Efficient cracking and catalytic agent thermal reaction device

Abstract

An efficient cracking and accelerant thermal reaction device comprises a combustion furnace, a plurality of positioning plates, reactants, a fuel barrel and a water tank. A thermal reaction space and a liquid storage space are arranged in the combustion furnace; the plurality of positioning plates are embedded and fixedly arranged in the thermal reaction space in a longitudinal interval arrangement manner, and reactants are supported by the positioning plates; an atomizer arranged on the fuel barrel is arranged at an air inlet of the combustion furnace; a sprinkler head arranged on the water tank is arranged at an air inlet of the combustion furnace; therefore, the plurality of reactants are firstly heated by the heater arranged on the combustion furnace, then fuel sprayed by the atomizer and water mist sprayed by the spraying head form continuous thermal reaction with the plurality of reactants, and heat energy generated by the plurality of reactants forming the thermal reaction is used for continuously heating liquid in the liquid storage space. Therefore, the efficient thermal reaction furnace is achieved.

Description

Technical Field

[0001] The utility model relates to an efficient cracking and catalyst thermal reaction device, in particular to a device that uses fuel sprayed by an atomizer and water sprayed by a sprinkler head to react with multiple reactants to form a continuous thermal reaction, achieving heating directly by the thermal reaction method without using an open flame combustion method, completely avoiding carbonized particles generated by combustion, thereby effectively eliminating air pollution generated by combustion and effectively improving air quality. Background Art

[0002] Traditional large-scale incinerators, heating combustion furnaces and other equipment, as well as various combustion furnaces that obtain heat energy by combustion, all require a large amount of fuel, such as coal, oil or wood, etc., to manufacture and obtain the required heat energy; however, during the combustion process of these devices, various exhaust gases (toxic gases) and a large amount of suspended particles (such as carbonized particles) entrained in the exhaust gases are the main causes of air pollution. When these exhaust gases and suspended particles are discharged into the high-altitude air flow through a tall chimney, it is an inevitable result that the exhaust gases and suspended particles will drift with the wind.

[0003] Secondly, traditional heat generation by combustion has many deficiencies in addition to insufficient heat energy utilization, large fuel consumption and high amounts of suspended particles generated, such as:

[0004] As long as the open flame combustion method is used, there will be problems of incomplete combustion and black smoke emission; moreover, the open flame phenomenon presented by combustion hides many dangers and directly poses a serious threat to life and property.

[0005] Furthermore, when a combustion furnace device generates heat energy by the open flame combustion method, it will cause pressure inside the combustion furnace device due to combustion. Once the pressure is not controlled, there will be an explosion risk: for this reason, news of combustion furnace explosions causing large fires is often heard.

[0006] Therefore, how to develop an efficient cracking and catalyst thermal reaction device that can generate heat energy without using the open flame combustion method is the main problem to be solved by the present utility model. Summary of the Utility Model

[0007] The main object of the present utility model is to provide an efficient cracking and catalyst thermal reaction device, which includes a combustion furnace, a plurality of positioning plates, a plurality of reactants, a fuel tank and a water tank; a thermal reaction space is provided inside the combustion furnace, an air inlet is provided at the bottom position of the thermal reaction space in the combustion furnace, and an air outlet is provided at the top position of the combustion furnace. A heater is provided at the air inlet of the combustion furnace and is connected with an air inlet pipe extending to the outside; furthermore, a closed liquid storage space is provided around the thermal reaction space inside the combustion furnace, and the liquid storage space is connected with at least one liquid input pipe and at least one liquid output pipe; the plurality of positioning plates are fixedly arranged inside the thermal reaction space of the combustion furnace in a vertically spaced arrangement; the plurality of reactants are respectively arranged on each positioning plate, so that the plurality of reactants are arranged in a spaced arrangement form; the fuel tank is located outside the combustion furnace for storing preset fuel, the fuel tank is connected with a fuel delivery pipe, and an atomizer is provided at the end of the fuel delivery pipe and is communicated with the air inlet pipe, so that the fuel inside the fuel tank can be transported through the fuel delivery pipe and the atomizer, and then enter the thermal reaction space through the air inlet; the water tank is located outside the combustion furnace for storing preset water, the water tank is connected with a water delivery pipe, and a sprinkler head is provided at the end of the water delivery pipe and is communicated with the air inlet pipe, so that the water inside the water tank enters the thermal reaction space through the water delivery pipe and the sprinkler head and then through the air inlet.

[0008] The heater heats the reactants, so that the reactants, the fuel and the water mist form a continuous thermal reaction, and the heat energy generated by the plurality of reactants forming the thermal reaction is used to continuously heat the liquid installed inside the liquid storage space.

[0009] Furthermore, the positioning plate is provided with a plurality of spaced-apart placement grooves, and at least one through hole is provided around each placement groove, and the through hole is communicated with the placement groove. The plurality of reactants are respectively arranged in the placement grooves of each positioning plate, so that the plurality of reactants are arranged in a spaced form.

[0010] Furthermore, the positioning plate is provided with a plurality of spaced-apart suspension ropes, and each suspension rope is connected to at least one of the reactants, so that the plurality of reactants are arranged in a spaced form.

[0011] Furthermore, at least one channel is provided between the thermal reaction space and the air outlet.

[0012] Furthermore, the combustion furnace is connected with an air outlet pipe extending to the outside at the air outlet.

[0013] Furthermore, a blower is further provided on the air inlet pipe.

[0014] Furthermore, a pressure pump is provided on the fuel delivery pipe.

[0015] Furthermore, a metering pump is provided on the water delivery pipe.

[0016] Further, the combustion furnace is further provided with a control panel, which is electrically connected to the heater, the air blower, the atomizer, the pressure pump and the metering pump respectively.

[0017] The beneficial effects of the present utility model are as follows: a thermal reaction is carried out in the combustion furnace, and a continuous heat energy is generated through sequential thermal reactions. Among them: multiple positioning plates are arranged inside the thermal reaction space, and the positioning plate surfaces are provided with placing grooves arranged at longitudinal intervals, and multiple reactants are respectively arranged in the placing grooves; during use, the heater provided in the combustion furnace first heats the multiple reactants, and then the fuel sprayed by the atomizer can be distributed on each reactant; at the same time, the water sprayed by the spray head can be mixed with the fuel, so that the multiple reactants, the fuel and the water form a better and continuous thermal reaction, and then the heat energy generated by the multiple reactants in the formed thermal reaction is used to continuously heat the liquid installed inside the liquid storage space, so that the heated liquid can be used for various purposes, achieving heating without the need for an open flame combustion method, completely avoiding the carbonized particles generated by open flame combustion, thereby effectively improving the air quality and exhaust emissions. Description of the Drawings

[0018] Figure 1 : A schematic cross-sectional view of the high-efficiency cracking and catalytic thermal reaction device of the present utility model.

[0019] Figure 2 : Of the present utility model Figure 1 Schematic enlarged view of the circled area A in the figure.

[0020] Figure 3 : Schematic diagram of a combined embodiment of the reactants and the placing grooves of the high-efficiency cracking and catalytic thermal reaction device of the present utility model.

[0021] Figure 4 : Schematic diagram of another embodiment of the reactants and the placing grooves of the high-efficiency cracking and catalytic thermal reaction device of the present utility model.

[0022] Figure 5 : Schematic diagram of an application embodiment of the high-efficiency cracking and catalytic thermal reaction device of the present utility model.

[0023] Description of the Reference Numerals

[0024] 1. Combustion furnace; 11. Thermal reaction space; 111. Air inlet; 112. Air outlet; 113. Channel; 114. Air inlet pipe; 115. Air outlet pipe; 116. Blower; 12. Liquid storage space; 121. Liquid input pipe; 122. Liquid output pipe; 13. Heater; 2. Positioning plate; 21. Placing groove; 22. Through hole; 21. Suspension rope; 3. Reactant; 4. Fuel tank; 41. Pressurizing pump; 5. Control panel; 6. Liquid; 7. Water tank; 71. Water delivery pipe; 72. Spraying head; 73. Dosing pump. Detailed implementation mode

[0025] For the convenience of understanding the characteristic content, advantages and achieved effects of the present utility model more simply and clearly, the present utility model will be described in detail in conjunction with the attached drawings. The following embodiments further illustrate the viewpoints of the present utility model in detail, but do not limit the scope of the present utility model in any way.

[0026] Please first refer to Figures 1 to 3 As shown, the present utility model discloses a high-efficiency cracking and catalytic thermal reaction device, including a combustion furnace 1, a plurality of positioning plates 2, a plurality of reactants 3, a fuel tank 4 and a water tank 7.

[0027] The combustion furnace 1 is internally provided with a thermal reaction space 11. The thermal reaction space 11 is provided with an air inlet 111 at the bottom of the combustion furnace 1 and an air outlet 112 at the top of the combustion furnace 1. At least one channel 113 is provided between the thermal reaction space 11 and the air outlet 112. The channel 113 can be cylindrical or other shapes. A heater 13 is provided at the air inlet 111 of the combustion furnace 1. The heater 13 is connected to and extends to the external air inlet pipe 114. At the air outlet 112 of the combustion furnace 1, an air outlet pipe 115 extending to the outside is connected; furthermore, a closed liquid storage space 12 is provided inside the combustion furnace 1 around the outside of the thermal reaction space 11 and the channel 113. The liquid storage space 12 is connected with at least one liquid input pipe 121 and at least one liquid output pipe 122, so that external water can flow into the liquid storage space 12 through the liquid input pipe 121, and the liquid 6 stored in the liquid storage space 12 (please refer to Figure 5 shown) can be discharged through the liquid output pipe 122. The air inlet pipe 114 may further be provided with a blower 116, and the blower 116 can transport external air into the thermal reaction space 11 through the air inlet pipe 114.

[0028] A plurality of positioning plates 2 are fixedly arranged in the thermal reaction space 11 of the combustion furnace 1 at intervals to arrange a plurality of reactants 3. As Figure 2 , Figure 3As shown, each positioning plate 2 is provided with a plurality of receiving grooves 21 arranged at intervals, such that a plurality of reactants 3 can be respectively arranged in the receiving grooves 21 of each positioning plate 2, so that the plurality of reactants 3 are arranged in a spaced-apart form. Moreover, at least one through-hole 22 is provided around each receiving groove 21, and the through-hole 22 and the receiving groove 21 communicate with each other. The through-hole 22 can be in any shape such as a dovetail shape, a triangular shape, a rectangular shape, etc.

[0029] The plurality of reactants 3 are arranged in a spaced-apart form on each positioning plate 2. The reactant 3 has a metal component, and the diameter of the reactant 3 is larger than the diameter of the receiving groove 21, such that the reactant 3 can be placed in the receiving groove 21 without rolling and touching each other (as Figure 3 shown); alternatively, the reactant 3 can be embedded in the receiving groove 21 and is not likely to roll and touch each other.

[0030] In addition, as Figure 4 shown, each positioning plate 2 is provided with a plurality of suspension ropes 23 arranged at intervals. Each suspension rope 23 can be connected to at least one reactant 3, so that the plurality of reactants 3 also form a spaced-apart form. This can not only prevent the reactants 3 from falling in case of an earthquake or impact, but also has a more efficient heat reaction ability without dead angles.

[0031] The fuel tank 4 is located outside the combustion furnace 1 and is used to store the preset fuel. The fuel tank 1 is connected to a fuel delivery pipe 41. The end of the fuel delivery pipe 41 is provided with an atomizer 42 and is connected to the intake pipe 114 of the combustion furnace 1. Moreover, the fuel delivery pipe 41 is provided with a pressure pump 43. The pressure pump 43 is used to extract the fuel inside the fuel tank 4 through the fuel delivery pipe 41, so that the fuel inside the fuel tank 4 is transported through the fuel delivery pipe 41 to the atomizer 42, and then the atomizer 42 sprays the fuel into the combustion space 11 through the air inlet 111 in the form of a spray (the optimal mixing ratio of air and fuel can be adjusted in this process).

[0032] The water tank 7 is located outside the combustion furnace 1 and is used to store the preset water. The water tank 7 is connected to a water delivery pipe 71. The end of the water delivery pipe 71 is provided with a sprinkler head 72 and is connected to the intake pipe 114 of the combustion furnace 1. Moreover, the water delivery pipe 71 is provided with a metering pump 73. The metering pump 73 is used to extract the water inside the water tank 7 through the water delivery pipe 71, so that the water inside the water tank 7 is transported through the water delivery pipe 71 to the sprinkler head 72 in a quantitative manner, and then the sprinkler head 72 sprays the water into the combustion space 11 through the air inlet 111 in the form of a spray (the optimal mixing ratio of air, fuel and water can be adjusted in this process).

[0033] The combustion furnace 1 is further provided with a control panel 5, which is electrically connected to the heater 13, the air blower 116, the atomizer 42, the pressure pump 43, and the metering pump 73 respectively. The control panel 5 is used to control the combustion intensity, weakness, time, and temperature of the heater 13, and the control panel 5 is used to control the intensity, weakness, start, or shutdown of the air blower 116, the atomizer 42, the pressure pump 43, and the metering pump 73.

[0034] The fuel inside the fuel tank 4 can be fuels such as methanol, ethanol, isopropanol, or methane.

[0035] Please refer to Figure 5 As shown, a description is given by way of an example of the present utility model. When the combustion furnace 1 of the present utility model operates, the heater 13 provided in the combustion furnace 1 can be started first to heat a plurality of reactants 3. When the reactants 3 reach a preset temperature, the heater 13 can be turned off. At this time, the atomizer 42 sprays the fuel in a spray form into the combustion space 11 through the air inlet 111, and at the same time, the sprinkler head 72 sprays water in a spray (atomized) form into the thermal reaction space 11 through the air inlet 111, so that air, fuel, and water are mixed at the air inlet 111 and then conveyed into the interior of the combustion furnace 1 by the air blower 116. Then, by using the positioning plates 2 arranged longitudinally at intervals inside the combustion space 11, each positioning plate 2 is further provided with a plurality of receiving grooves 21 arranged at intervals, and reactants 3 are arranged in each receiving groove 21, so that a plurality of reactants 3 are arranged in an interval arrangement form. Then, at least one through hole 22 is provided around each receiving groove 21, so that the fuel sprayed by the atomizer 42 and the water mist sprayed by the sprinkler head 72 can be evenly distributed and pass through the through holes 22 provided in each receiving groove 21, enabling a plurality of reactants 3 to undergo a thermal reaction with air, fuel, and water. That is, when air, fuel (such as methane), water, and the high-temperature reactants 3 come into contact, hydrogen and carbon monoxide will be formed, namely, a cracking reaction. The hydrogen generated will then oxidize with oxygen to produce a heat release effect. In addition, carbon monoxide will also react with oxygen to produce a heat release effect, achieving multiple chain reactions to generate higher heat energy.

[0036] Furthermore, the heat energy generated by the plurality of reactants 3 that form the thermal reaction is used to continuously heat the liquid 6 installed inside the liquid storage space 12, so that the heated liquid 6 can be used as power or for other heating purposes, achieving heating without the need for an open flame combustion method, completely avoiding the waste gas and carbonized particles generated during combustion, and thereby effectively improving air quality.

[0037] The multiple reactants 3 and the fuel, during their reaction process, only emit carbon dioxide and water, without generating various harmful substances and a large number of carbonized particles produced during an open-flame combustion process; moreover, the hot gas generated during the reaction process of the multiple reactants 3 will sequentially pass through the channel 113, the air outlet 112, and the air outlet pipe 115 and be discharged, and the hot gas without carbonized particles discharged during the reaction process of the multiple reactants 3 can be used as power or for other heating purposes.

[0038] Therefore, the technical feature of the present utility model lies in that, by using the combustion space 11 which is internally provided with a plurality of positioning disks 2 arranged at intervals longitudinally or transversely, each positioning disk 2 is used to arrange a plurality of reactants 3, and then by using the fuel sprayed by the atomizer 42 and the water mist sprayed by the sprinkler head 72 to form a continuous thermal reaction with the multiple reactants 3, heating is achieved without the need for open-flame combustion, completely avoiding the carbonized particles generated by open-flame combustion, thereby effectively improving air quality and exhaust emissions.

[0039] The above description is only a preferred embodiment of the present utility model. Obviously, the described embodiments are only a part of the embodiments of the present utility model, rather than all of them. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the scope of protection of the present utility model.

Claims

1. An efficient cracking and catalytic thermal reaction device, characterized in that, Comprising: A combustion furnace, which has a thermal reaction space inside. An air inlet is provided at the bottom position of the thermal reaction space in the combustion furnace, and an air outlet is provided at the top position of the combustion furnace. A heater is provided at the air inlet of the combustion furnace and is connected to an intake pipe extending to the outside. And inside the combustion furnace, a sealed liquid storage space is provided around the thermal reaction space. The liquid storage space is connected to at least one liquid input pipe and at least one liquid output pipe; A plurality of positioning disks, which are fixedly installed in the thermal reaction space of the combustion furnace in a vertically spaced arrangement; A plurality of reactants, which are respectively arranged on each of the positioning disks; A fuel tank, which is located outside the combustion furnace. The fuel tank is connected to a fuel delivery pipe. The end of the fuel delivery pipe is provided with an atomizer and is connected to the intake pipe in communication; A water tank, which is located outside the combustion furnace. The water tank is connected to a water delivery pipe. The end of the water delivery pipe is provided with a sprinkler head and is connected to the intake pipe in communication.

2. The high-efficiency cracking and catalyst thermal reaction device according to claim 1, wherein The positioning disk is provided with a plurality of spaced-apart placement grooves. At least one through hole is provided around each of the placement grooves. The through hole communicates with the placement groove. A plurality of reactants are respectively arranged in the placement grooves of each of the positioning disks, so that the plurality of reactants are arranged in a spaced form.

3. The high-efficiency cracking and catalyst thermal reaction device according to claim 1, wherein The positioning disk is provided with a plurality of spaced-apart suspension ropes. Each of the suspension ropes is connected to at least one of the reactants, so that the plurality of reactants are arranged in a spaced form.

4. The high-efficiency cracking and catalyst thermal reaction device according to claim 1, wherein At least one channel is provided between the thermal reaction space and the air outlet.

5. The high-efficiency cracking and catalyst thermal reaction device according to claim 1, characterized in that, The combustion furnace is connected to an exhaust pipe extending to the outside at the air outlet.

6. The high-efficiency cracking and catalyst thermal reaction device according to claim 1, characterized in that, A blower is provided on the intake pipe.

7. The high-efficiency cracking and catalyst thermal reaction device according to claim 6, characterized in that, A pressure pump is provided on the fuel delivery pipe.

8. The high-efficiency cracking and catalyst thermal reaction device according to claim 7, characterized in that, A metering pump is provided on the water delivery pipe.

9. The high-efficiency cracking and catalyst thermal reaction device according to claim 8, characterized in that, The combustion furnace is provided with a control panel, and the control panel is electrically connected to the heater, the blower, the atomizer, the pressure pump and the metering pump respectively.

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