Gas cooling apparatus and heat furnace

Abstract

The present application discloses a gas cooling apparatus and a heat furnace. The gas cooling apparatus comprises a pipeline structure. The pipeline structure defines a gas flow channel and a liquid channel; the gas flow channel is used for circulating a high-temperature gas; and the liquid channel is located outside the gas flow channel and is provided with a liquid spraying part communicated with the gas flow channel. The pipeline structure is further provided with a gas spraying part communicated with the gas flow channel; and a liquid sprayed from the liquid spraying part can be atomized under the action of the high-temperature gas in the gas flow channel and the high-pressure gas sprayed from the gas spraying part. The gas cooling apparatus has the advantages of simple structure, convenient use, rapid cooling rate for a high-temperature gas, and less use of a cooling liquid.

Description

Gas cooling device and hot furnace

[0001] This application claims priority to Chinese Patent Application No. 202321541270.4, filed on June 16, 2023, entitled “Gas Cooling Device”, the entire contents of which are incorporated herein by reference.

[0002] This application claims priority to Chinese Patent Application No. 202310716600.7, filed on June 16, 2023, entitled "A Heat Dissipation Device", the entire contents of which are incorporated herein by reference. Technical Field

[0003] This application relates to the field of semiconductor processing technology, and in particular to a gas cooling device and a furnace. Background Technology

[0004] The equipment used in photovoltaic deposition or diffusion processes is a hot furnace. During operation, the temperature inside the furnace can reach thousands of degrees Celsius. The gas discharged from the hot furnace needs to be cooled before it can be discharged. Existing exhaust cooling structures usually involve wrapping cold water pipes around the exhaust pipes to achieve exhaust cooling. However, this cooling method is inefficient, and the cold water pipes are very easy to be damaged by the exhaust pipes. Regular maintenance and replacement are required, making the maintenance and operation of the exhaust cooling structure very complicated and inconvenient to use.

[0005] Therefore, there is an urgent need for a gas cooling device that can achieve rapid cooling and is easy to use.

[0006] Summary of the Invention

[0007] The primary objective of this application is to provide a gas cooling device and a furnace, wherein the gas cooling device has a simple structure, is easy to use, has a fast cooling rate for high-temperature gases, and uses a small amount of cooling liquid.

[0008] To achieve the above-mentioned technical effects, the technical solution of this application is as follows:

[0009] This application discloses a gas cooling device, including a pipeline structure that defines an airflow channel and a liquid channel. The airflow channel is used to circulate high-temperature gas, and the liquid channel is located outside the airflow channel and has a liquid spraying part that communicates with the airflow channel. The pipeline structure also has a jet spraying part that communicates with the airflow channel. The liquid sprayed from the liquid spraying part can be vaporized under the action of the high-temperature gas in the airflow channel and the high-pressure gas sprayed from the jet spraying part.

[0010] In some specific embodiments, the gas channel includes a high-temperature zone located at one end of the gas channel near the direction of high-temperature gas inflow; the liquid channel includes a cooling channel and a liquid storage chamber, the cooling channel having a liquid inlet connected to an external liquid source, and the cooling channel being located outside the high-temperature zone; the liquid storage chamber has a connecting port and a spraying section, the connecting port being connected to the cooling channel, and the flow area of ​​the connecting port being smaller than the flow area of ​​the cooling channel and the liquid storage chamber.

[0011] In some specific embodiments, the gas cooling device further includes a liquid inlet pipe, one end of which is connected to the pipeline structure and communicates with the liquid inlet, and the other end of which is connected to an external liquid source.

[0012] In some specific embodiments, the gas cooling device further includes a guide pipe located within the cooling channel, which is used to allow the liquid in the cooling channel to approximately fill the cooling channel before flowing into the liquid storage chamber.

[0013] In some specific embodiments, the inlet of the guide pipe is connected to the cooling channel, the inlet of the guide pipe is located at the air inlet end of the airflow channel, and the outlet of the guide pipe is connected to the liquid storage chamber, so that the liquid in the cooling channel flows into the liquid storage chamber along the guide pipe.

[0014] In some specific embodiments, the guide tube includes a first section and a second section. The first section is connected to the liquid channel, and the second section is connected to the liquid storage chamber. The position where the first section and the second section are connected is higher than the air inlet end of the airflow channel.

[0015] In some specific embodiments, the guide tube is a bent tube, with the inlet of the bent tube connected to the liquid channel and the outlet of the bent tube connected to the liquid storage chamber, and the bend of the bent tube is higher than the air inlet end of the airflow channel.

[0016] In some specific embodiments, there are multiple spray sections, and the multiple spray sections are distributed at intervals along the circumference of the airflow channel.

[0017] In some specific embodiments, the jet section is inclined, and the extending direction of the liquid spray section intersects with the extending direction of the jet section.

[0018] In some specific embodiments, the pipeline structure also defines an air storage chamber, which can be connected to an external air source, and the jet nozzle is connected to the air storage chamber.

[0019] In some specific embodiments, the flow area of ​​the gas storage chamber gradually decreases along the gas flow direction in the airflow channel, and the jet is disposed on the inclined side wall of the gas storage chamber facing the airflow channel.

[0020] In some specific embodiments, the gas cooling device further includes an air inlet pipe, one end of which is connected to the gas storage chamber and the other end of which is connected to an external high-pressure gas source.

[0021] In some specific embodiments, there are multiple jet units, and the multiple jet units are distributed at circumferential intervals along the airflow channel.

[0022] In some specific embodiments, the airflow channel includes a high-temperature zone, an atomization zone, and a vaporization zone arranged sequentially along the airflow direction. Part of the liquid channel is located outside the high-temperature zone, and both the jetting part and the liquid spraying part are connected to the atomization zone.

[0023] This application discloses a gas cooling device, including a pipeline structure that defines an airflow channel and a liquid channel. The airflow channel is used to circulate high-temperature gas, and the liquid channel is located outside the airflow channel and has a spray section that communicates with the airflow channel. The spray section is used to spray liquid toward the airflow channel.

[0024] In some specific embodiments, the airflow channel has an inlet end and an outlet end. The inlet end is used to introduce high-temperature gas, and the liquid channel has a liquid inlet. The liquid channel also includes a connecting pipe. The outlet of the connecting pipe is located at the outlet end. The inlet of the connecting pipe is connected to the liquid channel, and the outlet of the connecting pipe is connected to the airflow channel to spray liquid toward the airflow channel. The spraying part is located at the outlet of the connecting pipe, and the outlet of the connecting pipe sprays liquid toward the airflow channel through the spraying part.

[0025] In some specific embodiments, the airflow channel is inclined, and the air inlet is higher than the air outlet.

[0026] In some specific embodiments, the connecting pipe includes a first pipe body and a second pipe body. The first pipe body is connected to a liquid channel, and the second pipe body is connected to an airflow channel. The position where the first pipe body and the second pipe body are connected is higher than the air inlet end of the airflow channel.

[0027] In some specific embodiments, the connecting pipe also includes a third pipe body, the two ends of which are connected to the first pipe body and the second pipe body respectively, and the third pipe body is higher than the air inlet end of the airflow channel.

[0028] In some specific embodiments, the connecting pipe is a bent pipe, the inlet of which is connected to the liquid channel, the outlet of which is connected to the airflow channel, and the bend of the bent pipe is higher than the air inlet of the airflow channel.

[0029] In some specific embodiments, the gas cooling device further includes a fan disposed within the piping structure to drive the forced flow of gas within the airflow channel.

[0030] In some specific embodiments, the gas cooling device further includes an exhaust pipe, one end of which is connected to the outlet end of the airflow channel, and the other end is used to install a fan. The end of the exhaust pipe where the fan is installed is lower than the end connected to the outlet end.

[0031] In some specific embodiments, the gas cooling device further includes an exhaust pipe connected to the side of the fan away from the exhaust pipe.

[0032] This application discloses a furnace, including a furnace body and the aforementioned gas cooling device, wherein the furnace body has an exhaust pipe; the gas cooling device is used to cool the gas released from the furnace body through the exhaust pipe.

[0033] The beneficial effects of the gas cooling device of this application are as follows: Compared with the prior art of winding cold water pipes around the exhaust pipe, the pipeline structure of the high-temperature gas cooling device of this application is connected to the outlet of the exhaust pipe, which is convenient to use and not easily damaged by the exhaust pipe, and has a longer service life; During operation, after the high-temperature gas enters the airflow channel, the liquid channel is set outside the airflow channel, which can cool the high-temperature gas. The liquid in the liquid channel can also be sprayed from the spraying part to the airflow channel. The sprayed liquid will vaporize sequentially under the combined action of the high-pressure gas sprayed by the jetting part and the high-temperature gas. The vaporization of the liquid can carry away a large amount of heat. Since the gas cooling device can carry away a large amount of heat through liquid cooling and liquid vaporization, it can achieve rapid cooling of high-temperature gas, improve the cooling rate and cooling efficiency; Since the jetting part can spray high-pressure gas towards the airflow channel, the liquid sprayed towards the airflow channel is atomized, which can make full use of the sprayed liquid to cool the high-temperature gas and reduce the amount of sprayed liquid used; Since the liquid channel is set outside the airflow channel, the structural materials of the entire pipeline can be conventional materials, without the need to use special high-temperature resistant materials, thus reducing the manufacturing cost of the gas cooling device.

[0034] Additional aspects and advantages of this application will be set forth in part in the description which follows, and in part will be obvious from the description, or may be learned by practice of this application. Attached Figure Description

[0035] Figure 1 is a cross-sectional structural schematic diagram of a gas cooling device in one embodiment of this application;

[0036] Figure 2 is a magnified view of part II in Figure 1;

[0037] Figure 3 is a schematic diagram of the structure of a gas cooling device in one embodiment of this application;

[0038] Figure 4 is a partial cross-sectional structural schematic diagram of a gas cooling device in one embodiment of this application;

[0039] Figure 5 is a schematic diagram of the internal structure of a gas cooling device in one embodiment of this application;

[0040] Figure 6 is a three-dimensional structural schematic diagram of a gas cooling device in one embodiment of this application;

[0041] Figure 7 is a cross-sectional structural schematic diagram of the gas cooling device shown in Figure 6;

[0042] Figure 8 is a partial cross-sectional structural schematic diagram of the gas cooling device shown in Figure 6;

[0043] Figure 9 is a structural block diagram of a furnace in one embodiment of this application.

[0044] The reference numerals in the accompanying drawings are as follows: 1. Hot furnace; 100. Gas cooling device; 200. Furnace body; 10. Piping structure; 11. Airflow channel; 111. High-temperature zone; 112. Atomization zone; 1121. Gradient section; 1122. Straight section; 113. Vaporization zone; 114. Inlet; 115. Outlet; 12. Liquid channel; 121. Cooling channel; 1211. Liquid inlet; 1212. First Section; 1213, Second section; 122, Liquid storage chamber; 1221, Connecting port; 13, Spraying part; 14, Jet part; 15, Gas storage chamber; 20, Liquid inlet pipe; 30, Guide pipe; 31, First pipe section; 32, Second pipe section; 33, Inlet; 40, Air inlet pipe; 50, Connecting pipe; 51, First pipe body; 52, Second pipe body; 53, Third pipe body; 60, Fan; 70, Extraction pipe; 80, Exhaust pipe. Detailed Implementation

[0045] To make the technical problems solved, the technical solutions, and the beneficial effects of this invention clearer, the invention will be further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.

[0046] This application discloses a gas cooling device 100, as shown in Figures 1, 2 and 9. The gas cooling device 100 includes a pipeline structure 10, which defines an airflow channel 11 and a liquid channel 12. The airflow channel 11 is used to circulate high-temperature gas. The liquid channel 12 is located outside the airflow channel 11 and has a liquid spraying part 13 communicating with the airflow channel 11. The pipeline structure 10 also has a jet spraying part 14 communicating with the airflow channel 11. The liquid sprayed by the liquid spraying part 13 can be vaporized under the action of the high-temperature gas in the airflow channel 11 and the high-pressure gas sprayed by the jet spraying part 14.

[0047] [Cited in Article (20.6) 16.12.2025] First, it should be noted that, taking water as an example, the specific heat capacity of water is 4.2 J (g·℃), and the latent heat of vaporization at 100℃ is 2257.2 kJ / kg. Therefore, during the vaporization phase change, the heat energy absorbed is much greater than that of conventional water cooling schemes.

[0048] It is understood that the terms "high temperature" and "high pressure" in the "high temperature gas" and "high pressure gas" described in the embodiments of this application have the meanings commonly understood by those skilled in the art, and do not impose specific numerical limitations on the temperature and pressure of the gas.

[0049] Understandably, in actual use, the pipeline structure 10 is connected to the exhaust pipe of the furnace 1. After the high-temperature gas enters the airflow channel 11, the liquid channel 12 outside the airflow channel 11 can cool the high-temperature gas. The liquid in the liquid channel 12 can also be sprayed from the spray section 13 to the airflow channel 11. The sprayed liquid will be rapidly atomized when it encounters the high-pressure gas sprayed from the jet section 14. The atomized liquid will mix with the high-temperature gas. When the atomized liquid encounters the high-temperature gas, it will quickly vaporize and become steam. When the liquid vaporizes, it absorbs a large amount of heat, thereby ensuring that the temperature of the high-temperature gas drops rapidly. When the high-temperature gas is discharged from the pipeline structure 10, it will have a lower temperature.

[0050] It should be noted that the atomization process and the vaporization process may not be strictly sequential. The sprayed liquid may be atomized under the action of high-pressure gas and then vaporized under the action of high-temperature gas, or it may be directly vaporized under the combined action of high-pressure gas and high-temperature gas. In actual operation, the phase change process of the liquid may be quite complex. For the sake of explanation, the atomization process and the vaporization process are described separately here.

[0051] Compared to the existing technology of wrapping cold water pipes around the exhaust pipe, the pipe structure 10 of this application is connected to the exhaust outlet of the exhaust pipe, which is convenient to use and not easily damaged by the exhaust pipe, and has a longer service life. During operation, liquid cooling and liquid vaporization can remove a large amount of heat, achieving rapid cooling of high-temperature gas and improving cooling rate and cooling efficiency. Since the jet part 14 can spray high-pressure gas toward the airflow channel 11, the liquid sprayed toward the airflow channel 11 is atomized, which can make full use of the sprayed liquid to cool the high-temperature gas and reduce the amount of sprayed liquid used.

[0052] It should be noted that, since a liquid channel 12 is provided outside the airflow channel 11, the existence of the liquid channel 12 can ensure that the temperature of the outer tube of the pipeline structure 10 is relatively safe, and the temperature of the outer wall cannot exceed the boiling point of water. On the other hand, it reduces the temperature of the inner tube of the pipeline structure 10, so that the material of the pipeline structure 10 can be conventional stainless steel pipe, without the need to use special heat-resistant materials, thereby reducing the manufacturing cost of the gas cooling device 100, ensuring the sealing characteristics of the gas cooling device 100, and preventing leakage.

[0053] Optionally, in actual operation, both the liquid channel 12 and the airflow channel 11 can be multi-layered. For example, in some embodiments, the pipeline structure 10 has a three-layer structure, with the middle layer being the airflow channel 11 and the inner and outer layers being liquid channels 12. The outermost and innermost liquid channels 12 can spray liquid into the airflow channel 11. The jetting part 14 is located at the position of the outermost liquid channel 12 of the pipeline structure 10 and is isolated from the liquid channel 12 to spray external gas into the airflow channel 11. Of course, in other embodiments of this application, the number of layers of liquid channels 12 and airflow channels 11 can be selected according to actual needs.

[0054] Optionally, the jet section 14 is a jet orifice. This allows for a relatively high pressure of the gas ejected from the jet section 14, which is beneficial for liquid atomization. In this embodiment, the cross-sectional shape of the jet orifice can be selected according to actual needs, and no limitation is made on the cross-sectional shape of the jet orifice here.

[0055] Optionally, the spray section 13 is a spray hole. This allows for a relatively high flow velocity of the liquid sprayed from the spray section 13, which is beneficial for liquid atomization. In this embodiment, the cross-sectional shape of the spray hole can be selected according to actual needs, and no limitation is made on the cross-sectional shape of the spray hole here.

[0056] In some embodiments, as shown in FIG1, the airflow channel 11 includes a high-temperature zone 111, an atomization zone 112, and a vaporization zone 113 arranged sequentially along the airflow direction. A portion of the liquid channel 12 is located outside the high-temperature zone 111, and both the jetting part 14 and the liquid spraying part 13 are connected to the atomization zone 112.

[0057] It is understandable that when the high-temperature gas flows through the high-temperature zone 111, it can be cooled by the coolant in the liquid channel 12. When the high-temperature gas moves to the atomization zone 112, it can come into contact with the liquid droplets atomized by the high-pressure gas. In the vaporization zone 113, it can come into full contact with the atomized liquid, so that the atomized liquid droplets can be rapidly vaporized to cool the high-temperature gas.

[0058] In some specific embodiments, as shown in Figures 1 and 2, the liquid channel 12 includes a cooling channel 121 and a liquid storage chamber 122. The cooling channel 121 has a liquid inlet 1211, which is connected to an external liquid source (not shown in the figure). The cooling channel 121 is located outside the high-temperature zone 111. The liquid storage chamber 122 has a connecting port 1221 and a spray section 13. The connecting port 1221 is connected to the cooling channel 121, and the flow area of ​​the connecting port 1221 is smaller than the flow area of ​​the cooling channel 121 and the liquid storage chamber 122.

[0059] It is understandable that when high-temperature gas flows through the high-temperature zone 111, it can be cooled by the coolant in the cooling channel 121. This allows for heat exchange to cool the high-temperature gas, which helps to increase the cooling rate. The coolant enters the storage chamber 122 from the cooling channel 121 and is then sprayed. Since the flow area of ​​the connecting port 1221 is smaller than that of the cooling channel 121 and the storage chamber 122, the coolant can have a larger pressure after entering the storage chamber 122. This results in the liquid being sprayed into the airflow channel 11 through the spray nozzle 13 having a higher pressure, thus facilitating atomization.

[0060] In some specific embodiments, the cooling channel 121 is located upstream of the pipeline structure 10. Therefore, the high-temperature gas can be cooled first by the coolant in the liquid channel 12 within the pipeline structure 10, and then further cooled by the atomized liquid, which can significantly improve the cooling effect on the high-temperature gas.

[0061] In some specific embodiments, as shown in Figures 1 and 3, the gas cooling device 100 further includes a guide pipe 30 located within the cooling channel 121. The guide pipe 30 is used to ensure that the liquid in the cooling channel 121 is approximately filled before flowing into the liquid storage chamber 122. This helps to ensure that the cooling channel 121 is always filled with liquid, so that when the high-temperature gas flows into the inlet pipe structure 10, it can be cooled by the coolant in the liquid channel 12 first.

[0062] It should be noted that by placing the guide pipe 30 inside the cooling channel 121, not only can the guide pipe 30 be protected and the risk of damage to the guide pipe 30 due to impact be reduced, but the structure of the gas cooling device 100 can also be made more compact, reducing the overall space occupied by the gas cooling device 100 and making it easier to use.

[0063] Of course, in other embodiments, the guide tube 30 may also be disposed on the outer wall of the pipeline structure 10. This application does not limit this, and those skilled in the art can choose according to the actual situation.

[0064] In some specific embodiments, the inlet 33 of the guide pipe 30 is connected to the cooling channel 121, and the inlet 33 of the guide pipe 30 is located at the end of the high temperature zone 111 away from the atomization zone 112. The outlet of the guide pipe 30 is connected to the liquid storage chamber 122, so that the liquid in the cooling channel 121 flows into the liquid storage chamber 122 along the guide pipe 30.

[0065] In some specific embodiments, the guide pipe 30 includes a first pipe section 31 and a second pipe section 32. The first pipe section 31 is connected to the liquid channel 12, and the second pipe section 32 is connected to the liquid storage chamber 122. The connection point of the first pipe section 31 and the second pipe section 32 is higher than the air inlet end 114 of the airflow channel 11. It can be understood that the inclusion of the first pipe section 31 and the second pipe section 32 in the guide pipe 30 facilitates the connection between the guide pipe 30 and the liquid channel 12 and the liquid storage chamber 122. The fact that the connection point of the first pipe section 31 and the second pipe section 32 is higher than the air inlet end 114 of the airflow channel 11 can, to a certain extent, increase the liquid pressure flowing into the liquid storage chamber 122 from the second pipe section 32, increase the total amount of liquid, thereby increasing the contact between the high-temperature gas and the liquid and accelerating the cooling efficiency.

[0066] It is worth noting that the highest point of the guide pipe 30 (the position where the first pipe section 31 and the second pipe section 32 are connected) is higher than the air inlet end 114 of the airflow channel 11. When the liquid passes through the pipeline structure 10, since the highest point of the guide pipe 30 is higher than the highest point of the multi-layer pipe structure, the liquid is ensured to fill the multi-layer pipe structure and can be stably sprayed into the airflow channel 11, thereby ensuring the cooling effect.

[0067] In some specific embodiments, a portion of the cooling channel 121 can serve as part of the guide pipe 30. For example, a portion of the cooling channel 121 can serve as the first segment 31 of the guide pipe 30. This reduces the amount of guide pipe 30 used and lowers manufacturing costs.

[0068] In some specific embodiments, the guide pipe 30 is a bent pipe. The inlet 33 of the bent pipe is connected to the liquid channel 12, and the outlet of the bent pipe is connected to the liquid storage chamber 122. The bend of the bent pipe is higher than the air inlet 114 of the airflow channel 11. It can be understood that since the highest point (bend) of the guide pipe 30 is higher than the air inlet 114 of the airflow channel 11, when the liquid passes through the pipeline structure 10, because the highest point of the guide pipe 30 is higher than the air inlet 114 of the airflow channel 11, the liquid fills the liquid channel 12 and can flow stably into the liquid storage chamber 122, thereby ensuring the cooling effect. At the same time, the guide pipe 30 is manufactured by bending a straight pipe, which facilitates the manufacturing of the guide pipe 30.

[0069] In some more specific embodiments, as shown in FIG1, the cooling channel 121 has a bend (not shown) and includes a first segment 1212 and a second segment 1213 arranged at an angle. The first segment 1212 is located upstream of the second segment 1213. The first segment 1212 intersects the extension direction of the airflow channel 11, and the second segment 1213 is arranged parallel to the extension direction of the airflow channel 11.

[0070] Understandably, in actual operation, after the high-temperature gas enters the airflow channel 11, since the first section 1212 intersects with the extension direction of the airflow channel 11, the high-temperature gas can enter the second section 1213 under the guidance of the first section 1212. This is conducive to the contact between the high-temperature gas in the airflow channel 11 and the coolant in the cooling channel 121, thereby facilitating the cooling of the high-temperature gas.

[0071] In some more specific embodiments, the liquid inlet 1211 of the cooling channel 121 is located downstream of the second section 1213. It can be understood that the location of the liquid inlet 1211 ensures that when the liquid spraying part 13 sprays liquid toward the airflow channel 11, the liquid has a large pressure, thereby facilitating liquid atomization and thus facilitating the cooling of high-temperature gas.

[0072] In some embodiments, the inlet 33 of the guide pipe 30 is located on the first segment 1212. It is understood that the inlet 33 of the guide pipe 30 is a liquid replenishment port. By placing the inlet 33 of the guide pipe 30 on the first segment 1212, on the one hand, it can be ensured that the coolant almost fills the cooling channel 121 before flowing into the storage chamber 122. Thus, the high-temperature gas can be cooled by the coolant in the liquid channel 121, and combined with cooling by atomized coolant, the cooling effect on the high-temperature gas can be significantly improved. On the other hand, it ensures that there is sufficient coolant in the cooling channel 121, which is beneficial for cooling the high-temperature gas.

[0073] In some specific embodiments, as shown in FIG2, the spray section 13 is disposed on the side wall of the liquid storage chamber 122 facing the airflow channel 11. This allows the liquid sprayed from the spray section 13 to be as close as possible to the high-temperature gas within the airflow channel 11, thereby facilitating the cooling of the high-temperature gas.

[0074] In some specific embodiments, the piping structure 10 has a first pipe body (not shown) and a second pipe body (not shown). The first pipe body forms the high-temperature zone 111 and the atomization zone 112 of the liquid channel 12 and the airflow channel 11. The second pipe body forms the vaporization zone 113 of the airflow channel 11. The first pipe body and the second pipe body are connected by a flange.

[0075] It is understandable that the liquid channel 12 is on the outside, while the high-temperature zone 111 and atomization zone 112 of the airflow channel 11 are on the inside. This means that the pipeline structure 10 needs to be a multi-layer structure at the position of the first pipe body, while it can be set as a single-layer pipe at the position of the second pipe body. Disassembling the pipeline structure 10 into a first pipe body and a second pipe body facilitates the manufacturing of the pipeline structure 10 and makes it easier to assemble the pipeline structure 10.

[0076] In some specific embodiments, as shown in Figures 1 and 2, the atomization zone 112 includes a tapered section 1121 and a straight section 1122, which is more conducive to the atomization of the sprayed liquid under the action of the sprayed gas.

[0077] In some specific embodiments, the flow area at the smaller end of the tapered section 1121 of the atomization zone 112 is larger than the flow area of ​​the high-temperature zone 111. As a result, when the high-temperature gas flows from the high-temperature zone 111 to the atomization zone 112, it forms a jet-like airflow. This airflow has more sufficient contact with the atomized liquid, which is beneficial for cooling the high-temperature gas.

[0078] It should be noted that the gas flow area gradually increases from the high-temperature zone 111 to the atomization zone 112 and then to the vaporization zone 113. On the one hand, this provides more space for the high-temperature gas to dissipate heat. On the other hand, the high-temperature gas is jet-shaped, which is conducive to more sufficient contact with the atomized liquid, thus making it more conducive to the cooling of the high-temperature gas.

[0079] In some specific embodiments, the atomization zone 112 is entirely a straight section 1122 to ensure that the high-temperature gas flows at a uniform speed, reduce the risk of turbulence in the high-temperature gas within the atomization zone 112, and reduce the cooling effect.

[0080] In some more specific embodiments, as shown in Figures 1 to 4, the gas cooling device 100 further includes a liquid inlet pipe 20, which is connected to the piping structure 10 and communicates with the liquid inlet 1211. Thus, liquid from an external cold source can enter the liquid channel 12 through the liquid inlet pipe 20 from the liquid inlet 1211. The liquid inlet 1211 is located downstream of the second section 1213, ensuring that the liquid channel 12 always has sufficient liquid throughout the entire process, which is beneficial for continuously spraying liquid towards the airflow channel 11.

[0081] In some other, more specific embodiments, the inlet pipe 20 and the inlet port 1211 connected to the inlet pipe 20 can be located upstream of the pipeline structure 10, and the spray section 13 is located downstream of the pipeline structure 10. It is understood that because the inlet pipe 20 is located upstream of the pipeline structure 10, the liquid channel 12 always has sufficient liquid throughout the entire process. The high-temperature gas can be cooled first by the coolant in the liquid channel 12 within the pipeline structure 10, and then further cooled by the atomized liquid, thus significantly improving the cooling effect on the high-temperature gas.

[0082] In some embodiments, as shown in FIG1, the pipeline structure 10 includes a bent structure (not shown) located at the connection between the first segment 1212 and the second segment 1213. The air inlet direction and the air outlet direction of the pipeline structure 10 are set at an angle. Compared to a straight pipe, the pipeline structure 10 in this embodiment has a bent structure, which reduces the total length in a certain direction while ensuring a longer airflow path, thereby facilitating the use of the pipeline structure 10.

[0083] The embodiments of this application do not limit the specific shape of the bending structure of the pipeline structure 10. In one possible case, the bending point of the pipeline structure 10 can be formed at the connection between the first segment 1212 and the second segment 1213 in the manner shown in FIG1. ​​In another possible case, the bending point of the pipeline structure 10 can be formed at the connection between the first segment 1212 and the second segment 1213 in a smooth transition manner.

[0084] In some specific embodiments, as shown in Figures 2 and 3, the liquid spraying part 13 extends along the airflow direction within the airflow channel 11, and the jet spraying part 14 is inclined, with the extension direction of the liquid spraying part 13 intersecting the extension direction of the jet spraying part 14. It is understood that the inclined arrangement of the jet spraying part 14 causes the airflow injected into the airflow channel 11 to generate angular inertia, forming a vortex. This vortex can increase the contact area between the high-pressure gas and the liquid, improving the atomization efficiency of the liquid and thus enhancing the cooling efficiency of the high-temperature gas.

[0085] In some specific embodiments, as shown in FIG2, the flow area of ​​the gas storage cavity 15 gradually decreases along the gas flow direction within the airflow channel 11, and the jet 14 is disposed on the inclined sidewall of the gas storage cavity 15 facing the airflow channel 11. It can be understood that the inner wall of the gas storage cavity 15 is formed as an inclined sidewall (for example, the cross-section of the gas storage cavity 15 is triangular, and the inclined sidewall is the hypotenuse of the triangle), which can increase the angular inertia generated by the airflow injected into the airflow channel 11 to a certain extent, making the vortex cyclone more intense, further increasing the contact area between the high-pressure gas and the liquid, further improving the atomization efficiency of the liquid, thereby helping to improve the cooling efficiency of the high-temperature gas.

[0086] In other embodiments, the gas storage cavity 15 may also take other shapes, such as a rectangular cross-section. It is only necessary to ensure that the jet 14 is positioned toward the airflow channel 11 and that the extension direction of the jet 14 intersects with the extension direction of the liquid spray 13. This application does not limit this.

[0087] In some specific embodiments, as shown in Figures 1, 3, and 4, the gas cooling device 100 further includes an air inlet pipe 40, one end of which is connected to the gas storage chamber 15, and the other end is connected to an external high-pressure gas source. This allows for convenient gas supply to the pipeline structure 10.

[0088] In some specific embodiments, there are multiple liquid spray sections 13, and the multiple liquid spray sections 13 are distributed circumferentially along the airflow channel 11. It can be understood that the multiple liquid spray sections 13 distributed circumferentially along the airflow channel 11 can make the liquid be sprayed into the airflow channel 11 evenly, which is beneficial to increasing the contact area between the high-temperature gas and the liquid, thereby improving the cooling rate.

[0089] In some specific embodiments, there are multiple liquid spray sections 13, and these multiple liquid spray sections 13 are distributed at intervals along the axial direction of the airflow channel 11. This allows the liquid to be uniformly sprayed into the airflow channel 11, which helps to increase the contact area between the high-temperature gas and the liquid, thereby improving the cooling rate.

[0090] It should be noted that, in actual design, the spray section 13 can be arranged in multiple rings along the airflow channel 11, with each ring having multiple spray sections 13 spaced out circumferentially along the airflow channel 11. The distribution of the spray sections 13 can be selected according to actual needs.

[0091] [Referencing (Details 20.6) 16.12.2025] In some specific embodiments, the size of the spray section 13 is less than 1 mm. Therefore, the liquid sprayed from the spray section 13 has a high pressure, which is beneficial for atomization of the liquid under the action of high-pressure gas. It should be noted that the shape and size of the spray section 13 can be selected according to actual needs and are not limited to the above limitations.

[0092] In some specific embodiments, the spray section 13 is formed as an elongated orifice. This can further increase the pressure of the liquid sprayed from the spray section 13, which is beneficial for the atomization of the liquid under the action of high-pressure gas.

[0093] In some specific embodiments, as shown in FIG4, there are multiple jet sections 14, and the multiple jet sections 14 are distributed circumferentially along the airflow channel 11. It can be understood that the multiple jet sections 14 distributed circumferentially along the airflow channel 11 can make the high-pressure gas be uniformly injected into the airflow channel 11, which is beneficial to increasing the contact area between the high-pressure gas and the liquid, facilitating the atomization of the liquid injected into the airflow channel 11, thereby improving the cooling rate.

[0094] In some specific embodiments, there are multiple jet nozzles 14, and the multiple jet nozzles 14 are distributed at intervals along the axial direction of the airflow channel 11. This allows the high-pressure gas to be uniformly injected into the airflow channel 11, which helps to increase the contact area between the high-pressure gas and the liquid, facilitates the atomization of the liquid injected into the airflow channel 11, and thus helps to improve the cooling rate.

[0095] It should be noted that, in actual design, the jet section 14 can be arranged in multiple rings along the airflow channel 11, with each ring having multiple jet sections 14 spaced circumferentially along the airflow channel 11. The distribution of the jet sections 14 can be selected according to actual needs.

[0096] [Referencing Article 20.6 of 2025] In some specific embodiments, the orifice diameter of the jet nozzle 14 is less than 1 mm. Therefore, the liquid ejected from the jet nozzle 14 has a higher pressure, which is beneficial for atomization of the liquid under the action of high-pressure gas. It should be noted that the shape and size of the jet nozzle 14 can be selected according to actual needs and are not limited to the above limitations.

[0097] It should be noted that, in the embodiments of this application, the distribution of the jet section 14 and the liquid spray section 13 can be arbitrarily combined according to actual needs. For example, in some embodiments, the jet section 14 has multiple rings and the liquid spray section 13 also has multiple rings; for another example, in some embodiments, both the jet section 14 and the liquid spray section 13 have one ring.

[0098] An embodiment of this application also provides a gas cooling device 100, as shown in Figures 5 to 8. The gas cooling device 100 includes a pipeline structure 10, which defines an airflow channel 11 and a liquid channel 12. The airflow channel 11 is used to circulate high-temperature gas, and the liquid channel 12 is located outside the airflow channel 11 and has a spray section 13 communicating with the airflow channel 11. The spray section 13 is used to spray liquid toward the airflow channel 11.

[0099] Specifically, the airflow channel 11 has an inlet end 114 and an outlet end 115. The inlet end 114 is used to introduce high-temperature gas, and the liquid channel 12 has a liquid inlet 1211. The liquid channel 12 also includes a connecting pipe 50. The outlet of the connecting pipe 50 is located at the outlet end 115. The inlet 33 of the connecting pipe 50 is connected to the liquid channel 12, and the outlet of the connecting pipe 50 is connected to the airflow channel 11 to spray liquid towards the airflow channel 11. A spraying part 13 is located at the outlet of the connecting pipe 50, and liquid is sprayed towards the airflow channel 11 through the spraying part 13 at the outlet of the connecting pipe 50.

[0100] It is understood that in the gas cooling device 100 of this embodiment, when the liquid is sprayed from the outlet of the connecting pipe 50 to the airflow channel 11, most of the liquid will rapidly vaporize after encountering the high-temperature gas. During the vaporization process, a large amount of heat will be absorbed. Thus, the heat carried by the high-temperature gas will be largely consumed during the liquid vaporization process, and the high-temperature gas will be cooled quickly. Compared with the water-cooled heat exchange cooling method of the prior art, this embodiment utilizes the principle that the liquid needs to absorb a large amount of heat when it changes from liquid phase to gas phase, so that the high-temperature gas can be cooled quickly, improving the cooling effect and cooling efficiency.

[0101] In addition, the presence of the liquid channel 12 ensures that the temperature of the outer tube of the pipeline structure 10 is relatively safe, and the temperature of the outer wall cannot exceed the boiling point of water. On the other hand, it reduces the temperature of the inner tube of the pipeline structure 10, so that the material of the pipeline structure 10 can be conventional stainless steel pipe, without the need to use special heat-resistant materials, thereby reducing the manufacturing cost of the pipeline structure 10, ensuring the sealing characteristics of the pipeline structure 10, and preventing leakage.

[0102] It should be further noted that in this application, there may be only one or multiple connecting pipes 50. When there are multiple connecting pipes 50, they can be distributed axially or circumferentially along the pipe structure 10. Alternatively, they can be arranged in multiple turns along the axial direction of the pipe structure 10, with each turn including connecting pipes 50 distributed circumferentially along the pipe structure 10. Therefore, in actual use, the arrangement of the connecting pipes 50 can be selected according to actual needs, as long as a good cooling effect is ensured.

[0103] In some specific embodiments, the airflow channel 11 is inclined, and the air inlet 114 is higher than the air outlet 115. It can be understood that the inclined arrangement of the airflow channel 11 allows the liquid channel 12 located outside the airflow channel 11 to also be inclined, and the fact that the air inlet 114 is higher than the air outlet 115 can prevent backflow of liquid in the liquid channel 12.

[0104] In some specific embodiments, as shown in Figures 5 to 8, the connecting pipe 50 includes a first pipe body 51 and a second pipe body 52. ​​The first pipe body 51 is connected to the liquid channel 12, and the second pipe body 52 is connected to the airflow channel 11. The position where the first pipe body 51 and the second pipe body 52 are connected is higher than the air inlet end 114 of the airflow channel 11.

[0105] It is understandable that the connecting pipe 50 includes a first pipe body 51 and a second pipe body 52, which facilitates connecting the connecting pipe 50 to the liquid storage chamber 122 and the gas channel. The connection position of the first pipe body 51 and the second pipe body 52 is higher than the air inlet end 114 of the airflow channel 11, which can increase the liquid pressure ejected from the second pipe body 52 to a certain extent, increase the total amount of liquid, thereby increasing the contact between the high temperature gas and the liquid and accelerating the cooling efficiency.

[0106] In some embodiments, the connecting pipe 50 further includes a third pipe body 53, the two ends of which are connected to the first pipe body 51 and the second pipe body 52, respectively. The third pipe body 53 is higher than the air inlet end 114 of the airflow channel 11. It can be understood that the highest point of the connecting pipe 50 (the position of the third pipe body 53) is higher than the highest point of the pipe structure 10 (the air inlet end 114). When the liquid passes through the pipe structure 10, since the highest point of the U-shaped pipe is higher than the highest point of the pipe structure 10, the liquid is ensured to fill the pipe structure 10 and can be stably sprayed into the airflow channel 11, thereby ensuring the cooling effect.

[0107] In some specific embodiments, as shown in Figure 5, the third tube 53 is horizontally positioned, and the first tube 51 and the second tube 52 are both perpendicular to the third tube 53. This ensures that the liquid fills the multi-layer tube structure and can be stably injected into the airflow channel 11, thereby ensuring a cooling effect. Of course, in other embodiments of this application, the included angle between the first tube 51, the third tube 53, and the second tube 52 can be selected according to actual needs and is not limited to the limitations of this embodiment.

[0108] In some specific embodiments, the connecting pipe 50 is a bent pipe. The inlet 33 of the bent pipe is connected to the liquid channel 12, and the outlet of the bent pipe is connected to the airflow channel 11. The bend of the bent pipe is higher than the air inlet 114 of the airflow channel 11. It can be understood that the highest point of the connecting pipe 50 (the bend) is higher than the highest point of the pipe structure 10 (the air inlet 114). When the liquid passes through the pipe structure 10, because the highest point of the connecting pipe 50 is higher than the highest point of the pipe structure 10, the liquid is ensured to fill the pipe structure 10 and can be stably sprayed into the airflow channel 11, thereby ensuring the cooling effect. At the same time, the connecting pipe 50 is manufactured by bending a straight pipe, which simplifies the manufacturing process.

[0109] In other embodiments, the connecting pipe 50 is a straight pipe, with its inlet 33 connected to the liquid channel 12 and its outlet connected to the airflow channel 11. That is to say, in the embodiments of this application, the connecting pipe 50 is not limited to the U-shaped pipe structure described above.

[0110] In some embodiments, the gas channel 11 includes a high-temperature zone (not shown), located at one end of the gas channel 11 near the direction of high-temperature gas inflow. The liquid channel 12 may further include a cooling channel (not shown) and a liquid storage chamber (not shown). An inlet 1211 is disposed in the cooling channel and connected to an external liquid source, and the cooling channel is located outside the high-temperature zone. The liquid storage chamber has a connecting port and a spray section 13. The connecting port communicates with the cooling channel, and the flow area of ​​the connecting port is smaller than the flow area of ​​the cooling channel and the liquid storage chamber. Exemplarily, the connecting port of the liquid storage chamber is connected to a connecting pipe 50 to obtain coolant from the cooling channel through the connecting pipe 50.

[0111] It is understandable that when high-temperature gas flows through the high-temperature zone, it can be cooled by the coolant in the cooling channel. This allows for heat exchange to cool the high-temperature gas, which helps to increase the cooling rate. The coolant enters the storage chamber from the cooling channel and is then sprayed. Since the flow area of ​​the connecting port is smaller than the flow area of ​​the cooling channel and the storage chamber, the coolant can have a larger pressure after entering the storage chamber, resulting in higher pressure of the liquid sprayed through the spray nozzle 13 onto the airflow channel 11.

[0112] In some specific embodiments, there are multiple liquid spray sections 13, and the multiple liquid spray sections 13 are distributed circumferentially along the airflow channel 11. It can be understood that the multiple liquid spray sections 13 distributed circumferentially along the airflow channel 11 can make the liquid be sprayed into the airflow channel 11 evenly, which is beneficial to increasing the contact area between the high-temperature gas and the liquid, thereby improving the cooling rate.

[0113] In some specific embodiments, as shown in Figures 1 and 5, the gas cooling device 100 further includes a fan 60, which is connected to the outlet 115 of the airflow channel 11. The fan 60 is used to drive the forced flow of gas within the airflow channel 11. It is understood that the fan 60 can drive the gas flow within the airflow channel 11, thereby increasing the airflow velocity within the airflow channel 11 and improving cooling efficiency.

[0114] In some specific embodiments, as shown in Figures 1 and 5, the gas cooling device 100 further includes an extraction pipe 70. One end of the extraction pipe 70 is connected to the outlet 115 of the airflow channel 11, and the other end is used to install a fan 60. The end of the extraction pipe 70 where the fan 60 is installed is lower than the end connected to the outlet 115 of the airflow channel 11. It is understood that the connection between the fan 60 and the outlet 115 of the airflow channel 11 via the extraction pipe 70 ensures that the airflow reaches the fan 60 at a relatively low temperature, thereby preventing corrosion of the fan 60 due to relatively high airflow temperature and extending the service life of the fan 60.

[0115] In some more specific embodiments, as shown in Figures 1 and 5, the gas cooling device 100 further includes an exhaust pipe connected to the side of the fan 60 away from the exhaust pipe 70. It is understood that the added exhaust pipe can exhaust gas towards a designated location, and when harmful gases are present in the high-temperature gas, it can discharge the harmful gases into a designated space, improving operational safety.

[0116] An embodiment of this application also provides a furnace 1, as shown in FIG9. The furnace 1 includes a furnace body 200 and the aforementioned gas cooling device 100. The furnace body 200 has an exhaust pipe 80, and the gas cooling device 100 is used to cool the gas released from the furnace body 200 through the exhaust pipe 80. It can be understood that in actual use, the pipeline structure 10 is connected to the exhaust pipe 80 of the furnace 1. After the high-temperature gas enters the airflow channel 11, the liquid channel 12 is provided outside the airflow channel 11, and the liquid channel 12 can cool the high-temperature gas. The liquid in the liquid channel 12 can also be sprayed from the spraying part 13 to the airflow channel 11. The sprayed liquid will be rapidly atomized when it encounters the high-pressure gas sprayed from the jet part 14. The atomized liquid will mix with the high-temperature gas. When the atomized liquid encounters the high-temperature gas, it will rapidly vaporize and become steam. When the liquid vaporizes, it absorbs a large amount of heat, thereby ensuring that the temperature of the high-temperature gas drops rapidly. When the high-temperature gas is discharged from the pipeline structure 10, it will have a lower temperature.

[0117] Compared to the existing technology of wrapping cold water pipes around exhaust pipes, the pipe structure 10 of this application is connected to the outlet of the exhaust pipe (e.g., exhaust pipe 80), which is convenient to use and not easily damaged by the exhaust pipe, and has a longer service life. During operation, liquid cooling and liquid vaporization can remove a large amount of heat, achieving rapid cooling of high-temperature gas and improving cooling rate and efficiency. Since the jet 14 can spray high-pressure gas toward the airflow channel 11, the liquid sprayed toward the airflow channel 11 is atomized, which can make full use of the sprayed liquid to cool the high-temperature gas and reduce the amount of sprayed liquid used.

[0118] It should be noted that, since a liquid channel 12 is provided outside the airflow channel 11, the existence of the liquid channel 12 can ensure that the temperature of the outer tube of the pipeline structure 10 is relatively safe, and the temperature of the outer wall cannot exceed the boiling point of water. On the other hand, it reduces the temperature of the inner tube of the pipeline structure 10, so that the material of the pipeline structure 10 can be conventional stainless steel pipe, without the need to use special heat-resistant materials, thereby reducing the manufacturing cost of the gas cooling device 100, ensuring the sealing characteristics of the gas cooling device 100, and preventing leakage.

[0119] The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention. Any modifications, equivalent substitutions, and improvements made within the spirit and principles of the present invention should be included within the protection scope of the present invention.

Claims

1. A gas cooling device, characterized by, The pipeline structure defines a gas flow channel for flowing high-temperature gas and a liquid channel outside the gas flow channel, and has a liquid injection part communicating with the gas flow channel and a gas injection part communicating with the gas flow channel, wherein the liquid injected from the liquid injection part can be vaporized under the action of the high-temperature gas in the gas flow channel and the high-pressure gas injected from the gas injection part.

2. A gas cooling device, characterized by The pipeline structure defines a gas flow channel for flowing high-temperature gas and a liquid channel outside the gas flow channel, and has a liquid injection part communicating with the gas flow channel and a gas injection part communicating with the gas flow channel, wherein the liquid injected from the liquid injection part can be vaporized under the action of the high-temperature gas in the gas flow channel and the high-pressure gas injected from the gas injection part.

3. The gas cooling device according to claim 1 or 2, characterized in that The gas channel comprises a high-temperature zone at one end of the gas channel close to the inflow direction of the high-temperature gas. The liquid channel comprises: A cooling channel having a liquid inlet connected to an external liquid source and located outside the high-temperature zone; A liquid storage cavity having a communication port communicating with the cooling channel and the liquid injection part, wherein the flow area of the communication port is smaller than the flow areas of the cooling channel and the liquid storage cavity.

4. The gas cooling device according to claim 3, characterized in that The gas cooling device further comprises a liquid inlet pipe connected to the pipeline structure and communicating with the liquid inlet at one end and connected to an external liquid source at the other end.

5. The gas cooling device according to claim 3, characterized in that The gas cooling device further comprises a flow guide pipe located in the cooling channel, which is used to make the liquid in the cooling channel substantially fill the cooling channel and then flow into the liquid storage cavity.

6. The gas cooling device of claim 5, wherein The inlet of the flow guide pipe communicates with the cooling channel, and the inlet of the flow guide pipe is located at the gas inlet end of the gas flow channel, and the outlet of the flow guide pipe communicates with the liquid storage cavity, so that the liquid in the cooling channel flows into the liquid storage cavity along the flow guide pipe.

7. The gas cooling device according to claim 5, characterized in that The flow guide pipe comprises a first pipe section communicating with the liquid channel and a second pipe section communicating with the liquid storage cavity, and the connection position of the first pipe section and the second pipe section is higher than the gas inlet end of the gas flow channel.

8. The gas cooling device of claim 5, wherein The flow guide pipe is a bent pipe, the inlet of the bent pipe communicates with the liquid channel, the outlet of the bent pipe communicates with the liquid storage cavity, and the bending position of the bent pipe is higher than the gas inlet end of the gas flow channel.

9. The gas cooling device according to claim 1 or 2, characterized in that, The liquid injection part is multiple, and multiple liquid injection parts are distributed along the circumference of the gas flow channel.

10. The gas cooling device of claim 1, wherein The gas injection part is inclined, and the extension direction of the liquid injection part intersects with the extension direction of the gas injection part.

11. The gas cooling device of claim 10, wherein The pipeline structure further defines a gas storage cavity capable of being connected to an external gas source, and the gas injection part communicates with the gas storage cavity.

12. The gas cooling device of claim 11, wherein, In the gas flow direction along the gas flow channel, the flow area of the gas storage cavity gradually decreases, and the gas injection part is arranged on the inclined side wall of the gas storage cavity facing the gas flow channel.

13. The gas cooling device of claim 11, wherein, The gas cooling device further comprises an air inlet pipe connected to the gas storage cavity at one end and connected to an external high-pressure gas source at the other end.

14. The gas cooling device of claim 1, wherein, The plurality of air injection parts are arranged along the circumference of the airflow channel.

15. The gas cooling device of claim 1, wherein, The airflow channel comprises a high-temperature zone, an atomization zone and a vaporization zone arranged in sequence along the airflow direction, and a part of the liquid channel is located outside the high-temperature zone, and the air injection part and the liquid injection part are both in communication with the atomization zone.

16. The gas cooling device of claim 2, wherein The airflow channel has an air inlet end for introducing high-temperature gas, and the liquid channel has a liquid inlet; The liquid channel further comprises a connecting pipe, the outlet of the connecting pipe is arranged at the air outlet end, the inlet of the connecting pipe is in communication with the liquid channel, and the outlet of the connecting pipe is in communication with the airflow channel to spray liquid towards the airflow channel; The liquid injection part is arranged at the outlet of the connecting pipe, and the outlet of the connecting pipe sprays liquid towards the airflow channel through the liquid injection part.

17. The gas cooling device of claim 16, wherein, The airflow channel is arranged obliquely, and the air inlet end is higher than the air outlet end.

18. The gas cooling device of claim 16, wherein, The connecting pipe comprises a first pipe body and a second pipe body, the first pipe body is in communication with the liquid channel, the second pipe body is in communication with the airflow channel, and the position where the first pipe body and the second pipe body are connected is higher than the air inlet end of the airflow channel.

19. The gas cooling device of claim 18, wherein, The connecting pipe further comprises a third pipe body, both ends of the third pipe body are connected with the first pipe body and the second pipe body respectively, and the third pipe body is higher than the air inlet end of the airflow channel.

20. The gas cooling device of claim 16, wherein, The connecting pipe is a bent pipe, the inlet of the bent pipe is in communication with the liquid channel, the outlet of the bent pipe is in communication with the airflow channel, and the bending part of the bent pipe is higher than the air inlet end of the airflow channel.

21. The gas cooling device according to any one of claims 1 or 2, characterized in that, The gas cooling device further comprises a fan arranged in the pipeline structure to drive the forced flow of gas in the airflow channel.

22. The gas cooling device of claim 21, wherein, The gas cooling device further comprises an air extraction pipe, one end of the air extraction pipe is connected with the air outlet end of the airflow channel, and the other end is used for mounting the fan, and the end of the air extraction pipe mounting the fan is lower than the end connected with the air outlet end.

23. The gas cooling device of claim 22, wherein, The gas cooling device further comprises an air exhaust pipe connected to the side of the fan away from the air extraction pipe.

24. A hot stove characterized by Comprise: a furnace body, the furnace body has an air exhaust pipe; The gas cooling device according to any one of claims 1 to 2, 10 to 20 is used for cooling the gas released by the furnace body through the air exhaust pipe.

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