Carbon monoxide combustion improver production device
The production device, which combines a closed kneader and a sprayer, solves the problems of uneven spraying and high safety risks in the production of carbon monoxide combustion improvers, and achieves efficient and safe automated production, thereby improving product quality and production efficiency.
Patent Information
- Application Number
- CN202423206448.7
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-12-25
- Publication Date
- 2025-12-12
- Estimated Expiration
- 2034-12-25
AI Technical Summary
The current production of carbon monoxide combustion improvers suffers from problems such as uneven spraying, high worker safety risks, high labor intensity, and low production efficiency.
The production device combines a closed kneader with a sprayer. The agitator inside the closed kneader mixes alumina powder and chemicals, and the sprayer sprays chemicals into the closed kneader. After the mixture is evenly mixed, it is dried and turned over by a drying conveyor bridge, reducing manual operation and realizing automated production.
It improved product quality and production efficiency, reduced safety risks, reduced labor intensity, and achieved continuous production and energy conservation.
Smart Images
Figure CN223654884U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of energy conservation and environmental protection technology, and in particular to a carbon monoxide combustion aid production device. Background Technology
[0002] In existing carbon monoxide combustion accelerant production, low-temperature alumina powder is added to a kneader. During the mixing process, the agent is manually sprayed on. After spraying, mixing is stopped, and workers remove the carbon monoxide accelerant from the kneader, place it in an oven to dry, and then remove it from the oven and stir it again. However, manual spraying can easily result in uneven spraying, reducing product quality. The process of removing the carbon monoxide accelerant from the oven and stirring it poses a risk of worker burns. Furthermore, the current carbon monoxide combustion accelerant production process requires a significant amount of manual labor, resulting in high labor intensity, high manpower consumption, and low production efficiency. Utility Model Content
[0003] The purpose of this invention is to provide a carbon monoxide combustion aid production device to solve the problems existing in the prior art, effectively improve product quality and production efficiency, and reduce safety risks.
[0004] To achieve the above objectives, this utility model provides the following solution:
[0005] This utility model provides a carbon monoxide combustion aid production device, including a closed kneader, a drive unit, a sprayer, and a drying conveyor bridge. The closed kneader has an inlet and a outlet. The inlet is used to feed alumina powder into the closed kneader, and the outlet is used to discharge the mixture of alumina powder and reagent obtained in the closed kneader to the outside of the closed kneader. A stirrer is installed inside the closed kneader to mix the alumina powder and reagent evenly. The drive unit is connected to the stirrer and drives the stirrer to operate. The first end of the sprayer is fixed... The sprayer is positioned inside the closed kneader. Its first end can spray the agent onto the alumina powder inside the closed kneader. The first end of the drying conveyor bridge is provided with a receiving port, which is connected to and communicates with the discharge port. The receiving port is used to discharge the mixture of alumina powder and agent obtained in the closed kneader into the drying conveyor bridge. The second end of the drying conveyor bridge is provided with a discharge port. The drying conveyor bridge can dry and stir the mixture of alumina powder and agent to obtain a carbon monoxide combustion aid product. The drying conveyor bridge can transport the carbon monoxide combustion aid product to the discharge port for discharge.
[0006] Preferably, it also includes a drug supply pump, with the second end of the sprayer located outside the enclosed kneader, and the second end of the sprayer connected and communicating with the outlet of the drug supply pump.
[0007] Preferably, it also includes a medicine hopper, which is capable of storing medicine, and the inlet of the medicine supply pump is connected to the medicine hopper.
[0008] Preferably, the sprayer includes a main spray pipe, several spray branch pipes, and several spray heads. The spray heads are placed inside the enclosed kneader and above the agitator. The number of spray branch pipes is equal to the number of spray heads. Each spray branch pipe corresponds to a spray head. The first end of each spray branch pipe is fixedly connected to and communicates with the first end of the main spray pipe, and the second end of each spray branch pipe is fixedly connected to and communicates with the spray head.
[0009] Preferably, it also includes a powder hopper and a feeding pipe. The powder hopper is capable of storing alumina powder and is positioned above the feed inlet. The top end of the feeding pipe is fixedly connected to and communicates with the bottom end of the powder hopper, and the bottom end of the feeding pipe is fixedly connected to and communicates with the feed inlet.
[0010] Preferably, it also includes a discharge pipe, with the first end of the drying conveyor bridge located below the discharge port, and the receiving port opened on the top surface of the first end of the drying conveyor bridge. The top end of the discharge pipe is fixedly connected to and communicates with the discharge port, and the bottom end of the discharge pipe is fixedly connected to and communicates with the receiving port. The discharge pipe is provided with a discharge valve, which can control the opening and closing of the discharge pipe.
[0011] Preferably, the drying conveyor bridge includes a conveyor shaft, conveyor blades, a conveyor motor, and a conveyor pipe. The first end of the conveyor pipe has the material inlet, and the second end of the conveyor pipe has the material outlet. The conveyor shaft and the conveyor blades are both placed inside the conveyor pipe. The conveyor blades are spirally fixed on the conveyor shaft. The conveyor shaft can rotate, and the rotation of the conveyor shaft can drive the conveyor blades to rotate. The rotation of the conveyor blades can push the material at the material inlet to the material outlet. The conveyor motor is connected to the conveyor shaft and can provide power for the rotation of the conveyor shaft.
[0012] Preferably, the system further includes a return air and dust collection pipe, an air and dust collection hood, and an axial flow fan. A return air port is provided at the second end of the conveying pipe, and the return air port is located between the discharge port and the receiving port. The air and dust collection hood is fixedly installed below the discharge port. One end of the return air and dust collection pipe is fixedly connected to and communicates with the air and dust collection hood, and the other end of the return air and dust collection pipe is fixedly connected to and communicates with the return air port. The axial flow fan is installed on the return air and dust collection pipe, and the axial flow fan can send air and dust from the discharge port into the conveying pipe.
[0013] Preferably, the return air and dust return duct is further provided with an electric heater, which is placed between the return air inlet and the axial flow fan. The electric heater can heat the air and dust in the return air and dust return duct. The return air and dust return duct is further provided with a dryer, which is placed between the return air inlet and the electric heater. The dryer can dry the air and dust in the return air and dust return duct.
[0014] Preferably, the conveying pipe is provided with an exhaust pipe, which is connected to the part between the return air port and the material receiving port on the conveying pipe, and the exhaust pipe is provided with a dust collector.
[0015] The present invention achieves the following technical advantages over the prior art:
[0016] The carbon monoxide combustion aid production device provided by this utility model uses a closed kneader to mix alumina powder and reagents. This prevents leakage of alumina powder and reagents into the environment during mixing, avoiding raw material waste and environmental pollution, improving raw material utilization, and thus increasing production efficiency. By installing a sprayer at the first end of the closed kneader to spray the reagents onto the alumina powder, manual operation and intervention in the reagent spraying process are reduced, spray uniformity is improved, and product quality is enhanced. The alumina powder and reagent mixture obtained in the closed kneader is discharged from the discharge port on the closed kneader to the receiving port at the first end of the drying conveyor bridge, and then enters the drying... Inside the dry conveyor bridge, manual transfer by workers is no longer required. The mixture of alumina powder and reagents is dried and stirred through the dry conveyor bridge to obtain the finished carbon monoxide combustion accelerator. The finished carbon monoxide combustion accelerator is then conveyed to the discharge port. Workers no longer need to take the carbon monoxide combustion accelerator out of the oven for stirring, which avoids worker burns and reduces safety risks. Furthermore, the carbon monoxide combustion accelerator production device provided by this utility model can effectively reduce manual operation in the entire production process, reduce labor intensity, reduce manpower consumption, thereby improving production efficiency, ensuring energy saving, high efficiency and continuity of the production process, facilitating continuous production, and ensuring stable product quality. Attached Figure Description
[0017] To more clearly illustrate the technical solutions in the embodiments of this utility model or the prior art, the drawings used in the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments of this utility model. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.
[0018] Figure 1 A schematic diagram of the carbon monoxide combustion aid production device provided by this utility model;
[0019] In the diagram: 1-Enclosed kneader, 2-Drive device, 3-Sprayer, 4-Drying conveyor bridge, 5-Discharge port, 6-Main spray pipe, 7-Spray branch pipe, 8-Spray head, 9-Powder hopper, 10-Discharge pipe, 11-Unloading pipe, 12-Unloading valve, 13-Return air and dust return pipe, 14-Air and dust collection hood, 15-Axial flow fan, 16-Electric heater, 17-Dryer, 18-Exhaust pipe, 19-Dust collector. Detailed Implementation
[0020] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the protection scope of the present utility model.
[0021] The purpose of this invention is to provide a carbon monoxide combustion aid production device to solve the problems existing in the prior art, effectively improve product quality and production efficiency, and reduce safety risks.
[0022] To make the above-mentioned objectives, features and advantages of this utility model more apparent and understandable, the utility model will be further described in detail below with reference to the accompanying drawings and specific embodiments.
[0023] like Figure 1As shown, this utility model provides a carbon monoxide combustion aid production device, including a closed kneader 1, a drive unit 2, a sprayer 3, and a drying conveyor bridge 4. The closed kneader 1 has an inlet and a outlet. The inlet is used to feed alumina powder into the closed kneader 1, and the outlet is used to discharge the mixture of alumina powder and reagent obtained in the closed kneader 1 to the outside of the closed kneader 1. The closed kneader 1 is equipped with a stirrer, which can stir and mix the alumina powder and reagent evenly. The drive unit 2 is connected to the stirrer and can drive the stirrer to work. The first end of the sprayer 3 is fixedly installed on the closed kneader 1. Inside the kneader 1, the first end of the sprayer 3 can spray the agent onto the alumina powder inside the closed kneader 1. The first end of the drying conveyor bridge 4 is provided with a receiving port, which is connected to and communicates with the discharge port. The receiving port is used to discharge the mixture of alumina powder and agent obtained in the closed kneader 1 into the drying conveyor bridge 4. The second end of the drying conveyor bridge 4 is provided with a discharge port 5. The drying conveyor bridge 4 can dry and stir the mixture of alumina powder and agent to obtain the carbon monoxide combustion aid product. The drying conveyor bridge 4 can transport the carbon monoxide combustion aid product to the discharge port 5 for discharge, meeting the product production requirements for packaging.
[0024] The carbon monoxide combustion aid production device provided by this utility model uses a closed kneader 1 to mix alumina powder and reagents. This prevents leakage of alumina powder and reagents to the outside environment during the mixing process, avoiding raw material waste and environmental pollution, improving raw material utilization, and thus increasing production efficiency. By installing a sprayer 3 at the first end inside the closed kneader 1 to spray the reagents onto the alumina powder, manual operation and intervention in the reagent spraying process are reduced, spray uniformity is improved, and product quality is enhanced. The alumina powder and reagent mixture obtained in the closed kneader 1 is discharged from the discharge port on the closed kneader 1 to the receiving port opened at the first end of the drying conveyor bridge 4. The mixture of alumina powder and reagent is dried and stirred within the drying and conveying bridge 4, eliminating the need for manual transfer by workers. The mixture is then conveyed to the discharge port 5 to produce the finished carbon monoxide combustion aid. This eliminates the need for workers to remove the carbon monoxide from the oven for stirring, preventing burns and reducing safety risks. Furthermore, the carbon monoxide combustion aid production device provided by this invention effectively reduces manual operation, labor intensity, and manpower consumption, thereby improving production efficiency, ensuring energy conservation, high efficiency, and continuity of production. This facilitates continuous production and guarantees stable product quality.
[0025] As a preferred embodiment of this invention, the driving device 2 includes a motor and a reducer, and the motor, reducer and stirrer are connected in sequence for transmission. The motor is preferably controlled by a frequency converter.
[0026] As a preferred embodiment of this invention, the carbon monoxide combustion aid production device provided by this utility model also includes a reagent supply pump. The second end of the sprayer 3 is placed outside the closed kneader 1, and the second end of the sprayer 3 is connected and communicated with the outlet of the reagent supply pump. This facilitates the mechanized and automated spraying of reagents onto the alumina powder inside the closed kneader 1, reduces manual operation and intervention in the reagent spraying process, improves spraying uniformity, and thus improves product quality and production efficiency.
[0027] As a preferred embodiment of this invention, the carbon monoxide combustion aid production device provided by this utility model also includes a reagent hopper, which can store reagents. The inlet of the reagent supply pump is connected to the reagent hopper. The structure is simple and easy to use.
[0028] In a preferred embodiment of this invention, the sprayer 3 includes a main spray pipe 6, several spray branch pipes 7, and several spray heads 8. The spray heads 8 are placed inside the closed kneader 1 and above the agitator. The number of spray branch pipes 7 is equal to the number of spray heads 8, and each spray branch pipe 7 corresponds to a spray head 8. The first end of the spray branch pipe 7 is fixedly connected to and communicates with the first end of the main spray pipe 6, and the second end of the spray branch pipe 7 is fixedly connected to and communicates with the spray head 8. This facilitates the spraying of the agent onto the alumina powder in the closed kneader 1 at multiple points and evenly, thereby improving the spraying uniformity and the mixing effect of the alumina powder and the agent.
[0029] As a preferred embodiment of this invention, the carbon monoxide combustion aid production device provided by this utility model further includes a powder hopper 9 and a feeding pipe 10. The powder hopper 9 can store alumina powder and is placed above the feed inlet. The top end of the feeding pipe 10 is fixedly connected to and communicates with the bottom end of the powder hopper 9, and the bottom end of the feeding pipe 10 is fixedly connected to and communicates with the feed inlet. When the powder hopper 9 is filled with alumina powder at once, it can continue to produce for a period of time, which can reduce the number of feeding times and save manpower.
[0030] As a preferred embodiment of this invention, the carbon monoxide combustion aid production device provided by this utility model further includes a discharge pipe 11. The first end of the drying conveyor bridge 4 is located below the discharge port. A receiving port is opened on the top surface of the first end of the drying conveyor bridge 4. The top end of the discharge pipe 11 is fixedly connected to and communicates with the discharge port. The bottom end of the discharge pipe 11 is fixedly connected to and communicates with the receiving port. A discharge valve 12 is provided on the discharge pipe 11. The discharge valve 12 can control the opening and closing of the discharge pipe 11. The structure is simple and easy to manufacture and use.
[0031] As a preferred embodiment of this invention, the drying conveyor bridge 4 includes a conveyor shaft, conveyor blades, a conveyor motor, and a conveyor pipe. The first end of the conveyor pipe has a material inlet, and the second end of the conveyor pipe has a material outlet 5. The conveyor shaft and conveyor blades are both placed inside the conveyor pipe. The conveyor blades are spirally fixed on the conveyor shaft. The conveyor shaft can rotate, and the rotation of the conveyor shaft can drive the conveyor blades to rotate. The rotation of the conveyor blades can push the material at the material inlet to the material outlet 5. The conveyor motor is connected to the conveyor shaft and can provide power for the rotation of the conveyor shaft. During the process of the conveyor blades pushing the material at the material inlet to the material outlet 5, the mixture of alumina powder and reagent can be stirred at the same time.
[0032] As a preferred embodiment of this invention, the carbon monoxide combustion aid production device provided by this utility model further includes a return air and dust collection pipe 13, an air and dust collection hood 14, and an axial flow fan 15. A return air port is provided at the second end of the conveying pipe, which is located between the discharge port 5 and the receiving port to achieve reverse ventilation into the conveying pipe. The air and dust collection hood 14 is fixedly installed below the discharge port 5. One end of the return air and dust collection pipe 13 is fixedly connected to and communicates with the air and dust collection hood 14, and the other end of the return air and dust collection pipe 13 is fixedly connected to and communicates with the return air port. The axial flow fan 15 is installed on the return air and dust collection pipe 13. The axial flow fan 15 can send the air and dust at the discharge port 5 into the conveying pipe, which can reduce material waste and recover the heat carried by the hot air and dust at the discharge port 5 for drying the alumina powder and reagent mixture in the conveying pipe, thereby improving energy utilization.
[0033] In a preferred embodiment of this invention, an electric heater 16 is also provided on the return air and dust return pipe 13. The electric heater 16 is placed between the return air inlet and the axial flow fan 15. The electric heater 16 can heat the air and dust in the return air and dust return pipe 13, increase the temperature of the air and dust entering the conveying pipe from the return air inlet, and reduce processing energy consumption by using hot air circulation to achieve drying of the alumina powder and reagent mixture in the conveying pipe. A dryer 17 is also provided on the return air and dust return pipe 13. The dryer 17 is placed between the return air inlet and the electric heater 16. The dryer 17 can dry the air and dust in the return air and dust return pipe 13 and prevent moisture from being introduced into the conveying pipe from the return air inlet. The dryer 17 preferably uses a filler-type, replaceable desiccant.
[0034] As a preferred embodiment of this invention, the conveying pipe is provided with an exhaust pipe 18, which is connected to the part between the return air port and the material receiving port on the conveying pipe. The water vapor generated by the drying material in the conveying pipe leaves the conveying pipe through the exhaust pipe 18 along with the air entering the conveying pipe from the return air port. The exhaust pipe 18 is provided with a dust collector 19, which can effectively reduce dust pollution.
[0035] This utility model uses specific examples to illustrate its principles and implementation methods. The above description of the embodiments is only for the purpose of helping to understand the method and core idea of this utility model. At the same time, for those skilled in the art, there will be changes in the specific implementation methods and application scope based on the idea of this utility model. In summary, the content of this specification should not be construed as a limitation of this utility model.
Claims
1. A carbon monoxide combustion accelerant production apparatus, characterized in that: The system includes a closed kneader, a drive unit, a sprayer, and a drying conveyor bridge. The closed kneader has an inlet and a outlet. The inlet is used to feed alumina powder into the closed kneader, and the outlet is used to discharge the mixture of alumina powder and reagents obtained from the closed kneader to the outside of the closed kneader. A stirrer is installed inside the closed kneader to mix the alumina powder and reagents evenly. The drive unit is connected to the stirrer and drives the stirrer to operate. The first end of the sprayer is fixedly mounted on the closed kneader. Inside, the first end of the sprayer can spray the agent onto the alumina powder inside the closed kneader. The first end of the drying conveyor bridge is provided with a receiving port, which is connected and communicates with the discharge port. The receiving port is used to discharge the mixture of alumina powder and agent obtained in the closed kneader into the drying conveyor bridge. The second end of the drying conveyor bridge is provided with a discharge port. The drying conveyor bridge can dry and stir the mixture of alumina powder and agent to obtain the carbon monoxide combustion aid product. The drying conveyor bridge can transport the carbon monoxide combustion aid product to the discharge port for discharge.
2. The carbon monoxide combustion accelerant production apparatus according to claim 1, characterized in that: It also includes a drug supply pump, with the second end of the sprayer located outside the enclosed kneader, and the second end of the sprayer connected and communicating with the outlet of the drug supply pump.
3. The carbon monoxide combustion aid production apparatus according to claim 2, characterized in that: It also includes a medicine container, which is capable of storing medicine, and the inlet of the medicine supply pump is connected to the medicine container.
4. The carbon monoxide combustion aid production apparatus according to claim 2, characterized in that: The sprayer includes a main spray pipe, several spray branch pipes, and several spray heads. The spray heads are placed inside the closed kneader and above the agitator. The number of spray branch pipes is equal to the number of spray heads. Each spray branch pipe corresponds to a spray head. The first end of each spray branch pipe is fixedly connected to and communicates with the first end of the main spray pipe, and the second end of each spray branch pipe is fixedly connected to and communicates with the spray head.
5. The carbon monoxide combustion aid production apparatus according to claim 1, characterized in that: It also includes a powder hopper and a feeding pipe. The powder hopper is capable of storing alumina powder and is positioned above the feed inlet. The top end of the feeding pipe is fixedly connected to and communicates with the bottom end of the powder hopper, and the bottom end of the feeding pipe is fixedly connected to and communicates with the feed inlet.
6. The carbon monoxide combustion accelerant production apparatus according to claim 1, characterized in that: It also includes a discharge pipe, with the first end of the drying conveyor bridge located below the discharge port. The receiving port is opened on the top surface of the first end of the drying conveyor bridge. The top end of the discharge pipe is fixedly connected to and communicates with the discharge port, and the bottom end of the discharge pipe is fixedly connected to and communicates with the receiving port. The discharge pipe is equipped with a discharge valve, which can control the opening and closing of the discharge pipe.
7. The carbon monoxide combustion accelerant production apparatus according to claim 1, characterized in that: The drying conveyor bridge includes a conveyor shaft, conveyor blades, a conveyor motor, and a conveyor pipe. The first end of the conveyor pipe has the material inlet, and the second end of the conveyor pipe has the material outlet. The conveyor shaft and the conveyor blades are both placed inside the conveyor pipe. The conveyor blades are spirally fixed on the conveyor shaft. The conveyor shaft can rotate, and the rotation of the conveyor shaft can drive the conveyor blades to rotate. The rotation of the conveyor blades can push the material at the material inlet to the material outlet. The conveyor motor is driven by the conveyor shaft and can provide power for the rotation of the conveyor shaft.
8. The carbon monoxide combustion accelerant production apparatus according to claim 7, characterized in that: It also includes a return air and dust return pipe, an air and dust collection hood, and an axial flow fan. A return air port is opened at the second end of the conveying pipe, and the return air port is located between the discharge port and the receiving port. The air and dust collection hood is fixedly installed below the discharge port. One end of the return air and dust return pipe is fixedly connected to and communicates with the air and dust collection hood, and the other end of the return air and dust return pipe is fixedly connected to and communicates with the return air port. The axial flow fan is installed on the return air and dust return pipe, and the axial flow fan can send the air and dust at the discharge port into the conveying pipe.
9. The carbon monoxide combustion accelerant production apparatus according to claim 8, characterized in that: An electric heater is also provided on the return air and dust return duct. The electric heater is placed between the return air inlet and the axial flow fan. The electric heater can heat the air and dust in the return air and dust return duct. A dryer is also provided on the return air and dust return duct. The dryer is placed between the return air inlet and the electric heater. The dryer can dry the air and dust in the return air and dust return duct.
10. The carbon monoxide combustion accelerant production apparatus according to claim 9, characterized in that: The conveying pipe is equipped with an exhaust pipe, which is connected between the return air port and the material receiving port on the conveying pipe, and a dust collector is installed on the exhaust pipe.