CN210663056U

CN210663056U - Catalyst structure of heating reaction furnace

Info

Publication number: CN210663056U
Application number: CN201921333427.8U
Authority: CN
Inventors: 蔡孜才
Original assignee: Individual
Current assignee: Individual
Priority date: 2019-08-16
Filing date: 2019-08-16
Publication date: 2020-06-02
Anticipated expiration: 2029-08-16

Abstract

The utility model provides a catalyst structure of a heating reaction furnace, which comprises a plurality of catalyst objects, wherein the catalyst objects are arranged in a reaction chamber of the reaction furnace; wherein, each catalyst comprises at least three blocks made of different materials, the at least three blocks are mutually combined into a three-dimensional catalyst, and the catalyst is respectively provided with a columnar elastomer in the range of each block; therefore, when a plurality of catalyst objects are respectively stacked and arranged in the reaction chamber, the elastic bodies arranged in each block of the catalyst objects can be mutually abutted for supporting, so that a space for air circulation can be formed between the catalyst objects and another catalyst object, the oxygen content required by the thermal reaction of each catalyst object is increased, and the thermal benefit of the catalyst objects is effectively improved through the thermal reaction.

Description

Catalyst structure of heating reaction furnace

Technical Field

The utility model relates to a heating installation technical field, concretely relates to catalyst structure of heating reaction stove.

Background

Due to the change of the climate of the earth, extreme cold and extreme hot climate phenomena gradually occur in the global temperature, and the original warm-keeping equipment is not suitable for use in many tropical or subtropical regions at low latitudes and regions without snowing and also in snowstorm snowing in recent years; therefore, when cold flows come and the indoor temperature suddenly drops, in order to resist severe cold, warm-keeping products such as the bosom warmer, the electric heater … and the like are pushed out to be new like bamboo shoots in spring after rain.

The heating demand in winter in high latitude countries or northern regions is more dependent on main vitamin resources besides being necessary for life; the traditional large heating equipment still adopts a large amount of coal or oil to produce heat energy until now, sulfide, hydride, carbon monoxide and a large amount of carbonized particles generated in the combustion process are the origin of air pollution, so that fine suspended particles (PM 2.5, the diameter is less than or equal to 2.5 microns) in the atmosphere are continuously increased, and particularly, the quality deterioration degree of the whole atmospheric environment is continuously increased due to the high-concentration fine suspended particles contained in the air blown from the north in winter.

In addition, the combustion mode is utilized to generate heat energy, so that not only can carbonization fine suspended particles be generated, but also the air contains various toxic substances and gases; for the traditional heating equipment, because coal or oil is adopted for combustion, namely, the danger of open fire exists, the danger is directly caused to life and property, and the operation and the use must be very careful and attentive; in addition, the conventional heating apparatus generates heat energy by combustion, and if the pressure is inevitably generated in the heating apparatus due to the combustion, the explosion risk is generated if the pressure is not properly controlled.

Therefore, how to develop a heating device capable of generating heat energy without using the conventional combustion method, and effectively increasing the heat energy efficiency generated by the thermal reaction of the catalyst required by the heating device, is the main subject to be solved by the present invention.

SUMMERY OF THE UTILITY MODEL

According to the utility model discloses a catalyst structure of a heating reaction furnace, which comprises a plurality of catalyst objects, wherein the plurality of catalyst objects are arranged inside a reaction chamber of the reaction furnace; wherein, each catalyst comprises at least three or more than three blocks made of different materials, such as: each block can be made of one of copper oxide, iron oxide, zirconium oxide, zinc oxide, aluminum oxide or manganese oxide, and three blocks are combined (such as high-temperature sintering) to form a three-dimensional catalyst object, and a columnar elastic body is arranged in the range of each block of the catalyst object.

The shape of the catalyst can be a sphere or a cube, and the elastic body can be a column body in the form of a spiral spring.

The utility model is technically characterized in that a plurality of catalyst substances are utilized to generate continuous heat energy in a reaction furnace, a heating pipe arranged in the reaction furnace is heated, the heating pipe discharges hot air to the indoor space, the temperature of the indoor space is effectively improved, and carbonized particles generated by heating air (central heating) in a traditional color combustion mode can be avoided, thereby effectively improving the air quality; meanwhile, each catalyst is combined into a three-dimensional shape by at least three blocks made of different materials, a columnar elastic body is arranged in the range of each block of the catalyst, and the elastic bodies arranged in each block of the catalyst are mutually supported and supported, so that a space for air circulation is formed between the catalyst and another catalyst, the oxygen content required by the thermal reaction of each catalyst is further increased, and the thermal benefit generated by the thermal reaction of the catalyst is further improved.

In addition, the catalyst is reused and a columnar elastomer is arranged in the range of each block, when a plurality of catalysts are stacked in the reaction chamber respectively, the elastomers of each block of the catalyst can mutually support and conflict with each other, so that each catalyst forms basic positioning capability, and the problems of displacement and shaking (rolling) of the plurality of catalysts in the reaction chamber are effectively improved and avoided.

Drawings

The present invention will be described in further detail with reference to the accompanying drawings and specific embodiments.

FIG. 1 is an overall structural view of a heating reactor according to the present invention;

FIG. 2 is a perspective view of the catalyst structure of the heating reactor of the present invention;

FIG. 3 is a plan view of the catalyst structure of the heating reactor of the present invention;

FIG. 4 is a schematic diagram showing a catalyst structure stacking state of the heating reactor of the present invention;

FIG. 5 is a schematic view of another stack state of the catalyst structure of the heating reactor of the present invention.

Description of the reference numerals

1. Reaction furnace

10. Reaction chamber

11. Heating tube

111. Air outlet end

112. Air inlet end

12. Exhaust gas discharge port

13. Heating device

14. Control panel

15. Sensor with a sensor element

16. Heat insulation layer

2. Catalyst material

21. Block

22. Elastic body

3. Air suction device

31. Blower fan

32. A first pipe body

33. Second tube

4. Fuel device

41. Fuel cartridge

42. Fuel pump

43. Third tube

44. Fourth tube

45. Atomizer

5. Indoor space

D. The distance of air circulation.

Detailed Description

The technical solution in the embodiment of the present invention is clearly and completely described below with reference to the drawings in the embodiment of the present invention. In the following description, numerous specific details are set forth in order to provide a thorough understanding of the present invention, but the present invention may be implemented in other ways different from the specific details set forth herein, and one skilled in the art may similarly generalize the present invention without departing from the spirit of the present invention, and therefore the present invention is not limited to the specific embodiments disclosed below.

As shown in fig. 1 to 5, the present invention discloses a catalyst structure for a heating reactor, especially for a reactor 1, wherein a reaction chamber 10 is disposed inside the reactor 1, the catalyst structure of the present invention is configured to be disposed in the reaction chamber 10, and the catalyst structure comprises a plurality of catalysts 2.

Each catalyst 2 includes at least three blocks 21 made of different materials, such as: the material of each block 21 can be one of copper oxide, iron oxide, zirconium oxide, zinc oxide, aluminum oxide, manganese oxide or other metal oxides, three blocks 21 are mutually combined in a high-temperature sintering way to form a three-dimensional catalyst 2, and the catalyst 2 is respectively provided with a columnar elastic body 22 in the range of each block 21. The catalyst 2 may be in the form of sphere, cube or other shape. The resilient body 22 may be a cylindrical body in the form of a coil spring.

The reaction furnace 1 further comprises a gas absorbing device 3 and a fuel device 4, a reaction chamber 10 is arranged in the reaction furnace 1, the reaction chamber 10 is provided with a heating pipe 11, one end of the heating pipe 11 is provided with a gas outlet end 111, the other end of the heating pipe is provided with a gas inlet end 112, the gas outlet end 111 and the gas inlet end 112 respectively extend out of the reaction furnace 1, and the gas outlet end 111 of the heating pipe 11 can extend to be connected to an indoor space 5; the reaction furnace 1 is provided with at least one waste gas discharge port 12, a heater 13, a control panel 14 and a sensor 15, wherein the waste gas discharge port 12 can be arranged at the top position of the reaction furnace 1, the heater 13 and the sensor 15 are respectively electrically connected with the control panel 14, and the control panel 14 controls the heater 13 to be started or closed; in addition, the wall surface of the reaction chamber 10 of the reaction furnace 1 may be provided with an insulating layer 16.

The air suction device 3 is used for being combined with the reaction furnace 1, the air suction device 3 comprises a blower 31, one end of the blower 31 is connected with a first pipe 32, the other end of the blower 31 is connected with a second pipe 33, one end of the first pipe 32 which is not connected with the blower 31 extends and is connected to the indoor space 5, and one end of the second pipe 33 which is not connected with the blower 31 is connected and communicated with the air inlet end 112 of the heating pipe 11; the blower 31 can be electrically connected to the control panel 14, and the control panel 14 controls the blower 31 to be turned on or off.

The fuel apparatus 4 is used for combining with the reaction furnace 1, the fuel apparatus 4 includes a fuel cylinder 41 and a fuel pump 42, a third tube 43 is connected between the fuel cylinder 41 and the fuel pump 42, the other end of the fuel pump 42 is connected with a fourth tube 44, one end of the fourth tube 44 not connected with the fuel pump 42 is extended and connected to the reaction furnace 1, and the fuel cylinder 41 stores fuel, the fuel can be methanol, ethanol, isopropyl alkali, methane and other fuels; the fuel pump 42 can be electrically connected to the control panel 14, and the control panel 14 controls the fuel pump 42 to be turned on or off; in addition, an atomizer 45 is disposed at one end of the fourth tube 44 extending into the reaction furnace 1.

When the blower 31 of the air suction device 3 is started, air (e.g., cool air) in the indoor space 5 is sucked by the first pipe 32 and is sent to the air inlet end 112 of the heating duct 11 by the second pipe 33 via the blower 31; when the fuel pump 42 of the fuel device 4 is activated, the fuel stored in the fuel tank 41 flows through the fuel pump 42 from the third pipe 43 and is then delivered into the reaction furnace 1 from the fourth pipe 44, and the fuel is supplied in an atomized form by the atomizer 45.

When the reactor 1 is started, the heater 13 of the reactor 1 heats the catalytic materials 2 (for example, the heating temperature is about 100 ℃), when the catalytic materials 2 reach a heating temperature, the fuel pump 42 of the fuel equipment 4 conveys the fuel into the reactor 1, so that the catalytic materials 2 can form a thermal reaction with the fuel to continuously generate heat energy, and further heat the heating pipe 11 (as shown in fig. 5), and the heater 13 can be closed at this time without heating the catalytic materials 2; however, the temperature of the indoor space 5 can be raised for heating by drawing out the cool air in the indoor space 5 by the blower 31 of the air suction device 3 and sending the cool air to the heating duct 11 for heating, and then discharging the hot air to the indoor space 5 through the air outlet end 111 of the heating duct 11.

Thus, the catalyst 2 in the reaction furnace 1 can react with the fuel to generate heat energy continuously, and the reaction process of the catalyst 2 and the fuel only discharges carbon dioxide and water (namely, the carbon dioxide and the water are discharged from the exhaust gas outlet 12 of the reaction furnace 1), so that air heating in a combustion mode is not needed, and carbonized particles generated during combustion are avoided, thereby effectively improving the air quality, and simultaneously, the danger of open fire and the danger of pressure explosion caused by combustion are avoided; the catalyst 2 can be used for other heating purposes (such as geothermal heating, wall heating … and the like) because carbon dioxide and water discharged by the reaction of the catalyst and fuel have high temperature; when the reactor 1 is in operation, the temperature of the reactor 1 is monitored by the sensor 15, the temperature information is transmitted from the sensor 15 to the control panel 14, and the control panel 14 controls the fuel pump 42 to start, stop or intermittently start according to the temperature information.

The utility model is technically characterized in that a plurality of catalyst objects 2 are utilized to generate continuous heat energy in a reaction furnace 1 so as to heat a heating pipe 11 arranged in the reaction furnace 1, and hot air is discharged to an indoor space 5 by the heating pipe 11, thereby effectively improving the temperature of the indoor space 5, avoiding the generation of carbonized particles by heating the air (central heating) in the traditional combustion mode, and effectively improving the air quality; meanwhile, each catalyst 2 is combined into a three-dimensional shape by at least three blocks 21 made of different materials, and the catalyst 2 is provided with a columnar elastic body 22 within the range of each block 21, and the elastic body 22 of each block 21 of the catalyst 2 is used for mutual interference and support, so that a gap D (shown in figure 4) for air circulation can be formed between the catalyst 2 and another catalyst 2, the oxygen content required by the thermal reaction of each catalyst 2 is further met, and the thermal benefit generated after the thermal reaction of the catalyst 2 can be further improved.

In addition, the catalyst 2 is further provided with a columnar elastic body 22 within each block 21, when a plurality of catalysts 2 are stacked in the reaction chamber 10, the elastic bodies 22 of each block 21 of the catalysts 2 can abut against and support each other, so that each catalyst 2 forms a basic positioning capability, thereby effectively improving and avoiding the problems of displacement and shaking (rolling) of the plurality of catalysts 2 in the reaction chamber 10.

It is obvious that the described embodiments are only some of the embodiments of the present invention, and not all of them. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.

Claims

1. The utility model provides a catalyst structure of heating reacting furnace, this reacting furnace inside is equipped with a reaction chamber, and this catalyst structure sets up in this reaction chamber, its characterized in that, this catalyst structure includes:

the catalyst comprises at least three blocks made of different materials, the three blocks are mutually combined into a three-dimensional catalyst, and a columnar elastomer is arranged in the range of each block of the catalyst;

the catalytic objects are respectively stacked and arranged in the reaction chamber, and the elastic bodies arranged in each block of the catalytic objects are mutually used for abutting and supporting, so that a space for air circulation is formed between each catalytic object and the other catalytic object.

2. The catalyst structure of claim 1, wherein each of the blocks is made of any one of copper oxide, iron oxide, zirconium oxide, zinc oxide, aluminum oxide and manganese oxide.

3. The catalyst structure for heating a reactor according to claim 1, wherein the catalyst is spherical.

4. The catalyst structure for heating a reactor according to claim 1, wherein the catalyst is cubic.

5. The catalyst structure for heating a reactor according to claim 1, wherein the elastic body is a columnar body in the form of a coil spring.