Bromine steaming device capable of comprehensively utilizing heat energy

Abstract

The utility model is applicable to the technical field of bromine steaming, and provides a thermal energy comprehensive utilization bromine steaming device which comprises a first tank body, a second tank body is arranged in the first tank body, a cover plate is arranged on the top surface of the first tank body and the top surface of the second tank body, a heating box is arranged in the second tank body, and a condensation tank is arranged above the cover plate. An inverted-U-shaped pipe is arranged in the condensation tank, a first guide pipe is arranged on the top face of the second tank body in a communicating mode, a second guide pipe and a third guide pipe are connected to the portion, located on the outer side of the second tank body, of the top face of the first tank body, the first guide pipe and the second guide pipe are connected with the two ends of the inverted-U-shaped pipe respectively, and an exhaust pipe is arranged on the top of the inverted-U-shaped pipe in a communicating mode. And the third guide pipe is communicated with the top of the inverted U-shaped pipe. According to the scheme, continuous bromine steaming operation can be realized in one device without connecting a plurality of bromine steaming devices in series, so that the utilization rate of heat is improved, energy waste is avoided, and the bromine steaming effect is greatly improved.

Description

Technical Field

[0001] This utility model belongs to the field of bromine distillation technology, and in particular relates to a bromine distillation device that comprehensively utilizes thermal energy. Background Technology

[0002] Bromine evaporation usually refers to the evaporation process of bromine. A bromine evaporation device is a device used to evaporate liquid bromine and convert it into gas. Bromine is a chemical element with a strong pungent odor, commonly found as a reddish-brown liquid, which can evaporate into a gas at room temperature.

[0003] Chinese patent application number CN202321883649.3, publication number CN220677052U, discloses a filtration device for hydrobromic acid production, relating to the field of hydrobromic acid production technology. The device includes a protective shell with a feed pipe installed on its top and a discharge pipe installed on its side wall. Several filter components are installed inside the protective shell. Each filter component includes a sealing shell and a filter bag, with the filter bag installed inside the sealing shell. The feed pipe is connected to one end of the sealing shell, and one end of the filter bag is connected to the discharge pipe. Solenoid valves are installed between the feed pipe and the sealing shell, and between the discharge pipe and the filter bag. This design, through the coordinated operation of several filter components, allows for easy maintenance even if a single filter component malfunctions; only the liquid supply to that component needs to be stopped, without requiring a complete shutdown. This design ensures production efficiency and reduces labor and maintenance costs.

[0004] Existing bromine distillation devices only heat the solution inside the container once during use, resulting in significant energy waste. Moreover, multiple bromine distillation devices are usually connected in series to improve the bromine distillation effect, which leads to large equipment space and high energy consumption. In response to this, this application proposes a bromine distillation device that integrates thermal energy utilization. Utility Model Content

[0005] The purpose of this invention is to provide a thermal energy comprehensive utilization bromine distillation device to solve the problems mentioned in the background art.

[0006] To achieve the above objectives, this utility model provides the following technical solution: a thermal energy comprehensive utilization bromine distillation device, comprising a first tank, a second tank inside the first tank, a cover plate shared on the top surfaces of the first tank and the second tank, a heating box inside the second tank, a condenser tank above the cover plate, an inverted U-shaped tube inside the condenser tank, a first conduit connected to the top surface of the second tank, a second conduit and a third conduit connected to the top surface of the first tank outside the second tank, the first conduit and the second conduit respectively connected to the two ends of the inverted U-shaped tube, an exhaust pipe connected to the top of the inverted U-shaped tube, the exhaust pipe penetrating the condenser tank and extending to the top of the condenser tank, and the third conduit connected to the top of the inverted U-shaped tube.

[0007] Preferably, the side wall of the condenser is provided with an inlet pipe and an outlet pipe, the inlet pipe being located at the bottom of the condenser and the outlet pipe being located at the top of the condenser.

[0008] Preferably, the inverted U-shaped tube is a spherical tube, and the top surface of the second tank is connected to a feed pipe.

[0009] Preferably, the first tank and the condenser are connected by a support frame, which is shaped like a gate.

[0010] Preferably, the heating box is equipped with a heating wire inside, and the heating wire is electrically connected to a power supply and a temperature control system.

[0011] Preferably, the bottom surface of the second tank is connected to a first liquid outlet pipe, the first liquid outlet pipe penetrates the bottom surface of the first tank, and the bottom surface of the first tank is connected to a second liquid outlet pipe.

[0012] This utility model has at least the following beneficial effects:

[0013] This utility model provides a thermal energy comprehensive utilization bromine distillation device. By cooperating with the first tank, the second tank, and the condenser, multiple bromine distillation devices can be connected in series, and continuous bromine distillation can be achieved in one device. This not only improves the utilization rate of heat and avoids energy waste, but also greatly improves the bromine distillation effect. Attached Figure Description

[0014] Figure 1 This is a schematic diagram of the internal structure of the present invention;

[0015] Figure 2 This is a schematic diagram of the external structure of this utility model;

[0016] Figure 3 This is a schematic diagram of the internal structure of the heating box of this utility model.

[0017] In the attached diagram, the following are the reference numerals: 1. First tank; 2. Second tank; 3. Cover plate; 4. Heating box; 5. Support; 6. Condenser; 7. Feed pipe; 8. First conduit; 9. Second conduit; 10. Inverted U-shaped pipe; 11. Exhaust pipe; 12. Third conduit; 13. Water inlet pipe; 14. Water outlet pipe; 15. First liquid outlet pipe; 16. Second liquid outlet pipe; 17. Heating wire. Detailed Implementation

[0018] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments of the present utility model. 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 skilled in the art without creative effort are within the scope of protection of the present utility model.

[0019] Example

[0020] Please see Figure 1 , Figure 2 and Figure 3 This utility model provides a technical solution: a thermal energy comprehensive utilization bromine distillation device, including a first tank 1, a second tank 2 inside the first tank 1, a cover plate 3 on the top surface of the first tank 1 and the second tank 2, specifically, the cover plate 3 is fixedly connected to both the first tank 1 and the second tank 2, a heating box 4 inside the second tank 2, specifically, the heating box 4 is fixedly connected to the second tank 2, a condenser 6 above the cover plate 3, an inverted U-shaped tube 10 inside the condenser 6, a first conduit 8 connected to the top surface of the second tank 2, a second conduit 9 and a third conduit 12 connected to the top surface of the first tank 1 outside the second tank 2, the first conduit 8 and the second conduit 9 respectively connected to the two ends of the inverted U-shaped tube 10, specifically, the first conduit 8 and the second conduit 9 respectively fixedly connected to the two ends of the inverted U-shaped tube 10, an exhaust pipe 11 connected to the top of the inverted U-shaped tube 10, the exhaust pipe 11 penetrates the condenser 6 and extends to the top of the condenser 6, and the third conduit 12 is connected to the top of the inverted U-shaped tube 10.

[0021] In this embodiment, the heating box 4 heats the bromine-containing mixture in the second tank 2. Steam enters the first conduit 8 and then the inverted U-shaped tube 10. Cold water or condensate is added to the condenser 6 for condensation. Bromine gas is discharged through the exhaust pipe 11. The condensed solution enters the second conduit 9 and then the cavity between the first tank 1 and the second tank 2. The cavity is heated by the heat radiated from the heating box 4. Steam enters the inverted U-shaped tube 10 through the third conduit 12. Bromine gas is discharged through the exhaust pipe 11. The condensed solution is thus condensed. Therefore, without the need for multiple bromine evaporation devices, continuous bromine evaporation can be achieved, and thermal energy can be utilized to the maximum extent.

[0022] Furthermore, the side wall of the condenser 6 is provided with a water inlet pipe 13 and a water outlet pipe 14. The water inlet pipe 13 is located at the bottom of the condenser 6, and the water outlet pipe 14 is located at the top of the condenser 6.

[0023] In this embodiment, circulating condensate is formed in the condenser tank 6 through the inlet pipe 13 and the outlet pipe 14. The inlet pipe 13 is located at the bottom of the condenser tank 6, and the outlet pipe 14 is located at the top of the condenser tank 6, which can reduce the flow rate of the circulating condensate and improve the condensation effect.

[0024] Furthermore, the inverted U-shaped tube 10 is a spherical tube, and the top surface of the second tank 2 is connected to a feed pipe 7.

[0025] In this embodiment, the inverted U-shaped tube 10 is a spherical tube, which can reduce the steam flow rate, improve the condensation effect, and avoid backflow; the feed pipe 7 facilitates the injection of a bromine-containing mixed solution into the second tank 2, which is convenient for bromine distillation operation.

[0026] Furthermore, the first tank 1 and the condenser tank 6 are connected together by a bracket 5, which is shaped like a gate.

[0027] In this embodiment, both the first tank 1 and the condenser tank 6 are fixedly connected to the bracket 5, which facilitates the fixation of the entire device.

[0028] Furthermore, the heating box 4 is equipped with a heating wire 17, which is electrically connected to a power supply and a temperature control system.

[0029] In this embodiment, the heating wire 17 is used for temperature control and heating to provide the heat required for bromine distillation.

[0030] Furthermore, the bottom surface of the second tank 2 is connected to a first liquid outlet pipe 15, which penetrates the bottom surface of the first tank 1, and the bottom surface of the first tank 1 is connected to a second liquid outlet pipe 16.

[0031] In this embodiment, the solution after bromine distillation is discharged and recovered through the first outlet pipe 15 and the second outlet pipe 16.

[0032] The working principle and usage process of this utility model: After the utility model is installed, work according to the above implementation method until all working steps are completed.

[0033] The foregoing has shown and described the basic principles, main features, and advantages of this utility model. It will be apparent to those skilled in the art that this utility model is not limited to the details of the exemplary embodiments described above, and that it can be implemented in other specific forms without departing from the spirit or basic characteristics of this utility model. Therefore, the embodiments should be considered exemplary and non-limiting in all respects. The scope of this utility model is defined by the appended claims rather than the foregoing description. Therefore, it is intended that all variations falling within the meaning and scope of equivalents of the claims be included within this utility model, and no reference numerals in the claims should be construed as limiting the scope of the claims.

[0034] Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made to these embodiments without departing from the principles and spirit of the present invention, the scope of which is defined by the appended claims and their equivalents.

Claims

1. A thermal energy comprehensive utilization bromine distillation device, characterized in that, The system includes a first tank (1), inside which is a second tank (2). The top surfaces of the first tank (1) and the second tank (2) are provided with a cover plate (3). Inside the second tank (2) is a heating box (4). Above the cover plate (3) is a condenser tank (6). Inside the condenser tank (6) is an inverted U-shaped tube (10). The top surface of the second tank (2) is connected to a first conduit (8). The top surface of the first tank (1) is located outside the second tank (2) and connected to a second conduit (9) and a third conduit (12). The first conduit (8) and the second conduit (9) are respectively connected to the two ends of the inverted U-shaped tube (10). The top of the inverted U-shaped tube (10) is connected to an exhaust pipe (11). The exhaust pipe (11) passes through the condenser tank (6) and extends to the top of the condenser tank (6). The third conduit (12) is connected to the top of the inverted U-shaped tube (10).

2. The thermal energy comprehensive utilization bromine distillation device according to claim 1, characterized in that: The side wall of the condenser (6) is provided with an inlet pipe (13) and an outlet pipe (14). The inlet pipe (13) is located at the bottom of the condenser (6), and the outlet pipe (14) is located at the top of the condenser (6).

3. The thermal energy comprehensive utilization bromine distillation device according to claim 1, characterized in that: The inverted U-shaped tube (10) is a spherical tube, and the top surface of the second tank (2) is connected to a feed pipe (7).

4. The thermal energy comprehensive utilization bromine distillation device according to claim 1, characterized in that: The first tank (1) and the condenser (6) are connected together by a bracket (5), which is in the shape of a door.

5. The thermal energy comprehensive utilization bromine distillation device according to claim 1, characterized in that: The heating box (4) is equipped with a heating wire (17) inside, and the heating wire (17) is electrically connected to a power supply and a temperature control system.

6. The thermal energy comprehensive utilization bromine distillation device according to claim 1, characterized in that: The bottom surface of the second tank (2) is connected to a first liquid outlet pipe (15), which penetrates the bottom surface of the first tank (1), and the bottom surface of the first tank (1) is connected to a second liquid outlet pipe (16).

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