Drying equipment for 2-ethyl anthraquinone production
Through the comprehensive design of spiral drying tube and heating pad structure, air circulation and condensation system, and material introduction and sealing system, the problems of low efficiency, high energy consumption and environmental pollution of traditional drying equipment are solved, and a high-efficiency, environmentally friendly and energy-saving 2-ethylanthraquinone drying effect is achieved.
Patent Information
- Application Number
- CN202422951501.X
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-12-02
- Publication Date
- 2025-10-17
- Estimated Expiration
- 2034-12-02
AI Technical Summary
Traditional 2-ethylanthraquinone drying equipment has problems such as low drying efficiency, high energy consumption, complex operation and serious environmental pollution. It is especially difficult to achieve ideal drying effects when processing materials with high water content, and untreated water vapor and exhaust gas emissions will cause environmental pollution.
The overall design adopts a spiral drying tube and heating pad structure, air circulation and condensation system, filtration and maintenance system, and material introduction and sealing system. Through centrifugal separation, heating evaporation, air circulation condensation, and material introduction and sealing, the drying efficiency is improved and environmental pollution is reduced.
An efficient, environmentally friendly and energy-saving drying process is achieved, the drying efficiency of 2-ethylanthraquinone is improved, environmental pollution is reduced, production costs are lowered, and the stable operation and automation level of the equipment are ensured.
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Figure CN223448865U_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The utility model belongs to 2 -ethyl anthraquinone production related technical field, specifically related to a kind of drying equipment for 2-ethyl anthraquinone production. BACKGROUND
[0002] In chemical production, especially in the field of fine chemical industry, drying technology is the key link to ensure product quality and production efficiency. Although traditional drying methods, such as hot air drying, vacuum drying, etc., can realize the drying of materials, their limitations become particularly obvious when dealing with fine chemical products such as 2-ethyl anthraquinone. Traditional methods often have low drying efficiency, high energy consumption, complex operation, serious environmental pollution and other problems. Especially when dealing with materials with high water content, traditional drying equipment often fails to achieve ideal drying results, and a large amount of water vapor and waste gas is generated during the drying process, which, if not effectively treated before being discharged, will cause serious pollution to the environment and increase production cost and environmental pressure.
[0003] In view of the above background, in recent years, the chemical industry has conducted in-depth research and innovation on drying technology, aiming to develop more efficient, environmentally friendly and energy-saving drying equipment to meet the needs of modern chemical production. This patent technology emerges as the times require, and provides an innovative drying solution for 2-ethyl anthraquinone production by integrating spiral drying pipe and heating pad structure, air circulation and condensation system, filtration and maintenance system, material introduction and sealing system and overall design. SUMMARY
[0004] The utility model aims at providing a kind of drying equipment for 2-ethyl anthraquinone production to solve the problems of low drying efficiency, high energy consumption, complex operation and serious environmental pollution of traditional 2-ethyl anthraquinone drying equipment as mentioned in the above background technology.
[0005] To achieve the above-mentioned purpose, the utility model provides the following technical scheme: a kind of drying equipment for 2-ethyl anthraquinone production, including support frame, the support frame is internally provided with spiral drying pipe and condenser pipe, and the drying pipe is located outside the condenser pipe, the front and back of the upper and lower ends of the drying pipe are fixedly connected in the support frame by connecting rod, the upper and lower ends of the drying pipe are communicated with the upper and lower ends of the condenser pipe by connecting seat, and the drying pipe and the condenser pipe are fixedly connected by connecting seat and multiple connecting rods, the upper end of the drying pipe is communicated with hopper, and the lower end of the drying pipe is communicated with material collecting tank.
[0006] Preferably, a fan slot is formed in the center of the upper end of the connecting seat on the lower side, and water vapor filters are arranged on the inner walls of the front and rear ends of the fan slot, and the two water vapor filters are respectively communicated with the inner sides of the front and rear ends of the connecting seat on the lower side and communicated with the interiors of the drying pipe and the condenser pipe through the connecting seat on the lower side.
[0007] Preferably, the upper end of the fan slot is internally clamped with an air guide fan, the inside of the far end of the drying tube and the inside of the lower end of the condenser tube are provided with water collecting tanks, and the upper and lower ends of the two water collecting tanks are respectively penetrated into the inside of the two connecting seats, and the drying tube and the condenser tube are provided with separation filter plates between the two water collecting tanks.
[0008] Preferably, the left end of the lower connecting seat is fixedly connected with a drain pipe head, the drain pipe head is not communicated with the inside of the drying tube and the condenser tube, the lower ends of the two water collecting tanks are communicated with the inside of the right end of the drain pipe head, and the left end of the drain pipe head is connected with a water collecting tank.
[0009] Preferably, the lower end of the connecting seat is communicated with a threaded connector on the front side, and the threaded connector is connected with the aggregate tank, and the lower end of the drying tube is provided with a heating pad on the side close to the condenser tube, and the heating pad is tightly attached to the outer wall of the lower end of the drying tube.
[0010] Preferably, the inside of the front and rear ends of the upper connecting seat is respectively communicated with the inside of the drying tube and the condenser tube, the inside of the upper end of the upper connecting seat is provided with a filter plate slot, and the front and rear ends of the filter plate slot are respectively communicated with the inside of the upper end of the drying tube and the condenser tube through the connecting seat, and the upper end of the filter plate slot is clamped with a filter baffle.
[0011] Preferably, the inside of the lower end of the hopper is provided with a material guiding sealing groove, the upper end of the material guiding sealing groove is communicated in the inside of the hopper, and the lower end of the material guiding sealing groove is communicated in the inside of the front side of the upper end of the connecting seat and communicated with the inside of the upper end of the drying tube through the connecting seat.
[0012] Preferably, the inside of the material guiding sealing groove is rotatably connected with a cylindrical material guiding sealing roller, a plurality of material guiding inner grooves are formed in the cylindrical outer wall of the material guiding sealing roller, and a material guiding motor is rotatably connected to the right end of the material guiding sealing groove through a rotating shaft, and the material guiding motor is fixedly connected to the outside of the right end of the hopper.
[0013] Compared with the prior art, the utility model provides a kind of drying equipment for 2-ethylanthraquinone production, with the following beneficial effects:
[0014] 1, the structure of helical drying tube and heating pad: the drying tube is designed as helical, through the action of helical centrifugal force, and the moisture in 2-ethylanthraquinone is centrifuged by separation filter plate and water collecting tank. By the setting of heating pad, the lower end of the heating drying tube is heated, and the moisture in 2-ethylanthraquinone is heated and separated, and the evaporation of the moisture in 2-ethylanthraquinone is accelerated. Through the synergistic effect of centrifugal separation and heating separation, the drying efficiency of 2-ethylanthraquinone is improved.
[0015] 2. Air circulation and condensation system: the combination of air guide fan and water vapor filter screen promotes the air circulation inside the drying tube and condensing tube, carries away the high-temperature water vapor inside the drying tube, and condenses in the condensing tube, improves the efficiency of heating separation, and the separated water and condensed water can be introduced into the water collecting tank through the drain pipe head to realize automatic collection and treatment of the separated water and condensed water, and reduce environmental pollution.
[0016] 3. Filtration and maintenance system: the design of filter baffle and filter plate clamping slot effectively blocks the material from entering the condensing tube, filters high-temperature water vapor, ensures the stability of the equipment operation, and the filter plate clamping slot facilitates the maintenance and replacement of the filter baffle, ensuring long-term stable operation of the equipment.
[0017] 4. Material introduction and sealing system: the innovative design of material guide sealing roller and material guide inner groove ensures smooth material introduction, prevents material flying and air leakage, and ensures the continuity and efficiency of the drying process. The driving of the material guide motor realizes continuous material supply and improves the automation degree of the drying process.
[0018] 5. Overall design and synergistic effect: the overall design of the equipment considers the material characteristics, drying efficiency, environmental protection requirements and maintenance convenience, realizes an efficient, environmentally friendly and energy-saving drying solution. BRIEF DESCRIPTION OF DRAWINGS
[0019] Figure 1 It is a three-dimensional structure schematic diagram of the drying equipment of the utility model.
[0020] Figure 2 It is a drying tube connection structure schematic diagram of the utility model.
[0021] Figure 3 It is a Figure 2 enlarged schematic diagram of A.
[0022] Figure 4 It is a hopper connection structure schematic diagram of the utility model.
[0023] Figure 5 It is a Figure 4 enlarged schematic diagram of B.
[0024] Figure 6 It is a heating pad connection structure schematic diagram of the utility model.
[0025] Figure 7 It is a Figure 6 enlarged schematic diagram of C.
[0026] In the figure: 1, support frame; 2, drying tube; 3, condenser tube; 4, connecting rod; 5, connecting seat; 6, hopper; 7, material collecting tank; 8, fan slot; 9, water vapor filter screen; 10, air guide fan; 11, water collecting tank; 12, drain pipe head; 13, threaded connector; 14, heating pad; 15, filter plate slot; 16, filter baffle; 17, separation filter plate; 18, material guide sealing groove; 19, material guide sealing roller; 20, material guide inner groove; 21, material guide motor. DETAILED DESCRIPTION
[0027] The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the drawings in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, rather than all the embodiments. Based on the embodiments in the present application, all other embodiments obtained by those skilled in the art without creative labor fall within the scope of protection of the present application.
[0028] The present application provides a kind of Figures 1-7The illustrated 2-ethyl anthraquinone production drying equipment, including support frame 1, support frame 1 inside set in spiral drying pipe 2 and condenser pipe 3, and drying pipe 2 is located outside the condenser pipe 3, drying pipe 2 upper and lower two ends of the front and back sides are fixedly connected in the support frame 1 inside through connecting rod 4, drying pipe 2 upper and lower ends are communicated with the upper and lower ends of condenser pipe 3 through connecting seat 5, and drying pipe 2 and condenser pipe 3 are fixedly connected through connecting seat 5 and multiple connecting rods 4, drying pipe 2 upper end is communicated with hopper 6, drying pipe 2 lower end is communicated with collecting tank 7, drying pipe 2 end away from condenser pipe 3 inside and condenser pipe 3 lower end inside are provided with water collecting tank 11, and upper and lower ends of two water collecting tanks 11 are respectively penetrated in two connecting seats 5 inside, drying pipe 2 and condenser pipe 3 and two water collecting tanks 11 are provided with separation filter plate 17, drying pipe 2 lower end is provided with heating pad 14 near one side of condenser pipe 3, and heating pad 14 is closely attached to the outer wall of drying pipe 2 lower end, the lower connecting seat 5 lower end front side is communicated with threaded connector 13, and is connected with collecting tank 7 through threaded connector 13, when the drying equipment is drying 2-ethyl anthraquinone, 2-ethyl anthraquinone is put into hopper 6 inside, and heating pad 14 is connected with power supply, hopper 6 guides 2-ethyl anthraquinone into drying pipe 2 inside through the upper connecting seat 5, 2-ethyl anthraquinone rolls down in drying pipe 2 inside under the action of gravity, because drying pipe 2 is set in spiral, so that 2-ethyl anthraquinone rolls in drying pipe 2 inside can produce centrifugal force, so that the moisture in 2-ethyl anthraquinone can swing away from condenser pipe 3 side under the action of centrifugal force, and the separated moisture is separated into water collecting tank 11 inside through separation filter plate 17 between drying pipe 2 and water collecting tank 11, at the same time, heating pad 14 can heat the side of drying pipe 2 lower end near condenser pipe 3, so that the moisture in 2-ethyl anthraquinone can be separated by centrifugal force and evaporated by heating of heating pad 14, thereby improving the drying efficiency of 2-ethyl anthraquinone, ensuring that the moisture in 2-ethyl anthraquinone can be completely removed, finally 2-ethyl anthraquinone is guided into collecting tank 7 inside through connecting seat 5 lower end connected with connecting seat 5, and collecting tank 7 is threadedly connected with connecting seat 5 through threaded connector 13, so that the dried 2-ethyl anthraquinone can be more conveniently taken.
[0029] Preferably, the lower connecting seat 5 is internally provided with a fan clamping groove 8 at the center of the upper end, the inner walls of the front and rear ends of the fan clamping groove 8 are internally provided with water vapor filters 9, and the two water vapor filters 9 are respectively communicated to the inside of the front and rear ends of the lower connecting seat 5 and communicated to the inside of the drying pipe 2 and the condensing pipe 3 through the lower connecting seat 5, a gas guide fan 10 is clamped in the upper end of the fan clamping groove 8, a drain pipe head 12 is fixedly connected to the left end of the lower connecting seat 5, the drain pipe head 12 is not communicated to the inside of the drying pipe 2 and the condensing pipe 3, the lower ends of the two water collecting tanks 11 are communicated to the inside of the right end of the drain pipe head 12, and the drain pipe head 12 is connected with a water collecting tank. In the process of drying 2-ethylanthraquinone, the air in the drying pipe 2 and the condensing pipe 3 can be circulated by turning on the gas guide fan 10, and the air flows upward in the drying pipe 2, so that the high-temperature water vapor evaporated in the drying pipe 2 can be brought to the upper end of the drying pipe 2 by the flowing air, and introduced into the condensing pipe 3 through the upper connecting seat 5, and cooled in the condensing pipe 3. Thus, the water in the high-temperature water vapor is condensed, and the condensed water is separated from the condensing pipe 3 to the inside of the water collecting tank 11 at the lower end of the condensing pipe 3 through the separation filter plate 17 between the condensing pipe 3 and the water collecting tank 11, and then filtered by the water vapor filter 9 and introduced into the drying pipe 2 at the lower end for circulation. The water collected in the two water collecting tanks 11 can be introduced into the water collecting tank through the drain pipe head 12 at the left end of the lower connecting seat 5 for collection and treatment.
[0030] Preferably, the upper connecting seat 5 is internally communicated to the inside of the drying pipe 2 and the condensing pipe 3 at the front and rear ends, the upper connecting seat 5 is internally provided with a filter plate clamping groove 15 at the center of the upper end, the filter plate clamping groove 15 is communicated to the inside of the upper end of the drying pipe 2 and the condensing pipe 3 at the front and rear ends through the connecting seat 5, and a filter baffle 16 is clamped in the upper end of the filter plate clamping groove 15. In the process of air flowing in the drying pipe 2 and the condensing pipe 3, the filter baffle 16 can filter the high-temperature water vapor flowing from the drying pipe 2 into the condensing pipe 3 and block 2-ethylanthraquinone from entering the condensing pipe 3, and the filter baffle 16 can be removed from the filter plate clamping groove 15 for maintenance.
[0031] Preferably, a material guide sealing groove 18 is provided inside the lower end of the hopper 6, the upper end of the material guide sealing groove 18 is connected to the inside of the hopper 6, and the lower end of the material guide sealing groove 18 is connected to the front interior of the upper end of the connecting seat 5, and is connected to the upper end of the drying tube 2 through the connecting seat 5. A cylindrical material guide sealing roller 19 is rotatably connected to the inside of the material guide sealing groove 18, and a plurality of material guide inner grooves 20 are provided inside the cylindrical outer wall of the material guide sealing roller 19. The right end of the material guide sealing groove 18 is rotatably connected to a material guide motor 21 through a rotating shaft, and the material guide motor 21 is fixedly connected to the outside of the right end of the hopper 6. In the process of 2-ethylanthraquinone passing through the hopper 6 and entering the interior of the upper connecting seat 5, the hopper 6 can introduce 2-ethylanthraquinone into the interior of the upper connecting seat 5 through the material guide sealing groove 18 at the lower end, and pass through the guide The material guide sealing roller 19 rotatably connected inside the material sealing groove 18 and the multiple material guide inner grooves 20 opened inside the material guide sealing roller 19 bring 2-ethylanthraquinone into the connecting seat 5, and the material guide inner grooves 20 are driven by the material guide motor 21 arranged on the lower side of the right end of the hopper 6. Since the multiple material guide inner grooves 20 are not connected to each other and the material guide sealing roller 19 is blocked inside the material guide sealing groove 18, the air flowing inside the drying tube 2 will not blow 2-ethylanthraquinone out of the connecting seat 5, which can ensure that 2-ethylanthraquinone can stably pass through the connecting seat 5 into the drying tube 2, and prevent dust from being raised at the upper end of the hopper 6. At the same time, it ensures that the flow rate of the air flowing inside the drying tube 2 and the condenser tube 3 remains stable, so that the high-temperature water vapor inside the drying tube 2 can be taken away in time.
[0032] Finally, it should be noted that the above is only a preferred embodiment of the present invention and is not intended to limit the present invention. Although the present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art can still modify the technical solutions described in the aforementioned embodiments or make equivalent replacements for some of the technical features therein. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention should be included in the scope of protection of the present invention.
Claims
1. A drying device for producing 2-ethylanthraquinone, characterized in that: The invention comprises a support frame (1), wherein a spiral drying pipe (2) and a condensing pipe (3) are arranged inside the support frame (1), and the drying pipe (2) is located outside the condensing pipe (3), and the front and rear sides of the upper and lower ends of the drying pipe (2) are fixedly connected to the inside of the support frame (1) through connecting rods (4), and the upper and lower ends of the drying pipe (2) are connected to the upper and lower ends of the condensing pipe (3) through connecting seats (5), and the drying pipe (2) and the condensing pipe (3) are fixedly connected to a plurality of connecting rods (4) through the connecting seats (5), and the upper end of the drying pipe (2) is connected to a hopper (6), and the lower end of the drying pipe (2) is connected to a collecting tank (7).
2. The drying equipment for producing 2-ethylanthraquinone according to claim 1, characterized in that: A fan slot (8) is provided at the center of the upper end of the lower connecting seat (5), and water vapor filters (9) are provided inside the inner walls of the front and rear ends of the fan slot (8), and the two water vapor filters (9) are respectively connected to the interiors of the front and rear ends of the lower connecting seat (5), and are connected to the interiors of the drying tube (2) and the condensing tube (3) through the lower connecting seat (5).
3. The drying equipment for producing 2-ethylanthraquinone according to claim 2, characterized in that: An air guide fan (10) is clamped inside the upper end of the fan slot (8), and a water collecting tank (11) is provided inside the end of the drying tube (2) away from the condensing tube (3) and the lower end of the condensing tube (3), and the upper and lower ends of the two water collecting tanks (11) respectively pass through the inside of the two connecting seats (5), and a separation filter plate (17) is provided between the drying tube (2) and the condensing tube (3) and the two water collecting tanks (11).
4. The drying equipment for producing 2-ethylanthraquinone according to claim 3, characterized in that: The left end of the connecting seat (5) on the lower side is fixedly connected to a drain pipe head (12), and the drain pipe head (12) is not connected to the interior of the drying pipe (2) and the condensing pipe (3). The lower ends of the two water collecting tanks (11) are both connected to the interior of the right end of the drain pipe head (12), and the left end of the drain pipe head (12) is connected to a water collecting tank.
5. The drying equipment for producing 2-ethylanthraquinone according to claim 4, characterized in that: The front side of the lower end of the connecting seat (5) on the lower side is connected to a threaded connector (13), and is connected to the collecting tank (7) through the threaded connector (13). A heating pad (14) is provided on the side of the lower end of the drying pipe (2) close to the condenser pipe (3), and the heating pad (14) is tightly fitted on the outer wall of the lower end of the drying pipe (2).
6. The drying equipment for producing 2-ethylanthraquinone according to claim 1, characterized in that: The interiors of the front and rear ends of the upper connecting seat (5) are respectively connected to the interiors of the drying tube (2) and the condensing tube (3); a filter plate slot (15) is provided at the center of the upper end of the upper connecting seat (5); and the front and rear ends of the filter plate slot (15) are respectively connected to the interiors of the upper ends of the drying tube (2) and the condensing tube (3) through the connecting seat (5); a filter baffle (16) is clamped inside the upper end of the filter plate slot (15).
7. The drying equipment for producing 2-ethylanthraquinone according to claim 1, characterized in that: A material guide sealing groove (18) is provided inside the lower end of the hopper (6), the upper end of the material guide sealing groove (18) is connected to the inside of the hopper (6), and the lower end of the material guide sealing groove (18) is connected to the front side of the upper end of the connecting seat (5), and is connected to the upper end of the drying pipe (2) through the connecting seat (5).
8. The drying equipment for producing 2-ethylanthraquinone according to claim 7, characterized in that: A cylindrical material guide sealing roller (19) is rotatably connected inside the material guide sealing groove (18), and a plurality of material guide inner grooves (20) are provided inside the cylindrical outer wall of the material guide sealing roller (19). The right end of the material guide sealing groove (18) is rotatably connected to a material guide motor (21) via a rotating shaft, and the material guide motor (21) is fixedly connected to the outside of the right end of the hopper (6).