11 is used to discharge the materials at the bottom of the tank body 8. The second valve 12 realizes the precise control of the discharge process. By opening or closing the valve, the discharge speed and discharge amount can be flexibly adjusted.

[0031] In this embodiment, a check valve 4 is assembled on the high-pressure air pipe 3. The check valve 4 can prevent the backflow of the sophorolipid raw materials inside the ceramic cylindrical filter membrane 17, helps to maintain the stability of the internal pressure of the ceramic cylindrical filter membrane 17, and improves the operation stability of the entire device. An electromagnetic valve 15 is assembled on the feed hose 14. The electromagnetic valve 15 is used to precisely control the conveying of the raw materials. By adjusting the opening and closing state of the electromagnetic valve 15, the precise control of the raw material flow rate and flow velocity can be realized. At the same time, the feed hose 14 can be closed through the electromagnetic valve 15 to prevent the gas in the ceramic cylindrical filter membrane 17 from leaking out through the feed hose 14, which is beneficial to maintaining the internal pressure of the ceramic cylindrical filter membrane 17.

[0032] In this embodiment, the backwashing mechanism 5 includes a washing component 51, an electric push rod 52, a bottom plate 53, a high-pressure water pump 54, a high-pressure water pipe 55 and a water inlet hose 56. There are two sets of washing components 51, which are symmetrically arranged on the left and right sides of the ceramic cylindrical filter membrane 17 inside the tank body 8. Electric push rods 52 are symmetrically assembled on both the left and right sides of the circumferential surface of the tank body 8. The output end of the electric push rod 52 extends into the tank body 8 and is fixedly connected to the washing component 51. A bottom plate 53 is fixedly arranged on the rear side of the circumferential surface of the tank body 8. A high-pressure water pump 54 is installed on the bottom plate 53. The output end of the high-pressure water pump 54 is connected to a high-pressure water pipe 55. Water inlet hoses 56 are arranged on both the left and right sides of the high-pressure water pipe 55 and are connected to the washing component 51. The backwashing mechanism 5 directly washes the surface of the ceramic cylindrical filter membrane 17 with high-pressure water flow, can quickly remove the residues on the ceramic cylindrical filter membrane 17, restore the filtering performance of the ceramic cylindrical filter membrane 17, reduce the risk of blockage and wear of the ceramic cylindrical filter membrane 17, and thus extend the service life of the ceramic cylindrical filter membrane 17.

[0033] In this embodiment, the flushing assembly 51 includes an enclosing plate 511, a buffer chamber 512, high-pressure nozzles 513 and grooves 515. The enclosing plate 511 is arranged in a semi-cylindrical tubular structure. After two groups of enclosing plates 511 are closed and connected, a tubular structure with a closed side is formed. Grooves 515 are formed on the inner side surface of the enclosing plate 511. A plurality of groups of high-pressure nozzles 513 are evenly arranged at the bottom of the grooves 515. A buffer chamber 512 is formed inside the enclosing plate 511. Both the high-pressure nozzles 513 and the water inlet hose 56 are communicated with the buffer chamber 512. The flushing assembly 51 sprays high-pressure water flow onto the outer surface of the ceramic tubular filter membrane 17 at a high speed through the high-pressure nozzles 513, which can quickly remove the residues on the ceramic tubular filter membrane 17 and improve the flushing efficiency. At the same time, the arranged enclosing plate 511 enables the flushing operation to be carried out in a closed space, avoiding the splashing of high-pressure water flow and ensuring the flushing effect. In addition, the uniform distribution of the high-pressure nozzles 513 also ensures the uniformity of the flushing operation, enabling the high-pressure water flow to completely cover the surface of the ceramic tubular filter membrane 17 and ensuring the flushing quality.

[0034] In this embodiment, a layer of sealing gasket 514 is pasted on the opposite surfaces of the two groups of enclosing plates 511. The arranged sealing gasket 514 ensures the sealing performance of the connection between the two groups of enclosing plates 511 after being closed.

[0035] The working principle of this sophorolipid raw material extraction device: In actual use, first close the first valve 9, open the second valve 12 and the solenoid valve 15 on the feed hose 14, and then start the material pump 6. The material pump 6 sucks the raw materials from the external sophorolipid raw material storage device through the pipeline and transports them to the feed flow channel 18 inside the sealing plug plate 13 via the feed hose 14. The raw materials flow out from the feed flow channel 18 and enter the inside of the ceramic tubular filter membrane 17. The raw materials are filtered inside the ceramic tubular filter membrane 17. The effective components such as sophorolipids are intercepted by the filter membrane, while other substances in the raw materials flow out through the filter membrane and are finally discharged through the discharge pipe 11 at the bottom of the tank body 8. During the filtering process, start the hydraulic cylinder 1. By controlling the hydraulic cylinder 1, the sealing plug plate 13 is pressed down to be in close contact with the upper end of the ceramic tubular filter membrane 17 to form a seal. Then the high-pressure air pump 2 works, and high-pressure gas is conveyed into the inside of the ceramic tubular filter membrane 17 through the high-pressure air pipe 3 to increase the pressure inside the filter membrane, accelerate the filtering speed of the raw materials, promote the filtering of the raw materials, and thus realize the rapid extraction and filtering treatment of the raw materials;

[0036] After the filtration is completed, open the first valve 9 to discharge the sophorolipid filtered out in the ceramic cylindrical filter membrane 17 through the discharge pipe 10. Then start the backwashing mechanism 5 for cleaning. The electric push rod 52 works to push the washing component 51 close to the ceramic cylindrical filter membrane 17, and the two groups of enclosing plates 511 are hermetically sleeved on the outer side of the ceramic cylindrical filter membrane 17. Then the high-pressure water pump 54 works to convey high-pressure water flow into the buffer cavity 512 in the enclosing plate 511 through the high-pressure water pipe 55 and the water inlet hose 56. The high-pressure water flow is sprayed onto the outer surface of the ceramic cylindrical filter membrane 17 at a high speed from the high-pressure nozzle 513 to perform backwashing on the ceramic cylindrical filter membrane 17 and remove the residues on the inner wall of the ceramic cylindrical filter membrane 17.

[0037] Obviously, the above embodiments of the present invention are merely examples for clearly illustrating the present invention, rather than limitations on the implementation manners of the present invention. For those of ordinary skill in the art, other different forms of changes or variations can be made based on the above description. It is impossible to list all the implementation manners here. Any obvious changes or variations derived from the technical solutions of the present invention still fall within the protection scope of the present invention.

Claims

1. A sophorolipid raw material extraction device, comprising a tank body (8) and an upper cover (7), characterized in that: A top cover (7) is hermetically connected to the upper side of the tank body (8). A ceramic cylindrical filter membrane (17) is arranged inside the tank body (8). A discharge pipe (10) is fixedly arranged at the bottom of the tank body (8), and the upper end of the discharge pipe (10) communicates with the bottom of the ceramic cylindrical filter membrane (17). A first valve (9) is assembled on the discharge pipe (10). A sealing plug plate (13) with a stepped structure is arranged at the corresponding position of the inner part of the top cover (7) and the ceramic cylindrical filter membrane (17). A hydraulic cylinder (1) is assembled on the upper side of the top cover (7). The lower end of the hydraulic cylinder (1) extends into the inner part of the top cover (7) and is fixedly connected with the sealing plug plate (13). An anti-flushing mechanism (5) is arranged inside the tank body (8). A high-pressure air pump (2) is assembled on the top cover (7) on the left side of the hydraulic cylinder (1). A high-pressure air pipe (3) is connected to the output end of the high-pressure air pump (2), and the end of the high-pressure air pipe (3) penetrates through the tank body (8) and extends into the inner part of the ceramic cylindrical filter membrane (17). A material pump (6) is assembled on the top cover (7) on the right side of the hydraulic cylinder (1). A feed hose (14) is connected to the output end of the material pump (6). The input end of the material pump (6) is connected to an external sophorolipid raw material storage device through a pipeline. A feed flow channel (18) is formed inside the sealing plug plate (13), and the lower end of the feed hose (14) is inserted into the feed flow channel (18).

2. The sophorolipid raw material extraction device according to claim 1, wherein: Fixed rings (16) are fixedly arranged on both the upper and lower sides of the circumferential surface of the ceramic cylindrical filter membrane (17). The fixed rings (16) are fixedly connected to the inner wall of the tank body (8) through multiple groups of radially structured support rods.

3. The sophorolipid raw material extraction device according to claim 1, wherein: The bottom of the tank body (8) is arranged as an upwardly convex arc-shaped structure. A discharge pipe (11) is fixedly arranged near the left edge of the bottom of the tank body (8). A second valve (12) is assembled on the discharge pipe (11).

4. The sophorolipid raw material extraction device according to claim 1, characterized in that: A check valve (4) is assembled on the high-pressure air pipe (3). An electromagnetic valve (15) is assembled on the feed hose (14).

5. The sophorolipid raw material extraction device according to claim 1, characterized in that: The anti-flushing mechanism (5) includes a flushing assembly (51), an electric push rod (52), a bottom plate (53), a high-pressure water pump (54), a high-pressure water pipe (55) and a water inlet hose (56). Two groups of flushing assemblies (51) are provided and symmetrically arranged on the left and right sides of the ceramic cylindrical filter membrane (17) inside the tank body (8). Electric push rods (52) are symmetrically assembled on both the left and right sides of the circumferential surface of the tank body (8). The output end of the electric push rod (52) extends into the inner part of the tank body (8) and is fixedly connected with the flushing assembly (51). A bottom plate (53) is fixedly arranged on the rear side of the circumferential surface of the tank body (8). A high-pressure water pump (54) is installed on the bottom plate (53). A high-pressure water pipe (55) is connected to the output end of the high-pressure water pump (54). Water inlet hoses (56) are arranged on both the left and right sides of the high-pressure water pipe (55) and are connected to the flushing assembly (51).

6. The sophorolipid raw material extraction device according to claim 5, characterized in that: The flushing assembly (51) includes an enclosure plate (511), a buffer chamber (512), high-pressure nozzles (513) and grooves (515). The enclosure plate (511) is arranged in a semi-cylindrical tubular structure. After two groups of the enclosure plates (511) are closed and connected, a tubular structure with a closed side is formed. A groove (515) is formed on the inner side surface of the enclosure plate (511). A plurality of groups of high-pressure nozzles (513) are evenly arranged at the bottom of the groove (515). A buffer chamber (512) is formed inside the enclosure plate (511), and the high-pressure nozzles (513) and the water inlet hose (56) are both communicated with the buffer chamber (512).

7. The sophorolipid raw material extraction device according to claim 6, wherein: A layer of sealing rubber pads (514) are pasted on the opposite surfaces of the two groups of the enclosure plates (511).