Possine production sewage treatment device

Abstract

The utility model relates to glassine production sewage treatment, in particular to a glassine production sewage treatment device which comprises a filtering device and a drying tank, the filtering device comprises a closed filtering box, the filtering box is divided into a left side and a right side by a fixedly arranged ceramic membrane, and the left side of the filtering box is communicated with a blow-off pipe; the right side of the filter box communicates with the water inlet end of a water outlet pipe, the water outlet end of the water outlet pipe communicates with the water inlet end of the drying tank, and a discharging pipe controlled by a discharging valve is arranged on one side of the lower portion of the drying tank. With the adoption of the sodium gluconate recovery device, the collection of sodium gluconate can be realized in a manner of firstly filtering sewage and then crystallizing the sewage, and few impurities in the collected crystals are ensured, so that the normal use of the recovered sodium gluconate can be ensured, and the waste of energy sources is reduced.

Description

Technical Field

[0001] The utility model belongs to the sewage treatment of bosicerin production, and specifically relates to a sewage treatment device for bosicerin production. Background Art

[0002] Bosicerin is a xylose derivative with anti-aging active substances, which can promote the synthesis of collagen, make the skin stronger and more elastic, improve neck fine lines, and prevent aging. Bosicerin is a mixture of glycoproteins derived from xylose. Since xylose is abundantly present in beech trees and has the ability to promote the production of glucosaminoglycan, i.e., mucopolysaccharide. As bosicerin extracted from beech trees, its function is similar to that of xylose.

[0003] Among them, during the production of bosicerin, a large amount of sewage is generated, and the sewage contains a large amount of sodium gluconate. If the sodium gluconate is directly discharged, it will cause waste of energy. Content of the Utility Model

[0004] The utility model provides a sewage treatment device for bosicerin production to solve the defects in the prior art.

[0005] The utility model is realized through the following technical solutions:

[0006] A sewage treatment device for bosicerin production includes a filtering device and a drying tank. The filtering device includes a closed filtering box, which is separated into left and right sides by a fixedly arranged ceramic membrane. The left side of the filtering box is communicated with a sewage discharge pipe, and the right side of the filtering box is communicated with the water inlet end of a water outlet pipe. The water outlet end of the water outlet pipe is communicated with the water inlet end of the drying tank. One side of the lower part of the drying tank is provided with a discharge pipe controlled by a discharge valve.

[0007] When this application is in use, sewage enters the filtering box through the sewage discharge pipe. Among them, a ceramic membrane is arranged in the filtering box. Therefore, macromolecular substances are isolated, and the small molecule sodium gluconate dissolved in water smoothly passes through the ceramic membrane and enters the drying chamber through the water outlet pipe for drying and crystallization. After the crystallization is completed, it flows out from the discharge pipe, thereby realizing the collection of sodium gluconate, ensuring that the collected crystal has few impurities, so as to ensure that the recovered sodium gluconate can be used normally and reduce energy waste.

[0008] Preferably, several drying tanks are provided. The water outlet end of the water outlet pipe is communicated with a longitudinal main pipe, and the longitudinal main pipe is horizontally communicated with several branch pipes. Solenoid valves are arranged on the branch pipes, and the water outlet ends of the branch pipes are respectively communicated with the water inlet ends of the corresponding drying tanks. The setting of multiple drying tanks can ensure that when one drying tank is cleaning the crystallized sodium gluconate after drying, another drying tank is working for drying operation, so as to ensure continuous drying and improve work efficiency.

[0009] Preferably, the upper part of the drying tank is detachably sealed with a tank cover. One end of an exhaust pipe communicates with the center of the top surface of the tank cover. The other end of the exhaust pipe is connected to the intake end of an outlet pipe through a flange. A condensation chamber is provided on one side of the drying tank. The outlet end of the outlet pipe is inserted into the condensed water in the condensation chamber. A water pump is provided in the condensation chamber. The water outlet end of the water pump communicates with one end of a thin pipe. The other end of the thin pipe penetrates into the right side of the filtration tank and the penetration point is sealed. A discharge port controlled by a valve is provided at the lower left part of the filtration tank. A control valve is provided on the outlet pipe. The condensation chamber can recover the water vapor generated by the drying tank. At the same time, after the recovery is completed, when filtration is not carried out, the ceramic membrane is backwashed, which not only saves water resources, but also can clean the ceramic membrane to prevent it from being blocked after long-term use.

[0010] Preferably, the thin pipe is vertically inserted into the filtration tank, and the lower end is fixedly connected to the inner wall of the filtration tank and sealed by the inner wall of the filtration tank. Several spray heads are vertically communicated with the thin pipe, and the spray heads face the ceramic membrane. Multiple spray heads can wash the ceramic membrane up and down to ensure more thorough cleaning.

[0011] Preferably, a rotating rod is provided in the drying tank. The rotating rod is located on the vertical axis of the drying tank, and the lower end of the rotating rod penetrates out of the drying tank and is rotatably connected to the drying tank through a sealing bearing. The rotating rod is vertically connected with a cross bar. The outer end of the cross bar is vertically connected with a scraper in contact with the inner wall of the drying tank. A driven gear is sleeved on the lower end of the rotating rod. The bottom surface of the drying tank is fixedly connected with a motor. The motor shaft is sleeved with a driven gear meshed with a driving gear. Through holes are provided on the scraper. The rotation of the motor shaft drives the rotation of the driving gear, the rotation of the driving gear drives the rotation of the driven gear, thereby driving the rotation of the rotating rod. The rotation of the rotating rod drives the scraper to rotate along the axis of the rotating rod, which not only realizes the stirring of the water in the heating tank before crystallization to accelerate crystallization, but also can clean the inner wall of the drying tank after crystallization to prevent crystals from sticking to the inner wall of the drying tank.

[0012] Preferably, it further includes a U-shaped material receiving channel, which is inclined downward from back to front and is located below the discharge pipes of all drying tanks. The material receiving channel can realize the unified collection of all crystallized sodium gluconate.

[0013] The beneficial effects of the present utility model are as follows: By filtering the sewage first and then crystallizing it, the present application can collect sodium gluconate and ensure that the collected crystals have few impurities, so as to ensure that the recovered sodium gluconate can be used normally and reduce energy waste. Description of the Drawings

[0014] To more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the following will briefly introduce the attached drawings required for the description of the embodiments or the prior art. Obviously, the attached drawings in the following description are some embodiments of the present invention. For those of ordinary skill in the art, without creative efforts, other attached drawings can also be obtained based on these attached drawings.

[0015] Figure 1 is a schematic structural diagram of the present invention;

[0016] Figure 2 is a layout schematic diagram of several drying tanks.

[0017] As shown in the figure:

[0018] 1. Drying tank, 2. Filter box, 3. Ceramic membrane, 4. Water outlet pipe, 5. Longitudinal main pipe, 6. Branch pipe, 7. Tank cover, 8. Exhaust pipe, 9. Condensation chamber, 10. Sprayer, 11. Thin pipe, 12. Rotating rod, 13. Scraper, 14. Through hole, 15. Driving gear, 16. Driven gear, 17. Motor, 18. Feeding channel. Specific embodiments

[0019] To make the objectives, technical solutions, and advantages of the embodiments of the present invention clearer, the following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the attached drawings in the embodiments of the present invention. Obviously, the described embodiments are some, but not all, of the embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts fall within the scope of protection of the present invention.

[0020] A hydroxyprogesterone caproate production sewage treatment device, as Figure 1 and Figure 2 shown. It includes a filtering device and a plurality of drying tanks 1 arranged. The filtering device includes a closed filter box 2, and the filter box 2 is separated into left and right sides by a fixedly arranged ceramic membrane 3. The left side of the filter box 2 is communicated with a sewage discharge pipe, and the right side of the filter box 2 is communicated with the water inlet end of a water outlet pipe 4. The water outlet end of the water outlet pipe 4 is communicated with a longitudinal main pipe 5, and the longitudinal main pipe 5 is horizontally communicated with several branch pipes 6. Solenoid valves are provided on the branch pipes 6, and the water outlet ends of the branch pipes 6 are respectively communicated with the water inlet ends of the corresponding drying tanks 1. A discharge pipe controlled by a discharge valve is provided on one side of the lower part of the drying tank 1.

[0021] When this application is in use, sewage enters the filtration tank 2 through the sewage discharge pipe. Among them, a ceramic membrane 3 is provided in the filtration tank 2. Therefore, macromolecular substances are isolated, and the small-molecule sodium glucuronate dissolved in water smoothly passes through the ceramic membrane 3 and enters the drying chamber through the water outlet pipe 4 for drying and crystallization. After the crystallization is completed, it flows out from the discharge pipe, thereby realizing the collection of sodium glucuronate. This ensures that the collected crystals have few impurities, so that the recovered sodium glucuronate can be used normally and the waste of energy is reduced. And multiple drying tanks 1 are provided, which can ensure that when one of them is cleaning the crystallized sodium glucuronate after drying, the other drying tank 1 is working for drying operation, so as to ensure continuous drying and improve work efficiency.

[0022] The upper part of the drying tank 1 is detachably sealed with a tank cover 7. One end of an exhaust pipe 8 communicates with the center of the top surface of the tank cover 7. The other end of the exhaust pipe 8 is connected to the intake end of the outlet pipe through a flange. A condensation chamber 9 is provided on one side of the drying tank 1. The outlet end of the outlet pipe is inserted into the condensed water in the condensation chamber 9. A water pump is provided in the condensation chamber 9. The water outlet end of the water pump communicates with one end of a thin pipe 11. The thin pipe 11 vertically downwardly inserts into the filtration tank 2 and the lower end is fixedly connected to the inner wall of the filtration tank 2 and is blocked by the inner wall of the filtration tank 2. Several nozzles 10 are vertically communicated with the thin pipe 11, and the nozzles 10 face the ceramic membrane 3. A discharge port controlled by a valve is opened in the lower left part of the filtration tank 2, and a control valve is provided on the water outlet pipe 4. The condensation chamber 9 can recover the water vapor generated by the drying tank 1. At the same time, after the recovery is completed, when filtration is not carried out, it can backwash the ceramic membrane 3, and the backwashing water can be discharged through the discharge port. Furthermore, not only water resources are saved, but also the ceramic membrane 3 can be cleaned to prevent it from being blocked after long-term use. Among them, the control valve on the water outlet pipe 4 can prevent the condensed water tank for cleaning from flowing in the direction of the water outlet pipe 4. The drying tank 1 and the tank cover 7 are detachable, and the exhaust pipe 8 and the outlet pipe are detachable through a flange, which can ensure that after crystallization, the sodium glucuronate crystals in the drying tank 1 can be removed through the tank cover 7 for collection. Multiple nozzles 10 can realize upper and lower flushing of the ceramic membrane 3 to ensure more thorough cleaning.

[0023] Inside the drying tank 1, there is a rotating rod 12. The rotating rod 12 is located on the vertical axis of the drying tank 1, and the lower end of the rotating rod 12 passes through the drying tank 1 and is rotationally connected to the drying tank 1 through a sealing bearing. The rotating rod 12 is vertically connected with a cross bar, and the outer end of the cross bar is vertically connected with a scraping plate 13 that contacts the inner wall of the drying tank 1. A driven gear 16 is sleeved on the lower end of the rotating rod 12. The bottom surface of the drying tank 1 is fixedly connected with a motor 17, and a driven gear 16 meshing with a driving gear 15 is sleeved on the rotating shaft of the motor 17. Through holes 14 are formed in the scraping plate 13. The rotation of the rotating shaft of the motor 17 drives the rotation of the driving gear 15, the rotation of the driving gear 15 drives the rotation of the driven gear 16, thereby driving the rotation of the rotating rod 12. The rotation of the rotating rod 12 drives the scraping plate 13 to rotate along the axis of the rotating rod 12. This not only realizes the stirring of the water in the heating tank before crystallization to accelerate crystallization, but also can clean the inner wall of the drying tank 1 after crystallization to prevent crystals from sticking to the inner wall of the drying tank 1. The through holes can reduce the resistance of water when the scraping plate stirs.

[0024] It further includes a U-shaped material receiving channel 18. The material receiving channel 18 slopes downward from back to front and is located below the discharge pipes of all drying tanks 1. The material receiving channel 18 can realize the unified collection of all crystallized sodium gluconate.

[0025] The use of this application can realize the collection of sodium gluconate by first filtering and then crystallizing the sewage, and ensure that the collected crystals have few impurities, so as to ensure that the recovered sodium gluconate can be used normally and reduce the waste of energy.

[0026] Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit them; although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that they can still modify the technical solutions described in the foregoing embodiments, or perform equivalent replacements for some of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the spirit and scope of the technical solutions of the embodiments of the present invention.

Claims

1. A Bose-producing wastewater treatment device, characterized in that: It includes a filtering device and a drying tank. The filtering device includes a closed filtering box. The filtering box is divided into left and right sides by a fixed ceramic membrane. The left side of the filtering box is connected to a sewage pipe, and the right side of the filtering box is connected to a water inlet end of a water outlet pipe. The water outlet end of the water outlet pipe is connected to the water inlet end of the drying tank. A discharge pipe controlled by a discharge valve is provided on one side of the lower part of the drying tank.

2. The Bose-producing wastewater treatment device according to claim 1 is characterized in that: There are several drying tanks, the water outlet end of the water outlet pipe is connected to a longitudinal main pipe, the longitudinal main pipe is horizontally connected to several branch pipes, the branch pipes are provided with solenoid valves, and the water outlet ends of the branch pipes are respectively connected to the water inlet ends of the corresponding drying tanks.

3. The Bose-producing wastewater treatment device according to claim 2 is characterized in that: The upper part of the drying tank is detachably sealed with a tank cover, one end of the exhaust pipe is connected to the center of the top surface of the tank cover, the other end of the exhaust pipe is connected to the air inlet end of the air outlet pipe through a flange, a condensation chamber is provided on one side of the drying tank, the air outlet end of the air outlet pipe is inserted into the condensed water in the condensation chamber, a water pump is provided in the condensation chamber, the water outlet end of the water pump is connected to one end of a thin tube, the other end of the thin tube penetrates into the right side of the filter box and the penetration is closed, a discharge port controlled by a valve is opened at the lower left side of the filter box, and a control valve is provided on the water outlet pipe.

4. The Bose-producing wastewater treatment device according to claim 3 is characterized in that: The thin tube is vertically inserted downward into the filter box, and the lower end is fixedly connected to the inner wall of the filter box and sealed by the inner wall of the filter box. The thin tube is vertically connected to several nozzles, and the nozzles face the ceramic membrane.

5. The Bose-producing wastewater treatment device according to claim 3 is characterized in that: A rotating rod is provided in the drying tank. The rotating rod is located on the vertical axis of the drying tank, and the lower end of the rotating rod passes through the drying tank and is rotatably connected to the drying tank through a sealed bearing. The rotating rod is vertically connected to a cross bar, and the outer end of the cross bar is vertically connected to a scraper in contact with the inner wall of the drying tank. The lower end of the rotating rod is sleeved with a driven gear, and a motor is fixedly connected to the bottom surface of the drying tank. The motor shaft is sleeved with a driven gear meshing with the driving gear, and a through hole is opened on the scraper.

6. The Bose-producing wastewater treatment device according to claim 2 is characterized in that: The utility model also comprises a U-shaped material receiving channel, which is inclined downward from the back to the front and is located below the material discharging pipes of all drying tanks.

Images