Continuous production method and equipment for preparing antimony pentoxide
By using continuous production equipment and automated filtration mechanisms, the problems of uneven mixing and heating of raw materials in the preparation of antimony pentoxide have been solved, achieving efficient and stable continuous production and automated filtration of antimony pentoxide, thereby improving product quality and production efficiency.
Patent Information
- Application Number
- CN202511485838.9
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-10-17
- Publication Date
- 2026-01-20
- Estimated Expiration
- Not applicable · inactive patent
AI Technical Summary
Existing methods for preparing antimony pentoxide suffer from uneven mixing of raw materials and uneven heating, leading to uneven reactions. Furthermore, the production process is intermittent, making it difficult to achieve efficient, stable, and continuous production.
The system employs continuous production equipment, precisely controlling the mixing ratio of raw materials through a feed pump and flow control valve. A mixing and heating mechanism ensures uniform heating, and an automated filtration mechanism enables continuous production and filtration.
This process achieves uniform mixing and thorough heating of raw materials, improving reaction efficiency and product quality. It also enables continuous production and automated filtration of antimony pentoxide, thereby enhancing production efficiency and product quality.
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Figure CN121361831A_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The present application relates to a production technology of antimony pentoxide colloid, in particular to a continuous production method and equipment for preparing antimony pentoxide. BACKGROUND
[0002] As an important inorganic compound, antimony pentoxide has a wide range of applications in various fields. For example, in the flame retardant industry, it can effectively improve the flame retardant performance of materials and ensure safety in use; in the catalyst field, it can be used as a catalyst or catalyst carrier for various chemical reactions to promote the reaction; in the glass manufacturing industry, it can improve the optical performance and chemical stability of glass. Therefore, efficient and stable preparation of antimony pentoxide has important economic value and practical significance.
[0003] Currently, the commonly used method is to mix antimony trioxide solution with a stabilizer, then add hydrogen peroxide solution and heat to make the antimony trioxide solution react with the hydrogen peroxide solution to produce antimony pentoxide colloid, and then stabilize the produced colloid with the stabilizer. This preparation method has some deficiencies in the preparation process, which seriously restricts the production efficiency and product quality of antimony pentoxide.
[0004] For example, in the aspect of raw material mixing, a simple mixing method is usually used, which leads to uneven mixing of raw materials, resulting in poor production reaction effect. At the same time, the heating process is also a big bottleneck of existing preparation technology. The traditional heating method often cannot heat the reaction raw materials sufficiently and uniformly, which easily causes local overheating. Local overheating can cause a series of adverse consequences. On the one hand, it may cause decomposition and other side reactions of raw materials, producing unnecessary by-products and reducing the yield of target product antimony pentoxide; on the other hand, uneven heating will lead to uneven temperature distribution in the reaction system, affecting the reaction rate and equilibrium, making the reaction difficult to proceed under ideal conditions, and finally leading to unstable product quality. For example, in some preparation methods that directly heat the reaction container, the temperature difference between the edge and center of the container is large, resulting in uneven size of the generated antimony pentoxide particles and obvious performance difference.
[0005] In addition, most of the existing preparation methods are batch production, which has obvious limitations. Batch production needs to stop the reaction after each production cycle, perform product collection, equipment cleaning and other operations, and then start the production of the next cycle. This not only leads to low production efficiency and increases production cost, but also makes it difficult to realize large-scale and continuous production.
[0006] In summary, the preparation method and equipment of antimony pentoxide in the prior art have many deficiencies in raw material mixing, heating, production mode and the like, and it is difficult to meet the market demand for efficient and stable production of antimony pentoxide. Therefore, it has important practical significance to develop a preparation method and equipment of antimony pentoxide which can accurately control the uniform mixing of raw materials, realize uniform heating, continuous production and have efficient automatic filtering function. SUMMARY
[0007] The purpose of the present application is to provide a continuous production method and equipment for preparing antimony pentoxide to solve the above-mentioned deficiencies in the prior art.
[0008] In order to achieve the above-mentioned purpose, the present application provides the following technical solutions: A continuous production method for preparing antimony pentoxide, characterized in that it comprises the following steps: Step one, uniformly mix the antimony trioxide solution and the stabilizer solution, and put the mixed solution into the A feeding barrel; put the hydrogen peroxide solution into the B feeding barrel; Step two, connect the feeding end of the continuous production equipment with the A feeding barrel and the B feeding barrel, start the antimony pentoxide colloid production device, and the continuous production equipment prepares the antimony pentoxide colloid; Step three, concentrate the antimony pentoxide colloid prepared in step two to obtain the antimony pentoxide colloid.
[0009] A continuous production equipment, the antimony pentoxide colloid production device comprises a mounting table, a plurality of reaction bends are fixedly connected on the mounting table, two feeding pumps are fixedly connected on the top of the mounting table, a first feeding pipe is fixedly connected to the output end of the feeding pump, a plurality of second feeding pipes fixedly connected with the reaction bends are fixedly connected to the outer surface of the two first feeding pipes, a flow control valve is arranged on the second feeding pipe, a discharge pipe is fixedly connected on the mounting table, and the discharge pipe is fixedly connected with the reaction bends through a pipeline; The mixing and heating mechanism connected with the mounting table is arranged on the reaction bend, which is used for mixing and heating the raw materials, one end of the discharge pipe is fixedly connected with the antimony pentoxide colloid filtering mechanism connected with the mounting table, and the antimony pentoxide colloid filtering mechanism is used for filtering out the reacted antimony pentoxide colloid.
[0010] Further, the mixed heating mechanism comprises a first rotating driving element fixedly connected with the mounting table, an output end of the first rotating driving element is fixedly connected with a first transmission shaft, an outer surface of the first transmission shaft is drivingly connected with two first transmission pipes in rotation with the reaction elbow through a transmission wheel and a transmission belt, the outer surfaces of the first transmission pipes are fixedly sleeved with first gears, the outer surfaces of the first gears are meshingly connected with second gears, the middle of the second gears is fixedly sleeved with a second transmission shaft in rotation with the reaction elbow, an outer surface of the second transmission shaft is drivingly connected with a second transmission pipe in rotation with the reaction elbow through a transmission wheel and a transmission belt, and the outer surfaces of the first transmission pipe and the second transmission pipe are fixedly connected with first spiral rods. The first transmission pipe and the second transmission pipe are both provided with a heat supply mechanism connected with the mounting table, and the heat supply mechanism is used for heating the raw materials in the reaction elbow.
[0011] Further, the heat supply mechanism comprises a heating spiral elbow fixedly connected with the first transmission pipe and the second transmission pipe, the top and the bottom of the first transmission pipe and the second transmission pipe are both fixedly connected with two water isolation blocks, the top ends of the first transmission pipe and the second transmission pipe are both rotatably connected with first connecting pipes, one end of each first connecting pipe is fixedly connected with a drain pipe, one end of the drain pipe is fixedly connected with a water heating device, an output end of the water heating device is fixedly connected with a water supply pump through a pipeline, an output end of the water supply pump is fixedly connected with a water supply pipe, the bottom ends of the first transmission pipe and the second transmission pipe are both rotatably connected with second connecting pipes, and the second connecting pipes are connected with the water supply pipe.
[0012] Further, one end of the drain pipe is fixedly connected with a second rotating driving element, an output end of the second rotating driving element is fixedly connected with a second spiral rod in rotation with the drain pipe through a shaft coupling.
[0013] Further, the antimony pentoxide colloidal filtering mechanism comprises a buffer tank fixedly connected with the drain pipe, a discharge pipe is fixedly connected with the bottom end of the buffer tank, an electromagnetic valve is arranged on the discharge pipe, the bottom end of the discharge pipe is rotatably connected with a mounting pipe in rotation with the mounting table, a third rotating driving element is fixedly connected with the mounting table, an output end of the third rotating driving element is fixedly connected with a third transmission shaft, an outer surface of the third transmission shaft is drivingly connected with the mounting pipe through a transmission wheel and a transmission belt, and a filtering mechanism is drivingly connected with the bottom end of the mounting pipe, and the filtering mechanism is used for filtering the liquid discharged from the mounting pipe.
[0014] Further, the filtering mechanism comprises a support table, a support shaft is rotatably connected to the support table, a fourth rotating drive is fixedly connected to the bottom end of the support shaft and fixedly connected to the support table, a first telescopic drive is fixedly connected to the top end of the support shaft through a connecting plate, two mounting racks are fixedly connected to the output end of the first telescopic drive through a connecting plate, a turnover shaft is arranged in the mounting rack, a driving mechanism connected with the mounting rack is drivingly connected to the outer surface of the turnover shaft, a filter box is fixedly connected to one end of the turnover shaft, a transmission disc is rotatably connected to the filter box, a first filter mesh ring is fixedly connected to the top of the transmission disc, a second filter mesh ring fixedly connected with the transmission disc is fixedly connected to the first filter mesh ring, ultrafiltration membranes are fixedly connected to the inner surfaces of the first filter mesh ring and the second filter mesh ring, a connecting iron ring is fixedly connected to the top of the second filter mesh ring, and an electromagnet ring is fixedly connected to the bottom of the mounting pipe.
[0015] Further, the driving mechanism comprises a second telescopic drive fixedly connected with the mounting rack, a transmission rack is fixedly connected to the output end of the second telescopic drive through a connecting block, and a transmission gear fixedly sleeved with the turnover shaft is meshingly connected to one side of the transmission rack.
[0016] Further, a guide rod is fixedly connected to the top of the transmission disc, a cleaning ring slidingly connected with the ultrafiltration membrane is slidingly connected to the outer surface of the guide rod, and a cleaning soft brush is fixedly connected to the outer surface of the cleaning ring.
[0017] Further, a counterweight is fixedly connected to one side of the cleaning ring.
[0018] Compared with the prior art, the continuous production method and equipment for preparing antimony pentoxide provided by the application have the following beneficial effects: (1) The two kinds of raw materials are accurately and proportionally fed into the reaction elbow pipe through the feed pump and the flow control valve, the first rotating drive drives the transmission pipe and the screw rod to rotate in the mixing and heating mechanism, so that the raw materials smoothly flow and fully mix and stir in the reaction elbow pipe, and the reaction is promoted. At the same time, the heating mechanism gradually increases the heating temperature from left to right, and fully and uniformly heats the raw materials, so as to avoid local overheating to generate byproducts and ensure the purity of the reaction. In addition, the second rotating drive in the discharge pipe drives the screw rod to transport the mixed raw materials again, so as to realize continuous and sufficient reaction, the generated antimony pentoxide colloid is stabilized by the stabilizer, the reaction effect and efficiency are greatly improved, and the product quality is improved.
[0019] (2) The fourth rotating driving member drives the mounting frame to rotate, so that the filter box is alternately located below the mounting pipe, and the electromagnet ring is used for quick fixing. The third rotating driving member drives the mounting pipe and the filter box to rotate, and centrifugal force is used to make the liquid pass through the ultrafiltration membrane for twice sufficient filtration. After a period of filtration, the filter box can be switched for continuous filtration, and the used filter box can be cleaned. The second telescopic driving member drives the transmission rack to reciprocate, so that the filter box reciprocates and turns over, and the cleaning ring cleans the surface of the filter ring under the action of gravity and pours out, realizing continuous automatic filtration and cleaning and collection, and further improving the production efficiency of the antimony pentoxide colloid. BRIEF DESCRIPTION OF DRAWINGS
[0020] In order to more clearly illustrate the technical solutions in the embodiments of the present application or the prior art, the drawings needed in the embodiments will be briefly introduced as follows. Obviously, the drawings in the following description are only some embodiments described in the present application, and other drawings can also be obtained by those skilled in the art according to these drawings.
[0021] Figure 1 It is a first perspective view of the external structure of the present application. Figure 2 It is a second perspective view of the external structure of the present application. Figure 3 It is a perspective view of the internal structure of the reaction elbow of the present application. Figure 4 It is a perspective view of the internal structure of the filter box of the present application. Figure 5 It is a perspective view of the internal structure of the filter box of the present application. Figure 1 It is an enlarged view of A in the present application. Figure 6 It is an enlarged view of B in the present application. Figure 1 Figure 7 It is an enlarged view of C in the present application. Figure 1
[0022] Explanation of reference signs: 1, installation platform; 2, reaction elbow; 3, feed pump; 4, first feed pipe; 5, second feed pipe; 6, flow control valve; 7, discharge pipe; 11, first rotary drive; 12, first transmission shaft; 13, first transmission pipe; 14, first gear; 15, second gear; 16, second transmission shaft; 17, second transmission pipe; 18, first screw rod; 21, heating spiral elbow; 22, first connecting pipe; 23, drain pipe; 24, water heating device; 25, water supply pump; 26, water supply pipe; 27, second connecting pipe; 31, second rotary drive; 32, second screw rod; 41, buffer tank; 42, discharge pipe; 43, electromagnetic valve; 44, mounting pipe; 45, third rotary drive; 46, third transmission shaft; 51, support platform; 52, support shaft; 53, fourth rotary drive; 54, first telescopic drive; 55, mounting frame; 56, turnover shaft; 57, filter box; 58, transmission disc; 59, first filter ring; 590, second filter ring; 591, ultrafiltration membrane; 592, connecting iron ring; 593, electromagnet ring; 61, second telescopic drive; 62, transmission rack; 63, transmission gear; 71, guide rod; 72, cleaning ring. DETAILED DESCRIPTION
[0023] In order to make the technical personnel in the art better understand the technical solutions of the present application, the present application will be further described in detail below in conjunction with the drawings.
[0024] Example one The present application provides a continuous production method for preparing antimony pentoxide, characterized in that it comprises the following steps: Step one, uniformly mix the antimony trioxide solution with the stabilizer solution, and put the mixed solution into the A feed barrel; put the hydrogen peroxide solution into the B feed barrel; Step two, connect the feed end of the continuous production equipment with the A feed barrel and the B feed barrel, start the antimony pentoxide colloid production device, and the continuous production equipment prepares antimony pentoxide colloid; Step three, concentrate the antimony pentoxide colloid prepared in step two to obtain antimony pentoxide colloid.
[0025] Example two On the basis of example one, please refer to Figures 1 to 7As shown, a continuous production equipment, antimony pentoxide colloid production device includes a mounting table 1, a plurality of reaction bend pipe 2 is fixedly connected on the mounting table 1, the top of the mounting table 1 is fixedly connected with two feed pumps 3, the output end of the feed pump 3 is fixedly connected with the first feed pipe 4, the outer surface of the two first feed pipes 4 is fixedly connected with a plurality of second feed pipes 5 fixedly connected with the reaction bend pipe 2, the second feed pipe 5 is provided with a flow control valve 6, the mounting table 1 is fixedly connected with a discharge pipe 7, the outer surface of the discharge pipe 7 is fixedly connected with the reaction bend pipe 2 through the pipeline; The reaction bend pipe 2 is provided with a mixing and heating mechanism connected with the mounting table 1, the mixing and heating mechanism is used for mixing and heating the raw materials, one end of the discharge pipe 7 is fixedly connected with an antimony pentoxide colloid filtering mechanism connected with the mounting table 1, the antimony pentoxide colloid filtering mechanism is used for filtering out the reacted antimony pentoxide colloid.
[0026] The mixing and heating mechanism includes a first rotating drive member 11 fixedly connected with the mounting table 1, the first rotating drive member 11 is a servo motor, the servo motor is controlled by a PLC programming program, the servo motor can control the forward and reverse rotation and the rotation angle, the output end of the first rotating drive member 11 is fixedly connected with a first transmission shaft 12, the outer surface of the first transmission shaft 12 is drivingly connected with two first transmission pipes 13 rotatably connected with the reaction bend pipe 2 through transmission wheels and transmission belts, the outer surface of the first transmission pipe 13 is fixedly sleeved with a first gear 14, the outer surface of the first gear 14 is meshingly connected with a second gear 15, the middle of the second gear 15 is fixedly sleeved with a second transmission shaft 16 rotatably connected with the reaction bend pipe 2, the outer surface of the second transmission shaft 16 is drivingly connected with a second transmission pipe 17 rotatably connected with the reaction bend pipe 2 through transmission wheels and transmission belts, the outer surfaces of the first transmission pipe 13 and the second transmission pipe 17 are fixedly connected with first spiral rods 18; The first transmission pipe 13 and the second transmission pipe 17 are provided with a heating mechanism connected with the mounting table 1, the heating mechanism is used for heating the raw materials in the reaction bend pipe 2.
[0027] The heating mechanism comprises a heating spiral bend pipe 21 fixedly connected with the first transmission pipe 13 and the second transmission pipe 17, two water isolation blocks are fixedly connected with the top and the bottom in the first transmission pipe 13 and the second transmission pipe 17, a first connecting pipe 22 is rotatably connected with the top end of the first transmission pipe 13 and the second transmission pipe 17, a drain pipe 23 is fixedly connected with one end of the first connecting pipe 22, a water heating device 24 is fixedly connected with one end of the drain pipe 23, the water heating device 24 is prior art, and water can be heated to a set temperature, for example, an existing water heater device, so that the water heating device 24 is not described in detail, and the output end of the water heating device 24 is fixedly connected with a water supply pump 25 through a pipeline, the output end of the water supply pump 25 is fixedly connected with a water supply pipe 26, the bottom end of the first transmission pipe 13 and the second transmission pipe 17 is rotatably connected with a second connecting pipe 27, and the second connecting pipe 27 is connected with the water supply pipe 26.
[0028] One end of the discharge pipe 7 is fixedly connected with a second rotary driving member 31, the second rotary driving member 31 is a servo motor, the servo motor is controlled by a PLC programming program, the servo motor can control the forward and reverse rotation and the rotation angle, and the output end of the second rotary driving member 31 is fixedly connected with a second spiral rod 32 rotatably connected with the discharge pipe 7 through a shaft coupling.
[0029] Firstly, the stabilizer solution is uniformly mixed in the antimony trioxide solution to obtain an antimony trioxide mixed solution, then the antimony trioxide mixed solution and the hydrogen peroxide solution are respectively supplied into the first feeding pipe 4 through two feeding pumps 3, then the first feeding pipe 4 supplies the raw materials into the second feeding pipe 5, the flow control valve 6 on the second feeding pipe 5 controls the flow of the supplied raw materials, so that the antimony trioxide mixed solution and the hydrogen peroxide solution are supplied into the multiple reaction bends 2 according to a certain proportion for reaction, at the same time, the first transmission shaft 12 is driven to rotate by the first rotary driving member 11, the two first transmission pipes 13 are driven to rotate by the transmission belt and the transmission wheel, the second transmission shaft 16 is driven to rotate by the first gear 14 and the second gear 15, the second transmission pipe 17 is driven to rotate by the transmission wheel and the transmission belt, so that the second transmission pipe 17 rotates in the opposite direction of the first transmission pipe 13, the second transmission pipe 17 rotates upwards and the first transmission pipe 13 rotates downwards, so that the first screw rod 18 driven by the second transmission pipe 17 rotates upwards and the first screw rod 18 driven by the first transmission pipe 13 rotates downwards, which drives the reaction raw materials in the reaction bends 2 to move upwards and downwards, so that the raw materials flow smoothly in the reaction bends 2, and at the same time, the spiral feeding of the first screw rod 18 enables the antimony trioxide mixed solution and the hydrogen peroxide solution to continuously stir and mix in the reaction bends 2, so that the raw materials are fully mixed and reacted, at the same time, the water in the water heating device 24 is heated to a set temperature from left to right, the temperature gradually increases from left to right, then the heated water in the water heating device 24 is pumped into the water supply pipe 26 through the water pump 25, then the hot water is supplied into the first transmission pipe 13 or the second transmission pipe 17 through the second connecting pipe 27, since the top and bottom of the first transmission pipe 13 and the second transmission pipe 17 are fixedly connected with the water isolation blocks, so that the hot water enters the heating spiral bend 21 through the first transmission pipe 13 or the second transmission pipe 17, the heating spiral bend 21 is located in the middle of the first screw rod 18, so that the heating spiral bend 21 fully heats the raw materials in the reaction bends 2, further improves the heating effect of the raw materials, and at the same time, the temperature of the water gradually increases from left to right, so that the reaction temperature of the raw materials gradually increases in the reaction bends 2 to the required reaction temperature, which prevents the local heating temperature of the raw materials from being too high to cause the reaction to produce by-products, affecting the purity of the reaction, thereby further improving the heating effect and promoting the reaction effect, then the reacted raw materials enter the discharge pipe 7, then the second screw rod 32 is driven to rotate by the second rotary driving member 31 to further mix and react the reacted raw materials, so that the antimony trioxide solution and the hydrogen peroxide solution are fully reacted to generate antimony pentoxide colloid in the continuous conveying process,The generated antimony pentoxide colloid is stabilized by a stabilizer, greatly improving the reaction effect and reaction efficiency between the antimony trioxide solution and the hydrogen peroxide solution, and further improving the preparation efficiency of the antimony pentoxide colloid and the quality of the antimony pentoxide.
[0030] Example three On the basis of example two, please refer to Figure 1 、 Figure 2 、 Figure 3 And Figure 7 As shown, the antimony pentoxide colloid filtering mechanism includes a buffer tank 41 fixedly connected with the discharge pipe 7, the bottom end of the buffer tank 41 is fixedly connected with a discharge pipe 42, the discharge pipe 42 is provided with a solenoid valve 43, the bottom end of the discharge pipe 42 is rotatably connected with an installation pipe 44 rotatably connected with the installation table 1, the installation table 1 is fixedly connected with a third rotary driving element 45, the third rotary driving element 45 is a servo motor, the servo motor is controlled by a PLC programming program, the servo motor can control the forward and reverse rotation and the rotation angle, the output end of the third rotary driving element 45 is fixedly connected with a third transmission shaft 46, the outer surface of the third transmission shaft 46 is transmissionally connected with the installation pipe 44 through transmission wheels and transmission belts, the bottom end of the installation pipe 44 is transmissionally connected with a filtering mechanism, the filtering mechanism is used for filtering the liquid discharged from the installation pipe 44.
[0031] The filtering mechanism includes a support table 51, a support shaft 52 is rotatably connected to the support table 51, the bottom end of the support shaft 52 is fixedly connected with a fourth rotary driving element 53 fixedly connected with the support table 51, the fourth rotary driving element 53 is a servo motor, the servo motor is controlled by a PLC programming program, the servo motor can control the forward and reverse rotation and the rotation angle, the top end of the support shaft 52 is fixedly connected with a first telescopic driving element 54 through a connecting plate, the first telescopic driving element 54 is an electric telescopic rod or a hydraulic rod, the output end of the first telescopic driving element 54 is fixedly connected with two mounting racks 55 through a connecting plate, a turnover shaft 56 is arranged in the mounting rack 55, the outer surface of the turnover shaft 56 is transmissionally connected with a driving mechanism connected with the mounting rack 55, one end of the turnover shaft 56 is fixedly connected with a filter box 57, a transmission disc 58 is rotatably connected in the filter box 57, the top of the transmission disc 58 is fixedly connected with a first filter ring 59, the first filter ring 59 is fixedly connected with a second filter ring 590 fixedly connected with the transmission disc 58, the inner surfaces of the first filter ring 59 and the second filter ring 590 are both fixedly connected with ultrafiltration membranes 591, the top of the second filter ring 590 is fixedly connected with a connecting iron ring 592, the bottom of the installation pipe 44 is fixedly connected with an electromagnet ring 593.
[0032] The driving mechanism comprises a second telescopic driving piece 61 fixedly connected with the mounting frame 55, the second telescopic driving piece 61 is an electric telescopic rod or an electric hydraulic rod, an output end of the second telescopic driving piece 61 is fixedly connected with a transmission rack 62 through a connecting block, one side of the transmission rack 62 is meshingly connected with a transmission gear 63 fixedly sleeved with the turnover shaft 56.
[0033] A top portion of the transmission disc 58 is fixedly connected with a guide rod 71, an outer surface of the guide rod 71 is slidingly connected with a cleaning ring 72 slidingly connected with the ultrafiltration membrane 591, and an outer surface of the cleaning ring 72 is fixedly connected with a cleaning soft brush.
[0034] One side of the cleaning ring 72 is fixedly connected with a counterweight.
[0035] The fourth rotating drive 53 drives the support shaft 52 to rotate, and the support shaft 52 drives the two mounting frames 55 to rotate, so that the filter box 57 on one of the mounting frames 55 is rotated to the lower side of the mounting pipe 44. Then, the first telescopic drive 54 drives the mounting frame 55 and the filter box 57 to move upwards, so that the connecting iron ring 592 at the top of the second filter ring 590 is in contact with the electromagnetic iron ring 593 at the bottom of the mounting pipe 44, and the electromagnetic iron ring 593 is electrified to adsorb and fix the connecting iron ring 592. Then, the colloid generated after the reaction is introduced into the buffer box 41 through the discharge pipe 7, and then the buffer box 41 is introduced into the mounting pipe 44 through the discharge pipe 42. The mounting pipe 44 introduces the raw material into the second filter ring 590, and the third rotating drive 45 drives the third transmission shaft 46 to rotate. The third transmission shaft 46 drives the mounting pipe 44 to rotate through the transmission wheel and the transmission belt. The mounting pipe 44 drives the second filter ring 590 to rotate, and the second filter ring 590 drives the transmission disc 58 and the first filter ring 59 to rotate. The liquid after the reaction in the second filter ring 590 is filtered through the ultrafiltration membrane 591 under the action of centrifugal force, and then enters the first filter ring 59 and is filtered again through the ultrafiltration membrane 591 in the first filter ring 59, so that the colloid after the reaction is fully filtered out. After a period of filtration, the electromagnetic valve 43 on the discharge pipe 42 is closed. At this time, the liquid after the reaction is buffered in the buffer box 41, and then the electromagnetic iron ring 593 is de-energized, and the mounting frame 55 and the filter box 57 are driven to move downwards and rotate, so that the other filter box 57 is rotated to the lower side of the mounting pipe 44. Then, the above-mentioned filtering action is repeated, and then the electromagnetic valve 43 on the discharge pipe 42 is opened for filtering, so as to realize continuous filtration of the solution after the reaction, and further improve the production efficiency of the antimony pentoxide colloid. At the same time, the filter box 57 just filtered is rotated to the discharge position. At this time, the second telescopic drive 61 drives the transmission rack 62 to move back and forth, the transmission rack 62 drives the transmission gear 63 to rotate back and forth, and the transmission gear 63 drives the turnover shaft 56 and the filter box 57 to move back and forth. At this time, the cleaning ring 72 in the filter box 57 drives the cleaning soft brush to clean the colloid filtered on the inner surface of the first filter ring 59 and the second filter ring 590 under the action of gravity, and the filter box 57 is inverted to pour out the cleaned colloid, so as to realize automatic discharge of the antimony pentoxide colloid after the filtration, realize continuous and automatic filtration of the antimony pentoxide colloid prepared by reaction, and realize automatic cleaning and collection of the antimony pentoxide colloid after the filtration, and further improve the production efficiency of the antimony pentoxide colloid.
[0036] Working principle: first, the stabilizer solution is uniformly mixed in the antimony trioxide solution to obtain an antimony trioxide mixed solution, then the antimony trioxide mixed solution and the hydrogen peroxide solution are supplied into the first feeding pipe 4 through two feed pumps 3, then the first feeding pipe 4 supplies the raw materials into the second feeding pipe 5, the flow control valve 6 on the second feeding pipe 5 controls the flow of the supplied raw materials, so that the antimony trioxide mixed solution and the hydrogen peroxide solution are supplied into the multiple reaction bends 2 according to a certain proportion for reaction, at the same time, the first transmission shaft 12 is driven to rotate by the first rotary drive 11, the first transmission pipe 13 is driven to rotate by the transmission belt and the transmission wheel, the second transmission shaft 16 is driven to rotate by the first gear 14 and the second gear 15, the second transmission pipe 17 is driven to rotate by the transmission wheel and the transmission belt, so that the second transmission pipe 17 rotates in the opposite direction of the first transmission pipe 13, the second transmission pipe 17 rotates upwards and the first transmission pipe 13 rotates downwards, so that the first screw rod 18 driven by the second transmission pipe 17 rotates upwards and the first screw rod 18 driven by the first transmission pipe 13 rotates downwards, which drives the reaction raw materials in the reaction bends 2 to move upwards, the first screw rod 18 driven by the first transmission pipe 13 moves downwards, which drives the raw materials to move downwards, so that the raw materials flow smoothly in the reaction bends 2, at the same time, the water in the water heating device 24 is heated to a set temperature from left to right, the temperature of the water heated by each water heating device 24 gradually increases from left to right, then the water heated in the water heating device 24 is pumped into the water supply pipe 26 by the water pump 25, then the hot water is supplied into the first transmission pipe 13 or the second transmission pipe 17 by the second connecting pipe 27, since the top and bottom of the first transmission pipe 13 and the second transmission pipe 17 are fixedly connected to the water isolation block, the hot water enters the heating spiral bend 21 through the first transmission pipe 13 or the second transmission pipe 17, the heating spiral bend 21 is located in the middle of the first screw rod 18, so that the heating spiral bend 21 sufficiently heats the raw materials in the reaction bends 2, which further improves the heating effect of the raw materials, at the same time, the temperature of the water gradually increases from left to right, so that the reaction temperature of the raw materials in the reaction bends 2 gradually increases to the required reaction temperature, which prevents the local heating temperature of the raw materials from being too high, causing the reaction to produce by-products, affecting the purity of the reaction, thereby further improving the heating effect and promoting the reaction effect, then the reacted raw materials enter the discharge pipe 7, then the second screw rod 32 is driven to rotate by the second rotary drive 31, which performs mixing reaction on the reacted raw materials again, so that the antimony trioxide solution and the hydrogen peroxide solution are fully reacted to generate antimony pentoxide colloid in the continuous conveying process,The generated antimony pentoxide colloid is stabilized by a stabilizer, the reaction effect and reaction efficiency between the antimony trioxide solution and the hydrogen peroxide solution are greatly improved, and the preparation efficiency of the antimony pentoxide colloid and the quality of the antimony pentoxide are further improved.
[0037] The prepared antimony pentoxide colloid is automatically filtered and discharged through the antimony pentoxide colloid filtering mechanism, so that the filtered antimony pentoxide colloid is automatically discharged, the continuously automatically filtered antimony pentoxide colloid prepared by reaction is realized, and the filtered antimony pentoxide colloid is automatically cleaned and collected, and the production efficiency of the antimony pentoxide colloid is further improved.
[0038] The above only describes certain exemplary embodiments of the present application in a descriptive manner, and it is needless to say that the described embodiments can be modified in various ways without departing from the spirit and scope of the present application for those skilled in the art. Therefore, the above drawings and descriptions are illustrative in nature and should not be understood as limiting the scope of protection of the claims of the present application.
Claims
1. A continuous production process for preparing antimony pentoxide, characterized in that, It comprises the following steps: Step one, the antimony trioxide solution and stabilizer solution are uniformly mixed, and the mixed solution is put into the A feeding barrel; The hydrogen peroxide solution is put into the B feeding barrel; Step two, the feeding end of the continuous production equipment is connected with the A feeding barrel and the B feeding barrel, and the continuous production equipment is started, and the antimony pentoxide colloid is prepared; Step three, the antimony pentoxide colloid prepared in step two is concentrated to obtain the antimony pentoxide colloid.
2. A continuous production apparatus suitable for use in a continuous production method of antimony pentoxide according to claim 1, characterized in that, The device comprises a mounting table (1), a plurality of reaction bends (2) are fixedly connected to the mounting table (1), two feeding pumps (3) are fixedly connected to the top of the mounting table (1), the output ends of the feeding pumps (3) are fixedly connected with first feeding pipes (4), the outer surfaces of the two first feeding pipes (4) are fixedly connected with a plurality of second feeding pipes (5) fixedly connected with the reaction bends (2), flow control valves (6) are arranged on the second feeding pipes (5), and a discharge pipe (7) is fixedly connected to the mounting table (1); and the discharge pipe (7) is fixedly connected with the reaction bends (2) through a pipeline; The reaction bends (2) are provided with a mixing and heating mechanism connected with the mounting table (1), the mixing and heating mechanism is used for mixing and heating the raw materials, and one end of the discharge pipe (7) is fixedly connected with a antimony pentoxide colloid filtering mechanism connected with the mounting table (1), and the antimony pentoxide colloid filtering mechanism is used for filtering out the reacted antimony pentoxide colloid.
3. A continuous production apparatus according to claim 2, wherein The mixing and heating mechanism comprises a first rotating driving member (11) fixedly connected with the mounting table (1), a first transmission shaft (12) fixedly connected to the output end of the first rotating driving member (11), two first transmission pipes (13) rotatably connected with the reaction bends (2) and in transmission connection with the first transmission shaft (12) through transmission wheels and transmission belts on the outer surfaces of the first transmission shaft (12), first gears (14) fixedly sleeved on the outer surfaces of the first transmission pipes (13), second gears (15) in meshing connection with the outer surfaces of the first gears (14), a second transmission shaft (16) fixedly sleeved in the middle of the second gears (15) and rotatably connected with the reaction bends (2), a second transmission pipe (17) rotatably connected with the reaction bends (2) and in transmission connection with the second transmission shaft (16) through transmission wheels and transmission belts on the outer surfaces of the second transmission shaft (16), and first spiral rods (18) fixedly connected to the outer surfaces of the first transmission pipes (13) and the second transmission pipe (17); The first transmission pipes (13) and the second transmission pipe (17) are provided with a heat supply mechanism connected with the mounting table (1), and the heat supply mechanism is used for heating the raw materials in the reaction bends (2).
4. A continuous production apparatus according to claim 3, wherein The heating mechanism includes a heating spiral bend pipe (21) fixedly connected with the first transmission pipe (13) and the second transmission pipe (17), two waterproof blocks are fixedly connected to the top and the bottom of the first transmission pipe (13) and the second transmission pipe (17), the top end of the first transmission pipe (13) and the second transmission pipe (17) is rotatably connected with a first connecting pipe (22), one end of the first connecting pipe (22) is fixedly connected with a drain pipe (23), one end of the drain pipe (23) is fixedly connected with a water heating device (24), the output end of the water heating device (24) is fixedly connected with a water supply pump (25) through a pipeline, the output end of the water supply pump (25) is fixedly connected with a water supply pipe (26), the bottom end of the first transmission pipe (13) is rotatably connected with a second connecting pipe (27), and the second connecting pipe (27) is connected with the water supply pipe (26).
5. The continuous production apparatus according to claim 2, wherein One end of the discharge pipe (7) is fixedly connected with a second rotary driving member (31), and the output end of the second rotary driving member (31) is fixedly connected with a second spiral rod (32) rotatably connected with the discharge pipe (7) through a shaft coupling.
6. The continuous production apparatus according to claim 2, wherein The antimony pentoxide colloidal filtering mechanism includes a buffer tank (41) fixedly connected with the discharge pipe (7), the bottom end of the buffer tank (41) is fixedly connected with a discharge pipe (42), the discharge pipe (42) is provided with a solenoid valve (43), the bottom end of the discharge pipe (42) is rotatably connected with a mounting pipe (44) rotatably connected with the mounting table (1), the mounting table (1) is fixedly connected with a third rotary driving member (45), the output end of the third rotary driving member (45) is fixedly connected with a third transmission shaft (46), the outer surface of the third transmission shaft (46) is drivingly connected with the mounting pipe (44) through a transmission wheel and a transmission belt, and the bottom end of the mounting pipe (44) is drivingly connected with a filtering mechanism, and the filtering mechanism is used for filtering the liquid discharged from the mounting pipe (44).
7. A continuous production apparatus according to claim 6, wherein The filtering mechanism includes a support table (51), a support shaft (52) is rotatably connected to the support table (51), a fourth rotary driving piece (53) is fixedly connected to the bottom end of the support shaft (52) and fixedly connected with the support table (51), a first telescopic driving piece (54) is fixedly connected to the top end of the support shaft (52) through a connecting plate, the output end of the first telescopic driving piece (54) is fixedly connected with two mounting racks (55) through a connecting plate, a turnover shaft (56) is arranged in the mounting rack (55), a driving mechanism is drivingly connected to the outer surface of the turnover shaft (56) and connected with the mounting rack (55), a filter box (57) is fixedly connected to one end of the turnover shaft (56), a transmission disc (58) is rotatably connected in the filter box (57), a first filter mesh ring (59) is fixedly connected to the top of the transmission disc (58), a second filter mesh ring (590) is fixedly connected with the transmission disc (58) and fixedly connected in the first filter mesh ring (59), an ultrafiltration membrane (591) is fixedly connected to the inner surfaces of the first filter mesh ring (59) and the second filter mesh ring (590), a connecting iron ring (592) is fixedly connected to the top of the second filter mesh ring (590), and an electromagnet ring (593) is fixedly connected to the bottom of the mounting pipe (44).
8. A continuous production apparatus according to claim 7, wherein The driving mechanism includes a second telescopic driving piece (61) fixedly connected with the mounting rack (55), a transmission rack (62) is fixedly connected to the output end of the second telescopic driving piece (61) through a connecting block, and a transmission gear (63) is fixedly sleeved with the turnover shaft (56) and meshingly connected to one side of the transmission rack (62).
9. The continuous production apparatus according to claim 6, wherein The top of the transmission disc (58) is fixedly connected with a guide rod (71), a cleaning ring (72) is slidingly connected to the outer surface of the guide rod (71) and slidingly connected with the ultrafiltration membrane (591), and a cleaning soft hair brush is fixedly connected to the outer surface of the cleaning ring (72).
10. A continuous production apparatus according to claim 9, wherein One side of the cleaning ring (72) is fixedly connected with a counterweight.