Semi-dry reaction tower for flue gas purification of waste incineration power plant
By designing a semi-dry reaction tower for flue gas purification in waste incineration power plants, using gasoline engines and gas heating tanks to generate flue gas, spray water agents and automatically remove residual water agents, the problems of high test costs and inaccurate concentrations in the prior art are solved, and the accuracy of the reaction is improved.
Patent Information
- Application Number
- CN202422537637.6
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-10-21
- Publication Date
- 2025-08-19
- Estimated Expiration
- 2034-10-21
AI Technical Summary
In the preparation of water agents, the prior art uses a proportional gas to generate waste incineration power plant flue gas, resulting in high test costs and inaccurate flue gas concentration. The residual of unreacted water agent affects the accuracy of subsequent reactions.
A semi-dry reaction tower for flue gas purification in waste incineration power plants is designed to generate flue gas through gasoline engines and gas heating tanks, and a water agent is sprayed with a nozzle to react. The residual water agent is automatically discharged through the gate mechanism to avoid reaction with subsequent flue gas.
The automatic generation of flue gas is achieved without distinction between the actual flue gas, saving costs, and ensuring the complete reaction of the water agent, improving the accuracy of the test.
Smart Images
Figure CN223233605U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the field of flue gas treatment in waste incineration power plants, in particular to a semi-dry reaction tower for flue gas purification in waste incineration power plants. Background Art
[0002] When preparing a new aqueous solution in the laboratory, it is necessary to test the reaction rate of the aqueous solution with the flue gas from the waste incineration power plant to determine the reaction rate of the aqueous solution. However, if the flue gas from the waste incineration power plant is generated by mixing various gases in a certain ratio, this will increase the cost of the test, and the concentrations of the flue gas will also be different from the actual flue gas from the waste incineration power plant. In addition, at the beginning of the reaction, the concentration of the exhaust gas is low, making it difficult for the exhaust gas to consume all the aqueous solution, and the unreacted aqueous solution will remain at the bottom of the reaction tank, affecting the accuracy of subsequent reaction tests. For this reason, it is necessary to design a semi-dry reaction tower for waste incineration power plant flue gas purification, which can automatically generate waste incineration power plant flue gas, and the flue gas produced is no different from the flue gas from the waste incineration power plant, and can process the aqueous solution produced at the beginning to avoid reaction with subsequent waste incineration power plant flue gas. Utility Model Content
[0003] The purpose of the utility model is to provide a semi-dry reaction tower for flue gas purification in a waste incineration power plant.
[0004] To achieve this purpose, the present invention adopts the following technical solutions:
[0005] Provided is a semi-dry reaction tower for purifying flue gas from a waste incineration power plant, comprising a gasoline engine, a liquid accumulation tank, a reaction tube, an aqueous solution delivery device, and a plurality of nozzles. The gasoline engine is connected to the liquid accumulation tank via a first pipe, and the gasoline engine is used to deliver flue gas from the waste incineration power plant into the liquid accumulation tank. The reaction tube is fixedly mounted on the top of the liquid accumulation tank and is in communication with the interior of the liquid accumulation tank. A plurality of nozzles are arranged in a vertical array in the reaction tube, and the aqueous solution delivery device is used to deliver aqueous solution to the plurality of nozzles.
[0006] Furthermore, a gas heating tank is provided in the middle of the pipeline 1, and the gas heating tank is used to heat the flue gas of the waste incineration power plant discharged from the gasoline engine toward the liquid accumulation tank.
[0007] Furthermore, the liquid medicine delivery device includes a liquid medicine tank and a liquid medicine delivery pipe, one end of the liquid medicine delivery pipe is provided with multiple branch air pipes, the multiple branch air pipes are respectively connected to the multiple nozzles, and the other end of the liquid medicine delivery pipe is connected to the liquid medicine tank.
[0008] Furthermore, a conical funnel and a gate mechanism are provided inside the liquid accumulation box. The conical funnel is fixedly installed at the bottom of the inner edge of the liquid accumulation box. A liquid outlet is provided at the bottom of the conical funnel. The gate mechanism is used to control the opening and closing of the liquid outlet. A liquid outlet pipe is provided on the outer edge of the liquid accumulation box, and the liquid outlet pipe is located below the conical funnel.
[0009] Furthermore, the gate mechanism includes a gate plate, an electric push rod and two guide columns. The gate plate covers the bottom of the liquid outlet. The two guide columns are fixedly installed at both ends of the gate plate. Both guide columns pass through the outer wall of the liquid accumulation box and are slidably connected to the liquid accumulation box. The electric push rod is located on the outside of the liquid accumulation box, and the output end of the electric push rod is fixedly connected to one end of one of the guide columns.
[0010] Furthermore, a heating tube is provided in the gas heating tank, and the power of the heating tube is adopted.
[0011] The beneficial effects of the utility model are as follows: the semi-dry reaction tower for flue gas purification of the waste incineration power plant can automatically generate waste incineration power plant flue gas through a gasoline engine and a gas heating tank, and the flue gas produced is no different from the flue gas of the waste incineration power plant, and the water agent remaining at the beginning of the reaction can be opened through the gate mechanism so that the water agent can be automatically discharged, thereby realizing the treatment of the water agent generated at the beginning and avoiding reaction with the subsequent waste incineration power plant flue gas. BRIEF DESCRIPTION OF THE DRAWINGS
[0012] In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the following briefly introduces the drawings required for use in the embodiments of the present invention.
[0013] Figure 1 It is a schematic diagram of the three-dimensional structure of the utility model;
[0014] Figure 2 It is a partial cross-sectional view of the utility model;
[0015] Figure 3 Schematic diagram of the three-dimensional structure of the gate mechanism;
[0016] In the figure: 1. Gasoline engine; 2. Gas heating tank; 3. Liquid accumulation tank; 3a. Liquid outlet pipe; 4. Reaction tube; 5. Water agent delivery pipe; 6. Nozzle; 7. Water agent tank; 8. Conical funnel; 8a. Liquid outlet; 9. Gate mechanism; 9a. Gate plate; 9b. Guide column; 9c. Electric push rod. DETAILED DESCRIPTION
[0017] The technical solution of the present invention will be further described below with reference to the accompanying drawings and through specific implementation methods.
[0018] Among them, the drawings are only used for illustrative purposes and represent only schematic diagrams rather than actual pictures, and should not be understood as limitations on this patent; in order to better illustrate the embodiments of the utility model, some parts of the drawings may be omitted, enlarged or reduced, and do not represent the size of the actual product.
[0019] Reference Figures 1 to 3 The illustrated semi-dry reactor for purifying flue gas from a waste incineration power plant comprises a gasoline engine 1, a liquid storage tank 3, a reaction tube 4, an aqueous solution delivery device, and multiple nozzles 6. The gasoline engine 1 is connected to the liquid storage tank 3 via a pipe 1 and is used to deliver waste incineration power plant flue gas into the liquid storage tank 3. The gas produced by the gasoline engine 1 is waste incineration power plant flue gas, avoiding the need for a ratio-based method to produce waste incineration power plant flue gas, saving costs, and achieving a gas concentration comparable to waste incineration power plant flue gas. The reaction tube 4 is fixedly mounted on the top of the liquid storage tank 3 and communicates with the interior of the liquid storage tank 3. Multiple nozzles 6 are arranged in a vertical array within the reaction tube 4. The aqueous solution delivery device delivers aqueous solution to the multiple nozzles 6, causing the aqueous solution to be sprayed along the nozzles 6. The sprayed aqueous solution reacts with the waste incineration power plant flue gas in the reaction tube 4, while some unreacted aqueous solution reacts with the waste incineration power plant flue gas in the liquid storage tank 3.
[0020] Among them, a gas heating tank 2 is provided in the middle of the pipeline 1, and the gas heating tank 2 is used to heat the flue gas from the waste incineration power plant discharged by the gasoline engine 1 toward the liquid storage tank 3, so that the heated gas can simulate the flue gas from the waste incineration power plant in terms of temperature, avoiding the influence of temperature on the accuracy of the test.
[0021] The liquid medicine delivery device includes a liquid medicine tank 7 and a liquid medicine delivery pipe 5. A plurality of branch air pipes are provided on one end of the liquid medicine delivery pipe 5, and the plurality of branch air pipes are respectively connected to a plurality of nozzles 6. The other end of the liquid medicine delivery pipe 5 is connected to the liquid medicine tank 7. A pump body is provided on the liquid medicine tank 7. The pump body draws out the liquid medicine inside the liquid medicine tank 7 and transports it along the liquid medicine delivery pipe 5 so that it can be sprayed along the plurality of nozzles 6.
[0022] The interior of the liquid accumulating tank 3 is provided with a conical funnel 8 and a gate mechanism 9. The conical funnel 8 is fixedly mounted on the inner bottom of the liquid accumulating tank 3. The bottom of the conical funnel 8 is provided with a liquid outlet 8a. The gate mechanism 9 is used to control the opening and closing of the liquid outlet 8a. At the beginning of the reaction, the unreacted aqueous solution will fall onto the conical funnel 8, and then the gate mechanism 9 will be opened, and the aqueous solution will be discharged along the liquid outlet 8a, that is, the aqueous solution will enter between the conical funnel 8 and the bottom of the liquid accumulating tank 3, avoiding the subsequent waste incineration power plant flue gas. A liquid outlet pipe 3a is provided on the outer edge of the liquid accumulating tank 3. The liquid outlet pipe 3a is located below the conical funnel 8. When it is necessary to clean the aqueous solution between the conical funnel 8 and the bottom of the liquid accumulating tank 3, the valve connected to the liquid outlet pipe 3a will be opened to allow the aqueous solution to be discharged to the outside of the liquid accumulating tank 3.
[0023] The gate mechanism 9 includes a gate plate 9a, an electric push rod 9c, and two guide posts 9b. The gate plate 9a covers the bottom of the liquid outlet 8a. The two guide posts 9b are fixedly mounted at both ends of the gate plate 9a. Both guide posts 9b penetrate the outer wall of the liquid storage tank 3 and are slidably connected to the liquid storage tank 3. The electric push rod 9c is located outside the liquid storage tank 3, and the output end of the electric push rod 9c is fixedly connected to one end of one of the guide posts 9b. By controlling the electric push rod 9c to operate, the electric push rod 9c pulls the guide post 9b to move horizontally, which drives the gate plate 9a to cover and move, so that the gate plate 9a opens or closes the liquid outlet 8a. The guide posts 9b mainly guide the movement of the gate plate 9a. And because the gate plate 9a covers the liquid outlet 8a during the reaction, air leakage between the guide posts 9b and the liquid storage tank 3 is avoided.
[0024] A heating pipe is provided in the gas heating tank 2, and the power of the heating pipe is 3KW.
[0025] The gas heating tank 2 has a diameter of 300 mm and a height of 500 mm. The liquid storage tank 3 has a diameter of 600 mm and a height of 600 mm. The reaction tube 4 has a diameter of 50 mm and a length of 2000 mm. The aqueous solution tank 7 has a diameter of 600 mm and a height of 400 mm.
[0026] The above are only preferred embodiments of the present invention. It should be pointed out that for ordinary technicians in this technical field, several improvements and modifications can be made without departing from the technical principles of the present invention. These improvements and modifications should also be regarded as the scope of protection of the present invention.
Claims
1. A semi-dry reaction tower for flue gas purification in a waste incineration power plant, characterized in that: The invention comprises a gasoline engine (1), a liquid storage tank (3), a reaction tube (4), a water agent delivery device and a plurality of nozzles (6), wherein the gasoline engine (1) is connected to the liquid storage tank (3) through a pipe 1, the gasoline engine (1) is used to deliver waste incineration power plant flue gas into the liquid storage tank (3), the reaction tube (4) is fixedly installed on the top of the liquid storage tank (3), the reaction tube (4) is connected to the inside of the liquid storage tank (3), the plurality of nozzles (6) are arranged in a vertical array in the reaction tube (4), and the water agent delivery device is used to deliver the water agent to the plurality of nozzles (6).
2. A semi-dry reaction tower for flue gas purification in a waste incineration power plant according to claim 1, characterized in that: A gas heating tank (2) is provided in the middle of the pipeline 1, and the gas heating tank (2) is used to heat the waste incineration power plant flue gas discharged from the gasoline engine (1) toward the liquid storage tank (3).
3. A semi-dry reaction tower for flue gas purification in a waste incineration power plant according to claim 2, characterized in that: The liquid medicine delivery device comprises a liquid medicine tank (7) and a liquid medicine delivery pipe (5); a plurality of branch air pipes are provided on one end of the liquid medicine delivery pipe (5); the plurality of branch air pipes are respectively connected to a plurality of nozzles (6); and the other end of the liquid medicine delivery pipe (5) is connected to the liquid medicine tank (7).
4. A semi-dry reaction tower for flue gas purification in a waste incineration power plant according to claim 2, characterized in that: A conical funnel (8) and a gate mechanism (9) are provided inside the liquid accumulation box (3). The conical funnel (8) is fixedly installed at the bottom of the inner edge of the liquid accumulation box (3). A liquid outlet (8a) is provided at the bottom of the conical funnel (8). The gate mechanism (9) is used to control the opening and closing of the liquid outlet (8a). A liquid outlet pipe (3a) is provided on the outer edge of the liquid accumulation box (3). The liquid outlet pipe (3a) is located below the conical funnel (8).
5. A semi-dry reaction tower for flue gas purification in a waste incineration power plant as claimed in claim 4, characterized in that: The gate mechanism (9) includes a gate plate (9a), an electric push rod (9c) and two guide pillars (9b). The gate plate (9a) covers the bottom of the liquid outlet (8a). The two guide pillars (9b) are fixedly mounted on both ends of the gate plate (9a). Both guide pillars (9b) pass through the outer wall of the liquid storage box (3) and are slidably connected to the liquid storage box (3). The electric push rod (9c) is located outside the liquid storage box (3), and the output end of the electric push rod (9c) is fixedly connected to one end of one of the guide pillars (9b).
6. A semi-dry reaction tower for flue gas purification in a waste incineration power plant according to claim 5, characterized in that: A heating tube is provided in the gas heating tank (2), and the power of the heating tube is 3KW.