Carclazyte bed in anthraquinone process hydrogen peroxide production process
By designing the upper and lower elliptical head sealing structure in the clay bed, setting up a liquid distributor and automatic discharger, the problems of high labor intensity of workers and clogging of activated alumina balls in the clay bed loading and unloading operations are solved, and fast and convenient operation and improved production efficiency and product quality are achieved.
Patent Information
- Application Number
- CN202421666746.1
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-07-15
- Publication Date
- 2025-05-16
- Estimated Expiration
- 2034-07-15
AI Technical Summary
During the loading and unloading operations, workers need to enter the confined space many times, which is labor-intensive, and the activated alumina balls are pulverized and agglomerated, causing clogging, affecting production efficiency and product quality.
A clay bed in the anthraquinone hydrogen peroxide production process is designed, and an upper and lower elliptical head sealing structure is adopted, a liquid distributor and an automatic discharger are installed, and a stainless steel trapezoidal wire mesh filter tube is used to prevent activated alumina balls from entering the pipeline.
It realizes the quick and convenient operation of activated alumina ball loading and unloading, reduces labor intensity, extends the use time and replacement cycle of white soil, and improves the production efficiency and product quality of hydrogen peroxide.
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Figure CN222871399U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to a white clay bed in the anthraquinone process for producing hydrogen peroxide. Background Art
[0002] The main defect of the conventional structure used in large quantities in the early stage of hydrogen peroxide development is that workers have to enter the confined space many times to work during filling or unloading. The packing plate, stainless steel wire mesh, inert porcelain balls, etc. are all heavy materials and components, which makes the workers' labor intensity very high and takes a long time to operate. The inert porcelain balls at the bottom of the lower head only play a supporting role, but if they are not replaced for a long time, the activated alumina balls (white clay) will be pulverized and agglomerated, which will increase the difficulty of disassembly and block the distribution holes of the liquid inlet distributor. The outlet cover at the drain port position of the lower head is generally made of a structure with a stainless steel plate cutting the drainage hole and covering it with a stainless steel wire mesh. It will also be blocked by the powdering and agglomeration of the white clay, resulting in poor drainage, and the working efficiency of the white clay bed will be greatly reduced.
[0003] The main defect of another kind of clay bed structure is that the supporting inert porcelain ball at the bottom of the lower head is eliminated on the basis of the conventional structure, and the structure of the grid and supporting parts (including I-beam, supporting ring, supporting grid) is used instead. The structure above it remains unchanged, but the construction process of loading and unloading is the same, and workers also need to enter the confined space for many times to work, which is labor-intensive. In this structure, the working fluid at the bottom of the lower head hardly flows upward and does not participate in the circulation, resulting in a waste of working fluid utilization, while increasing production costs and not fully utilizing the tower space.
[0004] The liquid distributors and outlet converging devices of the above two structures are both pipe-type with holes opened on stainless steel pipes. The hole diameters range from Φ10 to Φ30. Although the distribution pipes are covered with high-mesh stainless steel wire mesh, they are broken due to long-term extrusion and excessively fine wire diameters. In the production process, inert porcelain balls and white clay have the risk of falling into the pipes and blocking the pipes. Due to the limitations of its production method, the number of holes and pipes of the stainless steel pipe pipe-type distributor cannot evenly distribute the working fluid. If there are too many pipes, the production cost will be greatly increased. Utility Model Content
[0005] The utility model is a clay bed in the anthraquinone method hydrogen peroxide production process, which is convenient for loading and unloading activated alumina balls (clay), and is fast and convenient, labor-saving, safe and stable. It improves the efficiency and product quality of hydrogen peroxide production, increases the filling rate of activated alumina balls (clay) in the clay bed, and prolongs the service life and replacement cycle of activated alumina (clay).
[0006] In order to achieve the above purpose, the technical solution adopted by the utility model is:
[0007] A clay bed in an anthraquinone method hydrogen peroxide production process, characterized in that: the upper and lower ends of the cylinder are sealed and fixed by an upper elliptical head and a lower elliptical head respectively, a liquid distributor feed pipe is provided through one side wall of the cylinder, and a manhole is provided on the other side wall of the cylinder;
[0008] The upper elliptical head is provided with an activated alumina ball filling port for pouring the activated alumina balls into the cylinder body, and the upper elliptical head is also provided with a liquid outlet, and a liquid outlet collector is provided at the bottom of the liquid outlet, and the liquid outlet collector is used to collect the working liquid and flow out through the liquid outlet;
[0009] A drain collector and a liquid distributor are respectively arranged in the lower elliptical head, the drain collector is connected with a drain port, the drain port is used to empty the working liquid in the cylinder before unloading, the liquid distributor is connected with a feed pipe of the liquid distributor, the working liquid flows through the feed pipe of the liquid distributor, and flows into the activated alumina balls through the liquid distributor, and an automatic unloader of activated alumina balls is arranged at the bottom of the lower elliptical head for unloading the activated alumina balls in the cylinder;
[0010] The drain collector, the liquid distributor and the liquid outlet collector are respectively composed of stainless steel trapezoidal wire mesh filter tubes to prevent the activated alumina balls from entering.
[0011] The white clay bed in the anthraquinone method hydrogen peroxide production process, wherein: the liquid distributor feed pipe includes a main pipe and a steering connecting pipe, the main pipe is penetrated through a side wall of the cylinder, the main pipe is connected to the steering connecting pipe, and the steering connecting pipe is connected to the liquid distributor.
[0012] The white clay bed in the anthraquinone method hydrogen peroxide production process, wherein: the liquid distributor comprises an upper distributor and a lower distributor, and the upper distributor and the lower distributor are arranged in a relatively staggered manner.
[0013] The beneficial effects of the utility model are as follows: the loading and unloading of activated alumina balls (clay) is quick and convenient, labor-saving, safe and stable. The efficiency and product quality of hydrogen peroxide production are improved, the filling rate of activated alumina balls (clay) in the clay bed is increased, and the service life and replacement cycle of activated alumina (clay) are extended. BRIEF DESCRIPTION OF THE DRAWINGS
[0014] Figure 1 This is a structural diagram of the white clay bed in the anthraquinone method of hydrogen peroxide production process.
[0015] Figure 2 The present invention is a structural diagram of a liquid distributor and a liquid distributor feed pipe of a kaolin bed in anthraquinone method hydrogen peroxide production process.
[0016] Figure 3 This is a top view of the structure of the liquid distributor of the white clay bed in the anthraquinone method hydrogen peroxide production process.
[0017] Figure 4 This is a top view of the structure of the upper distributor of the white clay bed in the anthraquinone method hydrogen peroxide production process.
[0018] Figure 5 This is a top view of the structure of the lower distributor of the white clay bed in the anthraquinone method of hydrogen peroxide production process.
[0019] Figure 6 This is a structural diagram of the liquid outlet collector of the clay bed in the anthraquinone method hydrogen peroxide production process.
[0020] Figure 7 This is a structural diagram of the drain collector of the bleaching clay bed in the anthraquinone method of hydrogen peroxide production process.
[0021] Figure 8 for Figure 5 , Figure 6 , Figure 7 Enlarged view of part I in the middle.
[0022] Explanation of the reference numerals: 1-cylinder body; 2-lower elliptical head; 3-drain port; 4-automatic unloader of activated alumina balls; 5-drain collector; 6-liquid distributor; 7-feed pipe of liquid distributor; 8-loading port of activated alumina balls; 9-liquid outlet collector; 10-liquid outlet; 11-upper elliptical head; 12-activated alumina balls; 13-manhole; 14-main pipe; 15-steering connecting pipe; 16-upper distribution pipe; 17-lower distribution pipe; 18-stainless steel trapezoidal wire mesh filter pipe. DETAILED DESCRIPTION
[0023] like Figures 1 to 8 The clay bed in the anthraquinone method hydrogen peroxide production process is characterized in that: the upper and lower ends of the cylinder 1 are sealed and fixed by an upper elliptical head 11 and a lower elliptical head 2 respectively, a liquid distributor feed pipe 7 is penetrated on one side wall of the cylinder 1, and a manhole 13 is provided on the other side wall of the cylinder 1 for personnel to enter and exit for work.
[0024] The upper elliptical head 11 is provided with an activated alumina ball filling port 8 for pouring the activated alumina balls 12 into the cylinder 1. The upper elliptical head 11 is also provided with a liquid outlet 10, and a liquid outlet collector 9 is provided at the bottom of the liquid outlet 10. The liquid outlet collector 9 is used to collect the working fluid and let it flow out through the liquid outlet 10.
[0025] A drain collector 5 and a liquid distributor 6 are respectively arranged in the lower elliptical head 2, and the drain collector 5 is connected with the drain port 3, and the drain port 3 is used to drain the working fluid in the cylinder 1 before unloading. The liquid distributor 6 includes an upper distributor 16 and a lower distributor 17, and the upper distributor 16 and the lower distributor 17 are relatively staggered. The liquid distributor 6 is connected with the liquid distributor feed pipe 7, and the liquid distributor feed pipe 7 includes a main pipe 14 and a steering connecting pipe 15. The main pipe 14 is penetrated through one side wall of the cylinder 1, and the main pipe 14 is connected with the steering connecting pipe 15, and the steering connecting pipe 15 is connected with the liquid distributor 6. The working fluid flows through the main pipe 14 and the steering connecting pipe 15, and flows into the activated alumina balls 12 through the liquid distributor 6. An activated alumina ball automatic unloader 4 is arranged at the bottom of the lower elliptical head 2 for unloading the activated alumina balls 12 in the cylinder 1.
[0026] The drain collector 5, the liquid distributor 6 and the liquid outlet collector 9 are respectively composed of a stainless steel trapezoidal wire mesh filter tube 18, the trapezoidal wire mesh has a small spiral pitch, a large distribution surface, and is distributed in all directions, which can not only improve the distribution efficiency, but also ensure that the activated alumina balls will not enter the pipeline, avoiding the risk of damage to valves, water pumps, instruments, etc. in the pipeline network, and is safe and reliable.
[0027] In the embodiment, the drain port 3, the automatic unloader of activated alumina balls 4 and the manhole 13 are closed, the activated alumina ball loading port 8 is opened, and the activated alumina balls 12 are poured into the cylinder 1 through the activated alumina ball loading port 8 by lifting. After the balls are naturally flattened below the activated alumina ball loading port 8, the activated alumina ball loading port 8 is closed to complete the loading operation.
[0028] After the working fluid flows through the main pipe 14 and the turning connecting pipe 15, it flows into the activated alumina ball 12 through the upper distribution pipe 16 and the lower distribution pipe 17. After the activated alumina ball 12 completes the adsorption process, the working fluid flows upward into the liquid outlet collector 9 and flows out of the cylinder 1 through the liquid outlet 10, completing the production process.
[0029] Before unloading, the drain port 3 is opened first, and after the remaining working fluid in the cylinder 1 is emptied, steam is connected to the cylinder 1 to dry the activated alumina balls 12. After drying, the automatic unloader 4 of the activated alumina balls is opened to unload, and the unloaded activated alumina balls 12 are transported to the specified placement point and wait for recycling.
[0030] The above description is only illustrative and not restrictive of the present invention. Those skilled in the art will understand that many modifications, changes or equivalents may be made without departing from the spirit and scope defined by the claims, but all will fall within the scope of protection of the present invention.
Claims
1. A clay bed in an anthraquinone process for producing hydrogen peroxide, characterized in that: The upper and lower ends of the cylinder (1) are sealed and fixed by an upper elliptical head (11) and a lower elliptical head (2) respectively; a liquid distributor feed pipe (7) is provided through one side wall of the cylinder (1); and a manhole (13) is provided on the other side wall of the cylinder (1); The upper elliptical head (11) is provided with an activated alumina ball filling port (8) for pouring the activated alumina balls (12) into the cylinder (1); the upper elliptical head (11) is also provided with a liquid outlet (10) extending therethrough; a liquid outlet collector (9) is provided at the bottom end of the liquid outlet (10); the liquid outlet collector (9) is used to collect the working fluid and allow the working fluid to flow out through the liquid outlet (10); A drain collector (5) and a liquid distributor (6) are respectively arranged in the lower elliptical head (2); the drain collector (5) is connected to the drain port (3); the drain port (3) is used to drain the working liquid in the cylinder (1) before unloading; the liquid distributor (6) is connected to the liquid distributor feed pipe (7); the working liquid flows through the liquid distributor feed pipe (7) and flows into the activated alumina balls (12) through the liquid distributor (6); an activated alumina ball automatic discharger (4) is arranged at the bottom of the lower elliptical head (2) for discharging the activated alumina balls (12) in the cylinder (1); The drain collector (5), the liquid distributor (6) and the liquid outlet collector (9) are respectively composed of a stainless steel trapezoidal wire mesh filter tube (18) to prevent the activated alumina balls (12) from entering.
2. The clay bed in the anthraquinone method hydrogen peroxide production process according to claim 1, characterized in that: The liquid distributor feed pipe (7) comprises a main pipe (14) and a steering connecting pipe (15). The main pipe (14) is arranged through a side wall of the cylinder (1). The main pipe (14) is connected to the steering connecting pipe (15), and the steering connecting pipe (15) is connected to the liquid distributor (6).
3. The clay bed in the anthraquinone method hydrogen peroxide production process according to claim 1, characterized in that: The liquid distributor (6) comprises an upper distributor (16) and a lower distributor (17), and the upper distributor (16) and the lower distributor (17) are arranged in a relatively staggered manner.