JP2012189307A - Gas generation method of technological configuration for providing external force motion to action and reaction of fluid motion, and carbon dioxide decomposition, oxygen separation system - Google Patents

Abstract

PROBLEM TO BE SOLVED: To solve a key problem that assured clean combustion technology for every kind of fossil fuel and the like is uncompleted currently, leading to generation sources of air pollution, as a problem that a combustion method of a nozzle spraying method is mainly predominant for fossil fuel and various liquid fuels for global main energy and particles of spraying fuel are coarse in density, and flame moves straight at high speed in a combustion furnace, thus leaving uneven portions in mixing of spraying fuel and air and resulting in heat quantity loss of portions which are not completely burnt and a cost increase of purification facilities for harmful exhaust gas, and a problem of carbon dioxide reduction are overlapped.SOLUTION: A clean combustion system is constituted which eliminates the need for a nozzle and uses a new principle of generating gas with a technological configuration for making a means of clean combustion of fossil fuel and the like generate special fluid motion of gas in a combustion chamber, and for providing external force motion to an acceleration means for action and reaction thereof, and a separation system is constituted which decomposes a carbon dioxide of exhaust gas into oxygen, a carbon dioxide, and the like. In the humidified combustion of the system, superfine particles of water are decomposed by heat of flame, hydrogen is heated, and oxygen is added to oxygen in the air, causing clean combustion.

Description

  According to the world's primary energy situation, fossil fuels, which are said to be the source of air pollution, are converted into fossil fuels in the atmospheric environment by the combustion system based on the new gas generation principle of the present invention. Innovation to improve energy.

In the state-of-the-art technology of industrial combustion equipment of the conventional method, for the liquid fuel, the combustion method of the nozzle spray method is mainly used, and the spray particles are coarse in density, and the flame travels straight in the combustion furnace, so the residence time of the flame in the furnace In many cases, the mixture of sprayed fuel and air is non-uniform because it is short, and even in the state-of-the-art technology of electronic control and high-pressure nozzle system, liquid fuels include city gas and L.P. P. G. It is currently clearing environmental standards by purifying system technology for exhaust gas containing unburned energy that cannot be cleanly burned, such as natural gas, and as a countermeasure against pollution of remaining unburned parts even in automobiles Is cleared by the technology of exhaust gas purification system using catalyst.
However, with the conventional combustion method, the current situation seems to be the limit. On the other hand, with coal combustion, the adjustment combustion of the amount of air sent into the combustion furnace is the mainstream, and with these conventional technologies, a part of the fuel is released into the atmosphere without being converted into thermal energy. However, there is a problem of the loss of unburned energy and the high cost of the equipment of the exhaust gas purification system. In all types of fossil fuels that are said to be sources of air pollution, city gas and L.P. P. G. Establishment of clean combustion technology such as natural gas is required.

  There is no literature related to the present invention.

  Iwanami, Physics and Chemistry Dictionary, 5th edition, related to the third law of motion and the law of action and reaction among the three laws of motion on page 121.

  As described above, even in the state-of-the-art technology of electronic control and high-pressure nozzle method, the current state of liquid fuel is limited in the conventional combustion method, and in coal combustion, adjustment combustion of the amount of air sent into the combustion furnace remains the mainstream and there is no progress Because these issues are still unresolved, the world's primary energy situation describes fossil fuels as the source of air pollution.

As a means for solving the above problems, the present invention provides a clean combustion method, decomposition of carbon dioxide, and decomposition of oxygen and carbon monoxide by a combustion system based on a new gas generation principle having a technical configuration that gives external force motion to the action and reaction of fluid motion. And so on. Specifically, a concave circular body with a fan blade in a cylindrical shape is installed, and external force motion is given to the concave circular body, so that the main air flow of forward action is generated in the cylindrical shape. The generated air becomes a forward high-speed lateral fluid motion within the cylinder. The central portion reacts with the forward flow, and a high-speed recirculation phenomenon occurs in the cylindrical shape due to the interaction of the air flow and the reaction.
If fuel is sent during the high-speed recirculation phenomenon of reaction and reaction, fuel gas of high-speed transverse fluid motion of ultrafine particles is generated, and if the gas is ignited, extremely clean combustion occurs.
The thickness of the ultrafine particles of the fuel gas is proportional to the amount of external force kinetic energy applied to the concave circular body.

System exhaust gas is burned in the present invention, decomposition of CO ₂ to a high temperature reversibly C0 and O ₂ by the catalytic effect of passing the multilayer arrangement of platinum-based special catalysts, further molecules of the cooling layer C0 and O ₂ , O ₂ is released to the atmosphere through an oxygen permeable membrane filter, and the remaining C0 etc. is sent to the combustion chamber for recombustion.

  The ultrafine gas according to the present invention burns in a combustion chamber with a more uniform mixing of fuel, air, and oxygen due to the movement phenomenon of the high-speed lateral fluid. The staying time of the flame in the combustion chamber is extremely long due to the movement phenomenon of the lateral fluid, and the high temperature gas in the center portion of the flame causes a reflux phenomenon toward the back of the combustion chamber. For this reason, the ultrafine gas gas fuel is burned and exhausted in the combustion furnace so that meteors enter the atmosphere and burned out in the combustion chamber, resulting in clean combustion with a further improved thermal conversion rate of the fuel.

  In the humidified combustion of the mixture of the water ultrafine particles (minimum molecular level) gas generated by the gas generation principle of the present invention and the fuel gas, the ultrafine water particles are decomposed by the heat of the flame and hydrogen is exothermic, Oxygen is added to oxygen in the air to improve combustion, and excess oxygen is released into the atmosphere.

  Even the combustion of fossil fuels, which has been said to be a source of air pollution, has the merit of releasing oxygen into the atmosphere by thermal decomposition of ultrafine water particles in the present invention. Combustion of fossil fuels generates a new phenomenon of gas motion due to the new gas generation principle of the present invention, and the new combustion system thereby reverses the combustion of fossil fuels to the improvement of the atmospheric environment. Innovation.

  As described above, the fossil fuel, which has been said to be the source of air pollution as described above, is a technological innovation for converting fossil fuel into energy for improving the air environment, and gasification of ultrafine particles according to the present invention. The various fuels that enabled clean combustion enabled clean combustion of liquid hydrocarbons, biofuels, coal, and other water-containing contaminants.

Configuration diagram of the present invention Cross-sectional view of the combustion mechanism Sectional view of 3bCO ₂ decomposition mechanism chamber and sectional view of separation mechanism chamber for 4bCO, etc. Overall configuration external view of the present invention

  Hereinafter, embodiments of the present invention will be described with reference to FIGS.

FIG. 1 is a block diagram of the present invention. 1 burner, 2 combustion mechanism, 3CO ₂ decomposition mechanism, 4O ₂ separation mechanism, 5 chimney, 6 and 7 are recombustion circuits such as CO.

FIG. 2 is a sectional view of the structure of the combustion mechanism. The rotational power of motor 1 of the power source is transmitted at high speed to the next pulley-2, shaft 18, fan blade 3a, and concave circular body 3b, and the air 4c generated by fan blade 3a is Main air for forward action. 4a. 4b. The air sucked from each of 4g and 4e travels into the 16 combustion chambers by the high-speed rotation of the concave circular body (gas generator for high-speed lateral fluid motion) 3b.
In the cylindrical combustion chamber, the main air of forward action travels by high-speed transverse fluid motion, but the reaction phenomenon causes the gas to recirculate in the direction of the burner mechanism portion 15 and the cylindrical shape of 16 In the combustion chamber, a high-speed transverse fluid motion phenomenon of air occurs like 6, 7, 8, and 9. Reference numerals 4g and 4e are secondary air inlets. These phenomena are phenomena that can be caused by a technique for applying an external force motion to the reaction within the cylinder.
If liquid fuel is sent from the fuel inlet 10b into the combustion chamber in which such a high-speed transverse fluid motion phenomenon of air occurs, ultrafine gas is generated from the liquid fuel 6, 7, and 8. It becomes an ultrafine gas gas by the action of continuous high-speed transverse fluid motion of 5, 6, 7, 8, and 9.
If the gas gas of ultrafine particles generated by such a mechanism is ignited by the ignition mechanism 10a, clean gasification combustion is achieved in the cylindrical combustion chamber. Further, if water or a spray form of water generated by a humidifier is sent from the water supply inlet W, the water becomes ultrafine particles and is decomposed by the heat of the flame, resulting in extremely clean combustion due to the positive effect of oxygen. The flame shape in the combustion chamber can be controlled by adjusting the amount of air sucked in 11 to 14.
The following is a description of each part of the combustion mechanism of the present invention. Each of the following functions has all the functions shown in FIG.
6 is a first negative pressure part (decompression part) 7 is a second negative pressure part (decompression part) 8 is a gas generation end part, 9 is a trajectory of high-speed lateral fluid motion phenomenon of flame, 10a ignition mechanism, W, supply of water Inlet, 11 flame shape adjusting air inlet, 13 forward-acting main air flow rate adjuster, 14 air quantity adjusting opening / closing mechanism, 15 burner mechanism part, 16 combustion chamber cross section, 17 shaft bearing, 18 shaft. 12a. 12b clean exhaust gas.
[FIG. 3] Sectional view of 3bCO ₂ decomposition mechanism chamber and sectional view of separation mechanism chamber for 4bCO, etc.

Ｏ_２に分解、分解された分子を４ｂ内のｃａ冷却層で分子を安定させてｆｉ酸素透過膜のフィルタ−によってＯ_２を分離、４ｂ内から放出、ＣＯ等を次の図４の１Ｒからｆによって２Ｒより燃焼室へ送る再燃焼のシステムである。Before Figure 2 12a, X of CO ₂ decomposition mechanism 12b is clean exhaust gas in the following figure 3, 3b,

The molecule decomposed into O ₂ is stabilized in the ca cooling layer in 4b, and O ₂ is separated by the filter of the fi oxygen permeable membrane, released from inside 4b, CO, etc. from 1R in the next FIG. This is a re-combustion system that sends the fuel from 2R to the combustion chamber by f.

FIG. 4 shows the overall configuration of the present invention.

1 Burner, 2 Combustion mechanism exterior, 3CO ₂ decomposition mechanism exterior, 4O ₂ etc. separation mechanism exterior, 1R CO recombustion circuit, 2R CO inlet to combustion chamber, 20 chimney, etc. 10b Fuel inlet, W, water supply inlet, f, CO etc. blower to 2R,

  The present invention already has the following experimental results in the system described in FIG. 2 for implementing the above-described invention. Successful gasification and smokeless combustion of heavy oil A, B and C oils, successful gasification and smokeless combustion of waste cooking oil, successful gasification and smokeless combustion of coal, P. G. In the combustion of gas and water mixing, kerosene and water mixing, heavy oil A, B, C oil and water mixing, etc., these fuels succeeded in clean combustion by mixing water 1 or more with fuel 1 by volume. The exhaust gas is tasteless and odorless.

  In the field of application of the technology of the present invention, industrial combustion systems, boilers, heating machines (liquid fuel stoves, large and small warm air heaters for horticultural houses, building heaters, etc.) Gasification system etc.

[FIG. 1] Configuration diagram of the present invention 1 Burner
2 Combustion mechanism 3CO ₂ decomposition mechanism 4O ₂ separation mechanism 5 Chimney 6 and 7 are re-combustion circuits such as CO [FIG.

1 motor
2 Puri
33a Fan 3b Concave round body (gas generator for high-speed transverse fluid motion)
4 4a. 4b. 4c, main air for forward action 4g, 4e are inlets for secondary air 5 gas reaction in the direction of the burner in response to the progress of high-speed lateral fluid movement of main force air for forward action 6 first negative pressure part (Decompression section)
7 Second negative pressure part (pressure reduction part)
8 Gas generation end portion 9 Trajectory of high-speed lateral fluid motion phenomenon of flame 10 10a Ignition mechanism,
10b Fuel inlet W Water supply inlet 11 Flame shape adjusting air inlet 12 12a. 12b Clean exhaust gas 13 Main air flow rate regulator 14 for forward action 14 11 Opening / closing mechanism 15 for adjusting air quantity 15 Burner mechanism section 16 Combustion chamber section 17 Shaft bearing 18 shaft [Fig. 3] 3bCO ₂ decomposition Sectional view of mechanism chamber and sectional view of separation mechanism chamber such as 4bCO

3b Cross-sectional view of CO ₂ decomposition mechanism 4b Cross-sectional view of separation mechanism of O ₂ and CO X Platinum-based special catalyst layer ca cooling layer CL1 cooling medium inlet CL2 cooling medium outlet fi oxygen permeable membrane filter
Separation wall of 19O ₂ and CO, etc. [FIG. 4] Overall configuration external view of the present invention

1 burner
2 Appearance of the combustion mechanism 3 Appearance of the CO ₂ decomposition mechanism chamber 4 Appearance of the ₂ O ₂ separation mechanism 1 Re-combustion circuit for 2R CO, etc. 2R Combustion entrance 20 CO entrance 20 Chimney 10b Fuel entrance W Water supply entrance f CO etc. Blower to 2R

Claims (3)

  A rotating device having a concave circular body with wings is provided in the cylindrical shape, and a flow of air in which a high-speed transverse fluid motion advances is generated in the cylindrical shape by a mechanism that imparts a rotating motion to the rotating device by an external force. In the central part in the cylindrical shape, a recirculation phenomenon of interaction between the action in the air flow direction and the reaction in the opposite direction occurs. A gas generation system for concave high-speed lateral fluid motion that generates ultrafine fuel gas gas by means of sending fuel to the environment of the reflux phenomenon.   A system of mixed combustion of liquid water or water gas generated by a humidifier in the above system and various fuels.   The exhaust gas of the combustion system of claim 1 passes through the mechanism of a platinum-based special catalyst layer, reversibly decomposes carbon dioxide at a high temperature, and further passes through a cooling layer to stabilize molecules such as oxygen and carbon monoxide. After that, oxygen is released to the outside through the filter of the oxygen permeable membrane, and carbon monoxide is sent to the combustion chamber through the recombustion circuit.

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