Reduced-pressure filtering equipment for production of bovine-derived bilirubin

By adopting continuous feeding and stirring and negative pressure discharge mechanisms in the production equipment of Niuyuan bilirubin, combined with the pressure-keeping liquid discharge structure and efficient stirring system, the problem of the equipment not being able to continuously and efficient filtration is improved, and the filtration efficiency and product purity are improved. , ensuring the stability and safety of the production process.

CN222131131UActive Publication Date: 2024-12-10HAOTAI JUYUAN (JILIN) PHARMACEUTICAL CO LTD
View PDF 1 Cites 0 Cited by

Patent Information

Application Number
CN202422712199.2
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-11-07
Publication Date
2024-12-10
Estimated Expiration
2034-11-07

AI Technical Summary

Technical Problem

The existing bovine bilirubin production equipment cannot maintain high-efficiency filtration, resulting in unstable filtration efficiency and yield.

Method used

A reduced pressure filtering equipment including main base, column, liquid collecting bucket, filter cartridge, stirring structure and negative pressure generation structure was designed. Through continuous feeding stirring and negative pressure discharge mechanism, combining pressure-keeping and liquid discharge structure and high efficiency Agitate system to realize continuous rinsing and filtration.

Benefits of technology

It improves filtration efficiency and product purity, enhances process stability and safety, and ensures the quality consistency of each batch of products.

✦ Generated by Eureka AI based on patent content.

Smart Images

  • Figure CN222131131U_ABST
    Figure CN222131131U_ABST
Patent Text Reader

Abstract

The utility model discloses decompression filtering equipment for producing bovine-derived bilirubin, relates to the technical field of filtering equipment, and solves the technical problem that high efficiency cannot be continuously kept in the existing technical scheme. The decompression filtering equipment comprises a main base, a stand column is fixedly mounted on the upper wall surface of the main base, and a liquid collecting hopper is fixedly mounted on the upper wall surface of the stand column; the lower end of the liquid collecting hopper is fixedly provided with a pressure maintaining and liquid discharging structure, the liquid collecting hopper is internally provided with a filter cartridge, the liquid collecting hopper is provided with a stirring structure, and the liquid collecting hopper is provided with a negative pressure generating structure. The yield of a final product is improved; the problem that liquid cannot be discharged due to air suction from the lower part caused by excessive pressure relief and direct discharging can be effectively prevented, and the stability and safety of the process are improved; fine filtration can be achieved, and the purity and quality of products are effectively improved.
Need to check novelty before this filing date? Find Prior Art

Description

Technical Field

[0001] The utility model relates to the technical field of filtering equipment, in particular to a decompression filtering equipment for producing bovine bilirubin. Background Art

[0002] In the technical field involved in the utility model, the vacuum filtration of bovine bilirubin plays a key role in its production process, which is mainly reflected in purification and refining, improving product stability, improving process efficiency, strengthening quality control and enhancing safety. Through vacuum filtration, impurities and by-products can be effectively removed and the purity of bilirubin can be improved, which is crucial to meet the high specifications of the medical and industrial fields. In addition, by removing impurities and moisture, the chemical stability of bilirubin is enhanced, making it less likely to degrade during storage and use. Vacuum filtration can also speed up the filtration speed and shorten the production cycle, thereby improving overall efficiency, reducing production costs and increasing production capacity. In terms of quality control, vacuum filtration ensures that each batch of products can meet the expected quality standards. At the same time, because it is carried out at relatively low temperature and pressure, the safety of the process is also greatly improved, reducing the potential risk of chemical reactions. Therefore, vacuum filtration has important functions and significance for the production of bovine bilirubin.

[0003] For example, a utility model named "A bilirubin preparation precipitation and filtration device" with publication number CN221412356U includes: a base, a support plate, a feed seat and a servo motor, wherein the upper end of the base is fixedly provided with a support plate, a disassembly and removal structure is provided above the base, a double-rod stirring structure is provided above the base, the disassembly and removal structure includes an upper kettle body, the upper kettle body is fixedly connected to one end of the support plate, a feed seat is provided on the side wall of the upper kettle body, a servo motor is fixedly provided on the upper end of the upper kettle body, and a lower kettle body is assembled at the bottom end of the upper kettle body.

[0004] The existing technical solutions have the technical problem of being unable to maintain high efficiency continuously. Utility Model Content

[0005] In view of the deficiencies of the prior art, the utility model provides a decompression filtration device for producing bovine bilirubin, which solves the technical problem that the prior technical solution cannot continuously maintain high efficiency.

[0006] To achieve the above objectives, the utility model is implemented through the following technical solutions: a vacuum filtration device for producing bovine bilirubin, comprising a main base, a column is fixedly installed on the upper wall of the main base, a liquid collecting bucket is fixedly installed on the upper wall of the column, a pressure-maintaining liquid discharge structure is fixedly installed at the lower end of the liquid collecting bucket, a filter cartridge is installed in the liquid collecting bucket, a stirring structure is installed on the liquid collecting bucket, and a negative pressure generating structure is installed on the liquid collecting bucket. Through continuous feeding, stirring and negative pressure discharge, continuous flushing and filtration can be maintained, the filtering effect is improved, and the final output is increased.

[0007] Preferably, the pressure-maintaining drainage structure includes a drainage pipe, an upper solenoid valve and a lower solenoid valve, and the upper solenoid valve and the lower solenoid valve are fixedly installed on the drainage pipe, and the drainage pipe is fixedly installed at the lower end of the liquid collecting bucket. When a certain amount of filtered liquid is accumulated, the upper solenoid valve is opened to allow the liquid to flow naturally into the drainage pipe, and prevent excessive pressure relief and direct discharge that causes air to be sucked in from below and makes it impossible to drain the liquid. Then, the upper solenoid valve is closed and the lower solenoid valve is opened to discharge the product, and then the lower solenoid valve is closed to reset.

[0008] Preferably, the filter cartridge is a ball-end tube with an open end, the bottom end and side wall of the filter cartridge are provided with a mounting cage, a filtrate membrane is installed in the filter cartridge, a sealing frame is fixedly installed on the side wall of the filter cartridge, the sealing frame is fixedly connected to the liquid collecting bucket, and a liquid adding tube is fixedly installed on the sealing frame.

[0009] Preferably, the stirring structure includes a stirring frame, which is fixedly mounted on the upper wall of the liquid collecting hopper, and a first motor, a gear reducer and a stirring shaft are fixedly mounted inside the stirring frame, a stirring rod is fixedly mounted on the lower end of the stirring shaft, the driving end of the first motor is fixedly connected to the input end of the gear reducer, a driving bevel gear is fixedly mounted on the output end of the gear reducer, a driven bevel gear is fixedly mounted on the stirring shaft, and the driving bevel gear is meshingly connected with the driven bevel gear.

[0010] Preferably, the negative pressure generating structure comprises an air pump and a safety box, the air pump and the safety box are fixedly mounted on the column, the input end of the air pump is connected to the safety box, and the safety box is connected to the liquid collecting hopper.

[0011] Preferably, a pressure gauge is fixedly installed in the safety box, a sewage pipe is fixedly installed at the lower end of the safety box, a safety valve is arranged on the liquid collecting hopper, and a liquid retaining cylinder is installed in the liquid collecting hopper.

[0012] Beneficial Effects

[0013] The utility model provides a pressure-reducing filtration device for producing bovine bilirubin. The utility model can maintain continuous flushing and filtration through continuous feeding and stirring and negative pressure discharge mechanism, improve filtration efficiency, and thus increase the output of the final product. The upper and lower solenoid valves in the pressure-maintaining and liquid-discharging structure are designed to effectively prevent the problem of being unable to discharge liquid due to excessive pressure relief and direct discharge, thereby improving the stability and safety of the process. The open ball head tube design at one end of the filter cartridge, in conjunction with the filtrate membrane and the sealing frame, can achieve fine filtration and effectively improve the purity and quality of the product. In the stirring structure, efficient stirring is achieved through the design of the first motor, the gear reducer, and the active and driven bevel gears, which is beneficial to the uniform mixing and processing of the materials. BRIEF DESCRIPTION OF THE DRAWINGS

[0014] Figure 1 This is a schematic diagram of the main cross-sectional structure of a vacuum filtration device for producing bovine bilirubin described in the utility model.

[0015] In the figure: 1, main base; 2, column; 3, liquid collecting bucket; 4, filter cartridge; 5, drain pipe; 6, upper solenoid valve; 7, lower solenoid valve; 8, mounting cage; 9, filtrate membrane; 10, sealing frame; 11, liquid adding pipe; 12, stirring frame; 13, first motor; 14, gear reducer; 15, stirring shaft; 16, stirring rod; 17, driving bevel gear; 18, driven bevel gear; 19, vacuum pump; 20, safety box; 21, barometer; 22, drain pipe; 23, safety valve; 24, liquid retaining cylinder; DETAILED DESCRIPTION

[0016] In order to further explain the technical means and effects adopted by the present invention to achieve the predetermined purpose of the utility model, the technical scheme in the embodiment of the utility model will be clearly and completely described below in combination with the drawings in the embodiment of the utility model. Obviously, the described embodiment is only a part of the embodiment of the utility model, rather than all the embodiments. The detailed description is as follows.

[0017] See also Figure 1 The utility model provides a technical solution: a vacuum filtration device for producing bovine bilirubin, comprising a main base 1, a column 2 is fixedly installed on the upper wall of the main base 1, a liquid collecting bucket 3 is fixedly installed on the upper wall of the column 2, a pressure-maintaining and liquid-discharging structure is fixedly installed at the lower end of the liquid collecting bucket 3, a filter cartridge 4 is installed in the liquid collecting bucket 3, a stirring structure is installed on the liquid collecting bucket 3, and a negative pressure generating structure is installed on the liquid collecting bucket 3. Through continuous feeding, stirring and negative pressure discharge, continuous flushing and filtration can be maintained, the filtering effect is improved, and the final output is increased.

[0018] The present embodiment is further configured such that the pressure-maintaining liquid discharge structure includes a liquid discharge pipe 5, an upper solenoid valve 6 and a lower solenoid valve 7. The upper solenoid valve 6 and the lower solenoid valve 7 are fixedly mounted on the liquid discharge pipe 5. The liquid discharge pipe 5 is fixedly mounted at the lower end of the liquid collecting hopper 3. When a certain amount of filtered liquid is accumulated, the upper solenoid valve 6 is opened to allow the liquid to flow naturally into the liquid discharge pipe 5, and to prevent excessive pressure relief and direct discharge that causes air to be sucked in from below and makes it impossible to discharge the liquid. Then, the upper solenoid valve 6 is closed and the lower solenoid valve 7 is opened to discharge the product, and then the lower solenoid valve 7 is closed to reset.

[0019] The present embodiment is further configured as follows: the filter cartridge 4 is a ball-end tube with an open end, the bottom end and side wall of the filter cartridge 4 are provided with a mounting cage 8, a filtrate membrane 9 is installed in the filter cartridge 4, a sealing frame 10 is fixedly installed on the side wall of the filter cartridge 4, the sealing frame 10 is fixedly connected to the liquid collecting bucket 3, and a liquid adding pipe 11 is fixedly installed on the sealing frame 10.

[0020] The present embodiment is further configured as follows: the stirring structure includes a stirring frame 12, the stirring frame 12 is fixedly mounted on the upper wall of the liquid collecting hopper 3, a first motor 13, a gear reducer 14 and a stirring shaft 15 are fixedly mounted in the stirring frame 12, a stirring rod 16 is fixedly mounted on the lower end of the stirring shaft 15, the driving end of the first motor 13 is fixedly connected to the input end of the gear reducer 14, a driving bevel gear 17 is fixedly mounted on the output end of the gear reducer 14, a driven bevel gear 18 is fixedly mounted on the stirring shaft 15, and the driving bevel gear 17 is meshingly connected with the driven bevel gear 18.

[0021] This embodiment is further configured such that the negative pressure generating structure includes an air pump 19 and a safety box 20, the air pump 19 and the safety box 20 are fixedly mounted on the column 2, the input end of the air pump 19 is connected to the safety box 20, and the safety box 20 is connected to the liquid collecting hopper 3.

[0022] This embodiment is further configured as follows: a pressure gauge 21 is fixedly installed in the safety box 20, a sewage pipe 22 is fixedly installed at the lower end of the safety box 20, a safety valve 23 is provided on the liquid collecting hopper 3, and a liquid blocking cylinder 24 is installed in the liquid collecting hopper 3.

[0023] The detailed connection means are well known in the art; Figure 1 As shown, ensure that the equipment is in good working condition and check whether the connections of each part of the equipment are tight.

[0024] Ensure that the filtrate membrane 9 in the filter cartridge 4 is intact and replace it if necessary.

[0025] Ensure that the stirring structure and negative pressure generating structure operate normally.

[0026] The raw material liquid of bovine bilirubin is injected into the liquid collecting hopper 3 through the liquid adding pipe 11 .

[0027] Start the stirring structure, start the first motor 13, and drive the stirring shaft 15 to rotate through the gear reducer 14 and the driving bevel gear 17 and the driven bevel gear 18 to ensure that the stirring shaft 15 and the stirring rod 16 work normally and fully mix the raw material liquid.

[0028] The vacuum pump 19 in the negative pressure generating structure is started to generate negative pressure in the liquid collecting hopper 3 and start the filtering process.

[0029] The generation of negative pressure helps the liquid to be filtered through the filter cartridge 4 and the filtrate membrane 9 .

[0030] The pressure-maintaining liquid discharge structure is controlled by the upper solenoid valve 6 and the lower solenoid valve 7. When a certain amount of filtered liquid is accumulated in the liquid collecting hopper 3, the upper solenoid valve 6 is opened to allow the liquid to flow naturally into the liquid discharge pipe 5.

[0031] Close the upper solenoid valve 6 at the appropriate time and open the lower solenoid valve 7 to discharge the filtered product.

[0032] The pressure is monitored by the pressure gauge 21 in the safety box 20, and the safety valve 23 is adjusted as needed to ensure the safe operation of the equipment.

[0033] Check the sewage pipe 22 and the safety box 20 regularly to ensure that there is no blockage or leakage.

[0034] After use, the equipment should be cleaned, especially the filter cartridge 4 and various pipes.

[0035] Maintain equipment regularly and check components such as motors, pumps and valves to ensure long-term stable operation.

[0036] It should be noted that, in this document, relational terms such as first and second, etc. are merely used to distinguish one entity or operation from another entity or operation, and do not necessarily require or imply any actual relationship or order between these entities or operations.

[0037] The above description is only a preferred embodiment of the present invention and does not constitute any form of limitation to the present invention. Although the present invention has been disclosed as a preferred embodiment as above, it is not intended to limit the present invention. Any technical personnel in this field can make some changes or modify the technical contents disclosed above into equivalent embodiments without departing from the scope of the technical solution of the present invention. However, any brief modifications, equivalent changes and modifications made to the above embodiments based on the technical essence of the present invention without departing from the content of the technical solution of the present invention are still within the scope of the technical solution of the present invention.

Claims

1. A vacuum filtration device for producing bovine bilirubin, comprising a main base (1), characterized in that: A column (2) is fixedly mounted on the upper wall of the main base (1), a liquid collecting bucket (3) is fixedly mounted on the upper wall of the column (2), a pressure-maintaining liquid discharge structure is fixedly mounted on the lower end of the liquid collecting bucket (3), a filter cartridge (4) is mounted in the liquid collecting bucket (3), a stirring structure is mounted on the liquid collecting bucket (3), and a negative pressure generating structure is mounted on the liquid collecting bucket (3).

2. A vacuum filtration device for producing bovine bilirubin according to claim 1, characterized in that The pressure-maintaining liquid discharge structure comprises a liquid discharge pipe (5), an upper solenoid valve (6) and a lower solenoid valve (7), wherein the upper solenoid valve (6) and the lower solenoid valve (7) are fixedly mounted on the liquid discharge pipe (5), and the liquid discharge pipe (5) is fixedly mounted on the lower end of the liquid collecting hopper (3).

3. A vacuum filtration device for producing bovine bilirubin according to claim 1, characterized in that The filter cartridge (4) is a tube with an open ball head at one end. The bottom end and side wall of the filter cartridge (4) are provided with a mounting cage (8). A filtrate membrane (9) is installed in the filter cartridge (4). A sealing frame (10) is fixedly installed on the side wall of the filter cartridge (4). The sealing frame (10) is fixedly connected to the liquid collecting hopper (3). A liquid adding pipe (11) is fixedly installed on the sealing frame (10).

4. A vacuum filtration device for producing bovine bilirubin according to claim 1, characterized in that The stirring structure comprises a stirring frame (12), the stirring frame (12) is fixedly mounted on the upper wall of the liquid collecting hopper (3), a first motor (13), a gear reducer (14) and a stirring shaft (15) are fixedly mounted in the stirring frame (12), a stirring rod (16) is fixedly mounted at the lower end of the stirring shaft (15), a driving end of the first motor (13) is fixedly connected to an input end of the gear reducer (14), an active bevel gear (17) is fixedly mounted at an output end of the gear reducer (14), a driven bevel gear (18) is fixedly mounted on the stirring shaft (15), and the active bevel gear (17) is meshingly connected with the driven bevel gear (18).

5. A vacuum filtration device for producing bovine bilirubin according to claim 1, characterized in that The negative pressure generating structure comprises an air pump (19) and a safety box (20), wherein the air pump (19) and the safety box (20) are fixedly mounted on the column (2), the input end of the air pump (19) is connected to the safety box (20), and the safety box (20) is connected to the liquid collecting hopper (3).

6. A vacuum filtration device for producing bovine bilirubin according to claim 5, characterized in that A pressure gauge (21) is fixedly installed in the safety box (20), a sewage pipe (22) is fixedly installed at the lower end of the safety box (20), a safety valve (23) is arranged on the liquid collecting hopper (3), and a liquid retaining cylinder (24) is installed in the liquid collecting hopper (3).

Citation Information

Patent Citations

  • Precipitation filtering device for bilirubin preparation

    CN221412356U