A burner
By using a combination technology of hydrogen, fuel catalytic mixer and thermal cracking catalyst in the combustion device, the problems of flame instability and pollution emissions of existing combustion devices are solved, and an efficient and clean combustion effect is achieved.
Patent Information
- Application Number
- CN202110245520.9
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2021-03-05
- Publication Date
- 2025-02-25
- Estimated Expiration
- 2041-03-05
AI Technical Summary
The flames of existing combustion devices are unstable during combustion, resulting in high content of carbon monoxide, carbon dioxide, sulfur dioxide, hydrocarbons and nitrogen oxides in the exhaust gas, causing serious air pollution.
Using a hydrogen and fuel catalytic mixer, hydrogen and fuel are catalyzed in the first step through the split cracking catalytic hydrogen supply pipeline and the inlet pipeline, and then the second step of the heat cracking catalytic is carried out through the fixed heater and the thermal cracking catalyst, and the catalytic conductor is sprayed out and ignited for combustion.
The combustion of fuel catalyzed by hydrogen catalyzing the cracking and combustion is improved, and the pollution emissions are reduced, especially the emissions of hydrocarbons are reduced by 50-90%, while improving the stability and efficiency of combustion.
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Figure CN112879944B_ABST
Abstract
Description
Technical Field
[0001] The invention belongs to the technical field of combustion devices, and in particular relates to a burner. Background Art
[0002] As we all know, the environmental pollution that humans rely on for survival is mainly carbon dioxide, sulfur dioxide, hydrocarbons, nitrogen oxides, which have caused great harm to people's physical and mental health. According to domestic and foreign statistics, more than 75% of environmental pollution in urban areas comes from the incomplete combustion of fossil and bioenergy. The generation of environmental pollution depends on the nature of the fuel used. At present, most fuels are solid fossils, biofuels and liquid gasoline, diesel, pipeline gas, etc. The official scientific names of their main components are carbon monoxide, carbon dioxide, C5-C12 alkanes and C15-C18 alkanes. When they burn, the flames are not stable and thorough enough. The exhaust gas contains high levels of carbon monoxide, carbon dioxide, sulfur dioxide, hydrocarbons, and nitrogen oxides, causing serious air pollution.
[0003] However, it has brought two major hazards to mankind that are still difficult to resolve: one is the emission of carbon dioxide and hydrocarbons. The other is the emission of sulfur dioxide and nitrogen oxides. It has seriously polluted the living environment on which humans depend for survival;
[0004] In response to the above two major problems that have attracted worldwide attention, some countries have also taken corresponding measures to reduce emissions accordingly. However, these two fatal problems have not been fundamentally solved so far.
[0005] Hydrogen is an energy carrier. People can use the energy stored in hydrogen on a large scale. Hydrogen, as a secondary energy source, is not only highly energy efficient, but also does not produce waste such as carbon dioxide and sulfur dioxide. It is clean, efficient, widely available, and renewable. The development of hydrogen energy and its rational application is expected to become an important way to improve energy efficiency, reduce pollution emissions, reduce the consumption of fossil energy and bioenergy, ensure energy security, improve the ecological environment, and achieve energy diversification.
[0006] Hydrogen energy is regarded as the ultimate energy source for mankind in today's society. It is an extremely superior new energy source. The reasons are: ① Water is inexhaustible as a renewable energy source. ② The fuel after hydrogen cracking and catalytic combustion greatly reduces the emission of polluting gases. The main advantages are: increasing the calorific value of combustion, reducing pollution emissions, changing the energy structure, and saving fuel consumption. The calorific value of each kilogram of fuel after cracking and catalytic combustion can be increased by 20-35%. When used in internal combustion engines, it can increase the thermal efficiency of gasoline by 17%. It is a classic process of recycling and sustainable development of natural materials. Summary of the invention
[0007] The present invention aims at solving the above problems and provides a burner with good use effect.
[0008] To achieve the above-mentioned purpose, the present invention adopts the following technical scheme, which includes a hydrogen and fuel catalytic mixer 1, characterized in that the air inlet of the hydrogen and fuel catalytic mixer 1 is connected to one end of a split cracking catalytic hydrogen supply pipeline 5, the liquid inlet of the hydrogen and fuel catalytic mixer 1 is connected to a split cracking catalytic liquid inlet pipeline 4, the outlet of the hydrogen and fuel catalytic mixer 1 is connected to the inlet of a fixed heater 8, the fixed heater 8 is connected to a thermal cracking catalyst 3, a catalyst guide hole is provided on the thermal cracking catalyst 3, and a heat radiator 11 is provided on the hydrogen and fuel catalytic mixer 1.
[0009] As a preferred solution, the thermal cracking catalyst 3 of the present invention is arranged in the heat-conducting support bowl 2 .
[0010] As another preferred embodiment, the other end of the split cracking catalytic hydrogen supply pipeline 5 of the present invention is connected to the main hydrogen and oxygen supply pipeline 6, and the other end of the split cracking catalytic liquid inlet pipeline 4 is connected to the main liquid fuel supply pipeline 7;
[0011] The split cracking catalytic hydrogen supply pipeline 5 and the split cracking catalytic liquid inlet pipeline 4 are both L-shaped tubes, and the upper horizontal tube end of the L-shaped tube is connected to the hydrogen and fuel catalytic mixer 1; the hydrogen and oxygen main supply pipeline 6 and the liquid fuel main supply pipeline 7 are both horizontal pipelines, which are arranged on both sides below the hydrogen and fuel catalytic mixer 1, and the connection positions of the split cracking catalytic hydrogen supply pipeline 5 and the split cracking catalytic liquid inlet pipeline 4 and the hydrogen and fuel catalytic mixer 1 are placed on both sides of the hydrogen and fuel catalytic mixer 1.
[0012] As another preferred embodiment, the split cracking catalytic liquid inlet pipeline 4 of the present invention is a hydrocarbon liquid inlet pipeline.
[0013] As another preferred embodiment, the hydrogen and fuel catalytic mixer 1 of the present invention includes an annular side wall, the annular side wall has an inner cavity, a transverse tube is arranged in the upper inner part of the annular side wall, both ends of the transverse tube are connected with the inner cavity, the lower end of the middle part of the transverse tube is connected with the upper end of the vertical tube, the lower end of the vertical tube is an external threaded joint, an upper cover plate is arranged in the annular side wall above the transverse tube, and a heat radiation through hole is arranged on the upper cover plate; the inner cavity is respectively connected with the split cracking catalytic hydrogen supply pipeline 5 and the split cracking catalytic liquid inlet pipeline 4; a long nut 10 is screwed on the external threaded joint.
[0014] As another preferred embodiment, the annular side wall of the present invention is in the shape of a circular ring, and the upper and lower ends of the outer wall of the annular side wall are in arc transition.
[0015] As another preferred embodiment, the through holes in the present invention are multiple evenly distributed diamond-shaped holes.
[0016] As another preferred embodiment, the outer wall of the vertical pipe at the upper end of the external threaded joint of the present invention protrudes outward to form a flange.
[0017] As another preferred embodiment, the thermal cracking catalyst 3 of the present invention is in the shape of a truncated cone, with a top plate at the upper end of the truncated cone, a middle through hole is provided in the middle of the top plate, a fixed heater 8 is connected to the outlet of the hydrogen and fuel catalytic mixer 1 through the middle through hole, and a catalyst guide hole is provided on the top plate around the middle through hole.
[0018] As another preferred embodiment, the heating wire of the fixed heater 8 of the present invention is arranged in a vertical externally threaded sleeve, the upper end of the externally threaded sleeve passes through the middle through hole of the heat-conducting support bowl 2 and the middle through hole of the thermal cracking catalyst 3 in turn, and is screwed into the lower part of the long nut 10, and the part of the externally threaded sleeve placed in the thermal cracking catalyst 3 is provided with a catalytic body through hole; a nut 14 is screwed on the externally threaded sleeve at the lower end of the heat-conducting support bowl 2, and a sealing plate is provided at the lower end of the externally threaded sleeve.
[0019] As another preferred embodiment, the heating wire of the present invention is arranged in a U shape in an externally threaded sleeve, the two sides of the U shape are arranged along the length direction of the externally threaded sleeve, the lower end of the U shape is placed at the lower end of the externally threaded sleeve, and a heating wire power cord connection hole is provided on the externally threaded sleeve.
[0020] As another preferred embodiment, an igniter 9 is provided on the heat-conducting support bowl 2 of the present invention, and the ignition end of the igniter 9 is placed above the catalytic body guide hole on the thermal cracking catalyst 3.
[0021] As another preferred embodiment, the igniter 9 described in the present invention adopts an electronic igniter, which is connected to the outer wall of the heat-conducting support bowl 2 through an L-shaped connector. A notch is provided on the heat-conducting support bowl 2 corresponding to the setting position of the igniter 9. The ignition end of the electronic igniter extends through the notch to above the catalyst guide hole on the thermal cracking catalyst 3.
[0022] As another preferred embodiment, the front lower horizontal end of the L-shaped connector of the present invention is welded to the lower outer wall of the heat-conducting support bowl 2, and the rear upper vertical plate of the L-shaped connector is provided with a mounting hole for the electronic igniter.
[0023] Secondly, the hydrogen and oxygen main supply pipeline 6 of the present invention is connected to the buffer tank outlet through a one-way valve, and the buffer tank inlet is connected to the outlet of the hydrogen and oxygen preparation device; the liquid fuel main supply pipeline 7 is connected to the fuel tank through a filter and a delivery pump.
[0024] In addition, the heat radiation through hole of the present invention is provided with a pressure sensor, and the catalyst guide hole is provided with a photosensitive sensor.
[0025] The invention has beneficial effects.
[0026] The present invention uses hydrogen as the cracking catalytic gas raw material, supplies hydrogen to the fuel catalytic mixer 1 through the split cracking catalytic hydrogen supply pipeline 5 for the first step of catalysis, and then enters the cracking catalyst 3 through the fixed heater 8 for the second step of heating and cracking catalysis, and is ejected through the catalyst body guide hole and ignited by the igniter for combustion.
[0027] The fixed heater 8 of the present invention heats the catalyzed fuel to gasify it and make the combustion more complete.
[0028] The thermal cracking catalyst 3 of the present invention provides a buffer space for mixing, thereby ensuring the stable operation of the device. BRIEF DESCRIPTION OF THE DRAWINGS
[0029] The present invention is further described below in conjunction with the accompanying drawings and specific implementation methods. The protection scope of the present invention is not limited to the following description.
[0030] Figure 1 It is a schematic diagram of the structure of the present invention.
[0031] Figure 2 It is a schematic diagram of the structure of the hydrogen and fuel catalytic mixer of the present invention.
[0032] Figure 3 It is a cross-sectional view of the hydrogen and fuel catalytic mixer of the present invention.
[0033] Figure 4 It is a schematic diagram of the long nut structure of the present invention.
[0034] Figure 5 It is a schematic diagram of the structure of the thermal cracking catalyst of the present invention.
[0035] Figure 6 It is a schematic diagram of the structure of the fixed heater of the present invention. DETAILED DESCRIPTION
[0036] As shown in the figure, the present invention includes a hydrogen and fuel catalytic mixer 1, the air inlet of the hydrogen and fuel catalytic mixer 1 is connected to one end of a split cracking catalytic hydrogen supply pipeline 5, the liquid inlet of the hydrogen and fuel catalytic mixer 1 is connected to a split cracking catalytic liquid inlet pipeline 4, the outlet of the hydrogen and fuel catalytic mixer 1 is connected to the inlet of a fixed heater 8, the fixed heater 8 is connected to a thermal cracking catalyst 3, a catalyst guide hole is provided on the thermal cracking catalyst 3, and a heat radiator 11 is provided on the hydrogen and fuel catalytic mixer 1.
[0037] The thermal cracking catalyst 3 is arranged in the heat-conducting support bowl 2. The heat-conducting support bowl 2 can prevent the fuel from falling and make full use of the fuel.
[0038] The other end of the split cracking catalytic hydrogen supply pipeline 5 is connected to the main hydrogen and oxygen supply pipeline 6, and the other end of the split cracking catalytic liquid inlet pipeline 4 is connected to the main liquid fuel supply pipeline 7;
[0039] The split cracking catalytic hydrogen supply pipeline 5 and the split cracking catalytic liquid inlet pipeline 4 are both L-shaped tubes, and the upper horizontal tube end of the L-shaped tube is connected to the hydrogen and fuel catalytic mixer 1; the hydrogen and oxygen main supply pipeline 6 and the liquid fuel main supply pipeline 7 are both horizontal pipelines, which are arranged on both sides below the hydrogen and fuel catalytic mixer 1, and the connection positions of the split cracking catalytic hydrogen supply pipeline 5 and the split cracking catalytic liquid inlet pipeline 4 and the hydrogen and fuel catalytic mixer 1 are placed on both sides of the hydrogen and fuel catalytic mixer 1.
[0040] The hydrogen and fuel catalytic mixer 1 comprises an annular side wall, which has an inner cavity. A transverse tube 15 is arranged in the upper inner part of the annular side wall, and both ends of the transverse tube are connected with the inner cavity 17. The lower end of the middle part of the transverse tube is connected with the upper end of the vertical tube 16. The lower end of the vertical tube is an external threaded joint. An upper cover plate 18 is arranged in the annular side wall above the transverse tube, and a heat radiation through hole is arranged on the upper cover plate; the inner cavity is respectively connected with the split cracking catalytic hydrogen supply pipeline 5 and the split cracking catalytic liquid inlet pipeline 4; a long nut 10 is screwed on the external threaded joint.
[0041] The annular side wall is in the shape of an annulus, and the upper and lower ends of the outer wall of the annular side wall are in arc transition.
[0042] The through holes are multiple evenly distributed rhombus-shaped holes (which facilitate the use of tools to clamp the hydrogen and fuel catalytic mixer 1 through the rhombus-shaped holes for installation).
[0043] The outer wall of the vertical pipe at the upper end of the external threaded joint protrudes outward to form a flange.
[0044] The thermal cracking catalyst 3 is in the shape of a truncated cone, with a top plate at the upper end of the truncated cone, a middle through hole 19 is arranged in the middle of the top plate, a fixed heater 8 passes through the middle through hole and is connected to the outlet of the hydrogen and fuel catalytic mixer 1, and a catalyst guide hole is arranged on the top plate around the middle through hole.
[0045] The heating wire 20 of the fixed heater 8 is arranged in a vertical externally threaded sleeve, the upper end of the externally threaded sleeve passes through the middle through hole of the heat-conducting support bowl 2 and the middle through hole of the thermal cracking catalyst 3 in turn, and is screwed into the lower part of the long nut 10, and the part of the externally threaded sleeve placed in the thermal cracking catalyst 3 is provided with a catalytic body through hole; a nut is screwed on the externally threaded sleeve at the lower end of the heat-conducting support bowl 2, and a sealing plate is provided at the lower end of the externally threaded sleeve.
[0046] The heating wire is arranged in a U shape in the external threaded sleeve, the two sides of the U shape are arranged along the length direction of the external threaded sleeve, the lower end of the U shape is placed at the lower end of the external threaded sleeve, and a heating wire power line connection hole is arranged on the external threaded sleeve.
[0047] An igniter 9 is arranged on the heat-conducting support bowl 2 , and an ignition end of the igniter 9 is placed above the catalytic body guide hole on the thermal cracking catalyst 3 .
[0048] The igniter 9 is an electronic igniter, which is connected to the outer wall of the heat-conducting support bowl 2 through an L-shaped connector 12. A notch is provided on the heat-conducting support bowl 2 corresponding to the setting position of the igniter 9. The ignition end of the electronic igniter extends through the notch to above the catalyst guide hole 13 on the thermal cracking catalyst 3.
[0049] The front lower horizontal end of the L-shaped connector is welded to the lower outer wall of the heat-conducting support bowl 2, and the rear upper vertical plate of the L-shaped connector is provided with a mounting hole for the electronic igniter.
[0050] The main hydrogen and oxygen supply pipeline 6 is connected to the outlet of the buffer tank through a one-way valve, and the inlet of the buffer tank is connected to the outlet of the hydrogen and oxygen preparation device; the main liquid fuel supply pipeline 7 is connected to the fuel tank through a filter and a delivery pump. The buffer tank ensures stable gas supply pressure, stable cracking and catalytic combustion.
[0051] A pressure sensor is provided at the heat radiation through hole, and a photosensitive sensor is provided at the catalyst guide hole. The flow of fuel and gas is controlled by pressure detection, and the power of the fixed heater 8 is controlled to control the pressure at the heat radiation through hole at 0.2MP to 0.3MP. The photosensitive sensor detects whether the ignition is successful and controls the electronic igniter to be turned off.
[0052] The present invention is a hydrogen-oxygen cracking catalytic integrated burner, with hydrogen catalysis and oxygen combustion assistance.
[0053] The split cracking catalytic liquid inlet pipeline 4 is a hydrocarbon liquid inlet pipeline. Hydrogen likes to absorb carbon molecules of hydrocarbons due to its characteristics, thereby changing the structure of combustible gas molecules, allowing the fuel to be fully burned, thereby reducing the hydrocarbon content in the emitted harmful gases by 50-90%. The high-purity oxygen generated simultaneously can be used for oxygen-enriched combustion, which is environmentally friendly and efficient.
[0054] The liquid fuel of the present invention can be methanol, and an aqueous hydrogen and oxygen generating device (a device with patent number 200810229903.1 and name "aqueous hydrogen and oxygen source integrated extraction multi-purpose device") can be used to generate hydrogen and oxygen.
[0055] The present invention can be placed in a furnace to heat the furnace body when in use, and can control the flow of fuel and gas and the power of the fixed heater 8 by detecting the temperature of the furnace body.
[0056] The present invention is suitable for independent single-unit applications, and can also be used in combination of multiple modules. It is suitable for distributed energy applications in industry, agriculture, home, military, scientific research, etc.
[0057] It can be understood that the above specific description of the present invention is only used to illustrate the present invention and is not limited to the technical solutions described in the embodiments of the present invention. Those skilled in the art should understand that the present invention can still be modified or replaced by equivalents to achieve the same technical effects; as long as the use requirements are met, they are within the protection scope of the present invention.
Claims
1. A burner comprising a hydrogen and fuel catalytic mixer (1), characterized in that The air inlet of the hydrogen and fuel catalytic mixer (1) is connected to one end of the split cracking catalytic hydrogen supply pipeline (5), the liquid inlet of the hydrogen and fuel catalytic mixer (1) is connected to the split cracking catalytic liquid inlet pipeline (4), the outlet of the hydrogen and fuel catalytic mixer (1) is connected to the inlet of the fixed heater (8), the fixed heater (8) is connected to the thermal cracking catalyst (3), the thermal cracking catalyst (3) is provided with a catalyst body guide hole, and the hydrogen and fuel catalytic mixer (1) is provided with a heat radiator (11); Hydrogen is used as the cracking catalytic gas raw material, hydrogen is supplied through the split cracking catalytic hydrogen supply pipeline (5), fuel is supplied through the split cracking catalytic liquid inlet pipeline (4), the first step of catalysis is carried out in the hydrogen and fuel catalytic mixer (1), and then the catalytic gas enters the thermal cracking catalyst (3) through the fixed heater (8) for the second step of heating and cracking catalysis, and is ejected through the catalyst body guide hole, ignited by the igniter, and burned; The fixed heater (8) heats the catalyzed fuel; The thermal cracking catalyst (3) provides a buffer space for mixing; The hydrogen and fuel catalytic mixer (1) comprises an annular side wall, the annular side wall has an inner cavity, a transverse tube is arranged in the upper part of the annular side wall, both ends of the transverse tube are connected to the inner cavity, the lower end of the middle part of the transverse tube is connected to the upper end of the vertical tube, the lower end of the vertical tube is an external thread joint, an upper cover plate is arranged in the annular side wall above the transverse tube, and a heat radiation through hole is arranged on the upper cover plate; the inner cavity is respectively connected to the split cracking catalytic hydrogen supply pipeline (5) and the split cracking catalytic liquid inlet pipeline (4); a long nut (10) is screwed on the external thread joint; The thermal cracking catalyst (3) is arranged in the heat-conducting support bowl (2); The heating wire of the fixed heater (8) is arranged in a vertical externally threaded sleeve, the upper end of the externally threaded sleeve passes through the middle through hole of the heat-conducting support bowl (2) and the middle through hole of the thermal cracking catalyst (3) in sequence and is screwed into the lower part of the long nut (10), and the part of the externally threaded sleeve placed in the thermal cracking catalyst (3) is provided with a catalytic body through hole; a nut (14) is screwed onto the externally threaded sleeve at the lower end of the heat-conducting support bowl (2), and a sealing plate is provided at the lower end of the externally threaded sleeve.
2. A burner according to claim 1, characterized in that The other end of the split cracking catalytic hydrogen supply pipeline (5) is connected to the main hydrogen and oxygen supply pipeline (6), and the other end of the split cracking catalytic liquid inlet pipeline (4) is connected to the main liquid fuel supply pipeline (7); The split cracking catalytic hydrogen supply pipeline (5) and the split cracking catalytic liquid inlet pipeline (4) are both L-shaped tubes, and the upper transverse tube end of the L-shaped tube is connected to the hydrogen and fuel catalytic mixer (1); the hydrogen and oxygen main supply pipeline (6) and the liquid fuel main supply pipeline (7) are both transverse pipelines, which are arranged on both sides below the hydrogen and fuel catalytic mixer (1), and the connection positions of the split cracking catalytic hydrogen supply pipeline (5) and the split cracking catalytic liquid inlet pipeline (4) and the hydrogen and fuel catalytic mixer (1) are arranged on both sides of the hydrogen and fuel catalytic mixer (1).
3. A burner according to claim 1, characterized in that The split cracking catalytic liquid inlet pipeline (4) is a hydrocarbon liquid inlet pipeline.
4. A burner according to claim 1, characterized in that The thermal cracking catalyst (3) is in the shape of a truncated cone cylinder, with a top plate at the upper end of the truncated cone cylinder, a middle through hole being arranged in the middle of the top plate, a fixed heater (8) passing through the middle through hole and connected to the outlet of the hydrogen and fuel catalytic mixer (1), and a catalyst guide hole being arranged on the top plate around the middle through hole.
5. A burner according to claim 1, characterized in that The heating wire is arranged in a U shape in the external threaded sleeve, the two sides of the U shape are arranged along the length direction of the external threaded sleeve, the lower end of the U shape is placed at the lower end of the external threaded sleeve, and a heating wire power line connection hole is arranged on the external threaded sleeve.
6. A burner according to claim 1, characterized in that An igniter (9) is arranged on the heat-conducting support bowl (2), and an ignition end of the igniter (9) is placed above the catalytic body guide hole on the thermal cracking catalyst (3).
7. A burner according to claim 6, characterized in that The igniter (9) is an electronic igniter, which is connected to the outer wall of the heat-conducting support bowl (2) via an L-shaped connector. A notch is provided on the heat-conducting support bowl (2) corresponding to the location where the igniter (9) is provided, and an ignition end of the electronic igniter extends through the notch to above the catalytic body guide hole on the thermal cracking catalyst (3).
Citation Information
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