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KR20150089221A - a combustion system using the mixture fuel of water electrolysis gas and water vapor, and a combustion system with this mixture blended fossil fuel - Google Patents

a combustion system using the mixture fuel of water electrolysis gas and water vapor, and a combustion system with this mixture blended fossil fuel Download PDF

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KR20150089221A
KR20150089221A KR1020140009580A KR20140009580A KR20150089221A KR 20150089221 A KR20150089221 A KR 20150089221A KR 1020140009580 A KR1020140009580 A KR 1020140009580A KR 20140009580 A KR20140009580 A KR 20140009580A KR 20150089221 A KR20150089221 A KR 20150089221A
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fuel
water
gas
mixed
combustion
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KR1020140009580A
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Korean (ko)
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장동순
신미수
방건웅
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충남대학교산학협력단
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C1/00Combustion apparatus specially adapted for combustion of two or more kinds of fuel simultaneously or alternately, at least one kind of fuel being either a fluid fuel or a solid fuel suspended in a carrier gas or air
    • F23C1/08Combustion apparatus specially adapted for combustion of two or more kinds of fuel simultaneously or alternately, at least one kind of fuel being either a fluid fuel or a solid fuel suspended in a carrier gas or air liquid and gaseous fuel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D11/00Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
    • F23D11/10Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space the spraying being induced by a gaseous medium, e.g. water vapour
    • F23D11/16Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space the spraying being induced by a gaseous medium, e.g. water vapour in which an emulsion of water and fuel is sprayed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D11/00Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
    • F23D11/36Details, e.g. burner cooling means, noise reduction means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D17/00Burners for combustion conjointly or alternatively of gaseous or liquid or pulverulent fuel

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Abstract

The present invention relates to a system for burning a mixed fuel obtained by mixing a water electrolytic gas, a water vapor and a fossil fuel, more specifically, a mixed fuel obtained by mixing a water electrolytic gas and water vapor and a system for burning the mixed fuel and a water electrolytic gas, And fossil fuel, and a system for burning the same.
The present invention provides a combustion system comprising a water electrolytic gas generating device (200), a water vapor generating device (300), a gas mixing device (500), and a combustion device (400).
Further, the present invention provides a combustion system using mixed fuel obtained by mixing 100 parts by weight of water electrolytic gas with 1 to 1,000 parts by weight of steam.
The present invention also includes a water electrolytic gas generator 200, a water vapor generator 300, a gas mixing device 500, a fossil fuel supply device 100, a fuel mixing device 600, and a combustion device 400 And a combustion system.
Also, the present invention provides a combustion system using a mixed fuel composed of 1 to 1,000 parts by weight of a fossil fuel mixed with 100 parts by weight of a mixed fuel obtained by mixing 1 to 1,000 parts by weight of steam with 100 parts by weight of a water electrolytic gas .

Description

The present invention relates to a combustion system using a water electrolytic gas and a water vapor mixed fuel and a mixed combustion fuel and a fossil fuel,

The present invention relates to a system for burning a mixed fuel of a water electrolysis gas (also referred to as oxyhydrogen gas or brown gas or HHO) and water vapor, and a fuel mixed with the mixed fuel and a conventional fossil fuel, A mixed fuel obtained by mixing an electrolytic gas and water vapor and a system for burning the same, and a system for burning a fuel obtained by mixing a water electrolytic gas, water vapor and an existing fossil fuel.

Recently, the global energy problem seems to be in a very important phase of adjustment either in terms of policy or technological development. This is due to the seriousness of global warming caused by fossil fuels that have risen sharply over the past 50 years, and the growing anxiety due to the absence of energy problem solving caused by the Chernobyl and Fukushima nuclear accidents.

As part of the countermeasures to this end, it is important to utilize fossil fuels efficiently and to discover more powerful new renewable energy as one of the central theme in the energy field.

It is getting higher.

What is being attempted in recent years as a trend is water decomposition gas generated by so-called electrolysis of water. That is to say, the feasibility of this mixed gas, also called brown gas or HHO gas, as a fuel, and the technique of directly burning or blasting it in an automobile engine or other combustion device or incinerator have been tried in various fields at home and abroad Is being announced

As is well known, when water is electrolyzed, it occurs in the form of a mixture of 1860 times H2 and O2 gases in a volume of 1 liter of water.

Water electrolysis gas is called Brown gas or HHO gas since Yull Brown started research on energy field in earnest in 1977.

However, many people who study water electrolysis gases over-emphasize specificities such as ultra-efficiency or thermonuclear reactions that are not scientifically fully proven for such water electrolysis gases, so that instead of normal use of water electrolysis gases as energy, . ≪ / RTI >

The water electrolytic gas is a gas which is produced by the electrolysis of water and mixed with hydrogen and oxygen at a complete equivalent ratio of 2: 1, and is a completely non-polluting fuel which is reduced to a steam state after combustion. That is, carbon dioxide which is a warming gas or nitrogen oxide which is an acid gas is not generated.

In addition, the water electrolytic gas has a characteristic of completely burning in a very short time due to its own oxygen even if it does not supply air serving as an oxidizer like existing fossil fuel because hydrogen and oxygen have a condition of complete combustion of 2: 1. In addition, since there is no nitrogen which is essential for the oxidizing agent such as air and which does not help the reaction, the heating ability for the product generated in the combustion is three times as large as that of the gasoline combustion by the air. Therefore, the electrolytic gas is utilized as a useful tool in the welding field where the high temperature is required especially since the hot flame temperature is as high as 3000C.

The advantage of such a water electrolysis gas is that the hydrogen energy obtained by electrolysis of water is smaller than the energy used in electrolysis (60-80% efficiency), but it does not contain nitrogen as an oxidizing agent in burning, (Power = work / time) or the possibility of being a clean fuel is high in that it takes a long time to emit a large amount of energy in a short time.

In addition, the water electrolytic gas reacts with one molecule of hydrogen and one-half molecule of oxygen during combustion to produce one molecule of water, so that the number of moles of the product decreases compared to the number of moles of the reactant

In a special situation where the temperature is high and the expansion effect due to Bohr's Law is not conspicuous, the volume may be reduced, which may result in an impulsive characteristic.

 In addition, since the water electrolytic gas is completely premixed with hydrogen and oxygen at an equivalent ratio, not only the process of mixing the fuel and the oxygen in a turbulent manner is required but also the hydrogen molecule has a molecular diffusivity, It is very fast.

Therefore, the flame has a back-fire characteristic that burns in the direction of fuel supply.

In order to prevent such backflushing, it is necessary to increase the speed of the fuel jetted from the nozzle, so that the flame is inevitably formed by a very unstable pin point flame which advances a very long and long flame or is easily extinguished by a lift-off phenomenon . This feature is an obstacle to using water electrolysis gas more easily and practically.

In this way, the electrolytic gas, which can be mixed with hydrogen and oxygen by the electrolysis method, requires a new combustion method unlike the conventional burner or the combustion method because of the backlash or unstable characteristics of the flame.

The water electrolytic gas, which is generated by electrolysis of water and premixed with hydrogen and oxygen at an equivalence ratio, is explosively reacted to cause back-fire or flame lift-off. flammability of the fuel and oxidizer, and temperature control to prevent ignition.

A water electrolytic gas combustion apparatus for solving the above problems and demands have been studied by many engineers and researchers.

Patent Document 10-0367223 (Water electrolytic gas boiler, hereinafter referred to as prior art) relates to a water electrolytic gas boiler for using fuel of a gas boiler as a fuel instead of LPG or LNG as a water electrolytic gas, And a water electrolytic gas boiler equipped with a heating part and a circulating combustion chamber to which four characteristics of water electrolytic gas alone are applied in order to burn and generate decomposition gas.

It is an object of the present invention and an object of the present invention to provide an efficient use of water electrolysis gas using water vapor.

That is, the conventional water decomposition gas, the combustion device, and the prior art still have a problem of unstable flame in which back-fire or lift-off occurs, Fuel and a combustion system using the same.

In addition, conventional fossil fuels such as coal, oil, gasoline, diesel, kerosene, LNG, and LPG emit pollutants such as CO2, SOx, NOx and the like, Combustion system.

In order to solve the above problems and needs,

The present invention provides a combustion system comprising a water electrolytic gas generating device (200), a water vapor generating device (300), a gas mixing device (500), and a combustion device (400).

Further, the present invention provides a combustion system using mixed fuel obtained by mixing 100 parts by weight of water electrolytic gas with 1 to 1,000 parts by weight of steam.

The present invention also includes a water electrolytic gas generator 200, a water vapor generator 300, a gas mixing device 500, a fossil fuel supply device 100, a fuel mixing device 600, and a combustion device 400 And a combustion system.

Also, the present invention provides a combustion system using a mixed fuel composed of 1 to 1,000 parts by weight of a fossil fuel mixed with 100 parts by weight of a mixed fuel obtained by mixing 1 to 1,000 parts by weight of steam with 100 parts by weight of a water electrolytic gas .

Conventional technologies attempted to improve combustion efficiency and reduce pollutants by simply burning water electrolytic gas directly or with fossil fuel.

However, when the water vapor is not mixed, the amount of pollution-free electrolysis gas that can cope with the rapid increase of the flame temperature due to the rapid reaction of the water electrolytic gas and the excessive heating ability is absolutely restricted, do.

In this case, when the amount of the electrolytic gas is increased, the temperature rise is accelerated, and the problem of durability due to the generation and combustion of nitrogen oxides is further exacerbated.

Therefore, the mixed fuel of the water electrolytic gas and the water vapor according to the present invention, and the mixed fuel of the mixed gas and the fossil fuel and the combustion system therefor are very original, And to solve the problem.

If the effect of the present invention is illuminated from the viewpoint of combustion of conventional fossil fuels, conventional fossil fuels are a method of burning air (O2 + 3.76 N2) to fossil fuels, while the combustion method of the present invention is a method of water- (H2O vapor) is mixed with the gas (H2 + 1/2 O2), and the combustion gas is generated in proportion to the amount of the mixture of the water electrolytic gas and the water vapor and the generation of the acid gas by the nitrogen oxide (NOx) The generation of warming gas is controlled by source.

In addition, there is a coal-water slurry combustion technology that mixes liquid phases in conventional fossil fuels in comparison. The purpose of mixing and burning the water in the form of droplets is convenient for transportation and supply, and when the liquid water vaporizes, the mixture effect is enhanced by the strong volumetric expansion and the nitrogen oxide is reduced by the flame temperature lowering due to the heat of vaporization of water .

However, this method not only affects the stable formation of the flame due to the cooling down of the strong vaporization heat of water, but also the volumetric expansion effect due to the vaporization is a technique that is not continuously used because of negative factors such as a decrease in swirl force. Technology.

Therefore, it is judged that the water electrolytic gas and water vapor are different qualitatively from the technique of fusing with fossil fuel as in the case of the present invention.

In summary, the mixed fuel, mixed-composition fuel, and combustion system according to the present invention has the effect of providing an unstable and explosive electrolysis gas as a highly stable mixed fuel by mixing the water electrolytic gas, which is a clean fuel, with water vapor, By mixing and burning fuel, it is possible to significantly reduce pollutants such as CO2, NOx, SOx and the like which are problems of fossil fuel in proportion to the decrease of the amount of fossil fuel.

In addition, when a mixed-type fuel and combustion system according to the present invention is used to completely incinerate a refrigerant such as Freon with excess air, a large amount of water vapor introduced in the present invention is discharged through a deacon reaction It converts toxic fluorine or chlorine gas into less toxic hydrofluoric acid or hydrochloric acid.

[Deacon Reaction]

H2O + Cl2 = 2 HCl + 1 / 2O2

       Chlorine gas hydrochloric acid

H2O + F2 = 2 HF + 1/2 O2

Intoxicated fluorine gas Foshan

BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 shows a combustion system for a mixed fuel in which water electrolytic gas and water vapor are mixed according to the present invention. FIG.
FIG. 2 is a schematic diagram of a combustion system for a mixed composition fuel in which water electrolytic gas, water vapor and fossil fuel are mixed according to the present invention.
3 is a conceptual diagram of a steam generator according to the present invention;
4 is a conceptual view of a gas mixing apparatus according to the present invention.
5 is a conceptual view of a fuel mixing apparatus according to the present invention.
FIG. 6A is an external view of a combustion furnace burner for a cement kiln for computational analysis experiments according to the present invention. FIG.
FIG. 6b is a graph showing a grid (376,000 mesh) of a burner furnace burner for cement drying for the computational analysis experiment according to the present invention.
Fig. 6c is a schematic view of a combustion furnace burner for a cement kiln for computational analysis experiments according to the present invention. Fig.
FIG. 7a is a graph showing the degree of flame of 100% LNG fuel in the computer simulation according to the present invention.
FIG. 7B is a diagram showing a partial flame distribution diagram (combustion temperature of 1,122 degrees Celsius of average exhaust gas temperature) at the front, middle, and exit positions of 100% LNG fuel in the computer analysis experiment according to the present invention.
Figure 7c is a computed three-dimensional (3-D) velocity vector plot for 100% LNG fuel in a computational analysis experiment according to the present invention.
FIG. 8A is a graph showing the relationship between a mixed fuel (1: 1) of 100% LNG fuel, water electrolytic gas and water vapor, a mixed fuel of water electrolytic gas and water vapor (1: 2) is a comparison of calculated temperature distributions.
FIG. 8B is a graph showing the relationship between a mixed fuel (1: 1) of 100% LNG fuel, water electrolytic gas and water vapor, a mixed fuel of water electrolytic gas and water vapor (1: 2). Fig.

Hereinafter, the present invention will be described in detail with reference to the drawings.

The present invention provides a combustion system comprising a water electrolytic gas generating device (200), a water vapor generating device (300), a gas mixing device (500), and a combustion device (400).

The present invention also includes a water electrolytic gas generator 200, a water vapor generator 300, a gas mixing device 500, a fossil fuel supply device 100, a fuel mixing device 600, and a combustion device 400 And a combustion system.

The water electrolytic gas generator 200 of the present invention means a conventional water electrolytic gas generator or means for generating hydrogen and oxygen gas by decomposing water.

Thus, the water electrolytic gas generator generates water electrolytic gas by decomposing water.

The steam generator of the present invention means a device that generates steam by using ordinary heat energy or ultrasonic energy.

3, the water vapor generator 300 includes a water dissociation unit 310, a water storage space 320, a water inlet 330, and a water vapor outlet 340.

The water dissociating means 310 refers to a heater or the like, but is a concept including an apparatus or means for activating and vaporizing water molecules such as ultrasonic waves.

It is needless to say that the steam generator may include a control unit 350 and a valve for controlling the steam pressure and the steam pressure.

The present invention transfers the water vapor generated in the water vapor generating device to the gas mixing device 500 which mixes the water vapor generated in the water electrolytic gas generating device with the water electrolytic gas.

The gas mixing apparatus of the present invention means an apparatus or means for mixing a water electrolytic gas and water vapor into a combustion apparatus.

4, the gas mixing apparatus 500 of the present invention includes a mixing space 520, a water electrolysis gas inflow adjusting unit 210, a steam inflow adjusting unit 220, and a mixed fuel injection adjusting unit 510 .

The mixing space part 520 may be provided with a conventional structure or apparatus for mixing the water electrolytic gas and the water vapor into a space where they are mixed.

The water electrolytic gas inflow adjusting unit 210 may include a gas adjusting valve 211 as an apparatus or means for adjusting the amount and speed of the incoming water electrolytic gas.

Also, the steam inflow control unit 220 may be equipped with a steam control valve 311 as an apparatus or means for controlling the amount and speed of the incoming steam.

In addition, the mixed fuel injection regulator 510 may be provided with an injection regulating valve 511 as an apparatus or means for regulating the amount and speed of the mixed fuel supplied to the combustion apparatus 400.

The mixed fuel of the water electrolytic gas and the water vapor is supplied to the combustion apparatus described above.

The above combustion apparatus 400 is a concept including a water electrolytic gas combustion apparatus or a boiler for burning solid, liquid, and gaseous fuels, an internal combustion engine using gasoline, diesel, or the like.

Therefore, among the combustion apparatuses of the present invention, the boiler is consistently provided with a combustion furnace, an air conditioning unit, an exhaust gas discharge unit, and the like provided in a conventional boiler.

Further, among the combustion apparatuses of the present invention, the internal combustion engine is consistently provided with an ignition device, cylinder, etc., provided in a conventional internal combustion engine.

The combustion apparatus using the mixed water of the water electrolytic gas and the water vapor of the present invention is suitable for a water electrolytic gas combustion apparatus.

The present invention has a technical feature in the configuration of the mixed fuel injected into the above combustion system.

The mixing ratio of the water electrolytic gas and the water vapor is such that mixed fuel containing 1 to 1,000 parts by weight of water vapor is injected into 100 parts by weight of the water electrolytic gas.

Preferably, 50 to 200 parts by weight of water vapor is mixed with 100 parts by weight of water electrolytic gas, and more preferably 80 to 120 parts by weight of water vapor is mixed with 100 parts by weight of water electrolytic gas.

The present invention provides a combustion system for a mixed fuel in which water electrolytic gas including water vapor is mixed with water vapor comprising the above structure.

The present invention provides a combustion system for burning mixed composition fuel obtained by mixing fossil fuel with mixed fuel obtained by mixing water electrolytic gas and water vapor.

2B, the water electrolytic gas generator 200, the water vapor generator 300, the gas mixing apparatus 500, the fossil fuel supply apparatus 100, the fuel mixing apparatus 600, and the combustion apparatus 400, And a combustion system.

The water electrolytic gas generator 200, the water vapor generator 300, the gas mixer 500, and the combustion device 400 are as described above.

The fossil fuel supplying apparatus 100 refers to an apparatus or means for providing coal, petroleum, LNG, LPG, gasoline, diesel, kerosene, other biodiesel, waste gasification gas, etc., which are ordinary fossil fuels.

The fossil fuel of the present invention is a concept including coal, petroleum, LNG, LPG, gasoline, diesel, kerosene, other biodiesel and waste gasification gas.

The fuel mixing apparatus 600 according to the present invention is a fuel mixing apparatus for mixing the fossil fuels such as coal, petroleum, LNG, LPG, gasoline, diesel, kerosene, etc. and the mixed fuel composed of water electrolytic gas and water vapor Means a device or means for supplying the combustion apparatus 400.

5, the fuel mixing apparatus 600 includes a mixed composition space 620, a fossil fuel inflow control unit 110, a mixed fuel inflow control unit 530, and a mixed composition fuel injection control unit 610 .

The mixed composition space unit 520 refers to a space where the mixture of the water electrolytic gas and the water vapor is mixed with the fossil fuel.

In addition, the fossil fuel inflow control unit 110 may include a fossil fuel control valve 111 as an apparatus or means for controlling the amount and speed of the incoming fossil fuel.

Also, the mixed-fuel inflow adjusting unit 530 may be equipped with a mixed-fuel inflow control valve 531 as an apparatus or means for adjusting the amount and speed of the mixed fuel to be introduced.

The mixing composition fuel injection regulator 610 may be provided with an injection regulating valve 611 as an apparatus or means for regulating the amount and speed of the mixed composition fuel supplied to the combustion apparatus 400.

The present invention enables to control the amount and speed of the mixed composition fuel supplied to the combustion apparatus by the action of the fuel mixing apparatus described above.

The present invention provides a combustion system for burning mixed composition fuel obtained by mixing water electrolytic gas, steam, and fossil fuel having the above-described constitution.

The fuel to be supplied to the combustion system of the present invention is a mixed fuel composed of the water electrolytic gas, the water vapor and the fossil fuel as described above. The fuel is mixed with 100 parts by weight of the mixture of water electrolytic gas and water vapor, It is a technical feature that the fuel is a mixture of a mixture of parts by weight.

Preferably, 50 to 200 parts by weight of the fossil fuel is mixed with 100 parts by weight of the mixed fuel, and more preferably 80 to 120 parts by weight of the fossil fuel is mixed with 100 parts by weight of the mixed fuel.

The present invention provides a mixed composition fuel comprising water electrolytic gas, water vapor, and fossil fuel comprising the above structure and function, and a combustion system for burning the fuel.

The present invention was conceived through a computational analytical method for the mixed fuel and the method of combustion of the mixed fuel according to the invention as described above. As a result, compared with the conventional method of burning water electrolytic gas, It can be seen that there is a remarkable effect in terms of

1. Experimental Method

In the present invention, combustion characteristics of a conventional LNG fuel and combustion characteristics of a mixed fuel obtained by mixing a water electrolytic gas and water vapor are quantitatively investigated in a kiln type combustion furnace. In particular, the ratio of water electrolytic gas and water vapor is controlled Flame stability and flow characteristics were investigated.

2. Experimental apparatus for combustion characteristics

The characteristics of the burner and the furnace for the kiln for cement drying by the combustion characteristic test apparatus are shown in Figs. 6A to 6C.

3. Experimental results

(1) Combustion characteristics of LNG fuel and mixed fuel mixed with water electrolytic gas and water vapor were investigated quantitatively in a kiln type combustion furnace.

(2) Calculation conditions of LNG fuel are as shown in [Table 1] and the flame characteristics of LNG fuel are as described below.

Figure pat00001

FIGS. 7A and 7B are the results of numerical analysis of the internal heat flow of the combustion furnace when only LNG is injected as fuel. The fuel and air were injected by turning the primary fuel injection port and the primary air injection port, and the fuel injection port and the secondary air injection port were injected with fuel and air without turning.

The firing air was injected at a temperature of 220 ° C through the 16 nozzles at the edge with a combustion amount of 10,000 m 3 / hr. Swirl flow is usually used to achieve flame stability in intense combustion processes, the main effect of which is to shorten the flame length by forming a recirculation zone in the center of the furnace and rapid mixing. As a result of this calculation, these flame patterns are shown successfully. The maximum temperature of the combustion furnace was 1,642 ℃ and the mean temperature at the exit was 1,122 ℃.

Referring to the flow distribution shown in FIG. 7C, it can be seen that a recirculation zone is formed at the center of the combustion furnace (CTRZ) by the swirl effect in the vicinity of the burner. The average flow rate at the exit was about 15.94 m / s.

(3) Based on the results of the above calculation of LNG fuel, the characteristics of the flame varying by controlling the amount of water vapor and the amount of water vapor are examined to determine whether a stable flame can be obtained by mixing water electrolytic gas and water vapor. The characteristics of the water electrolytic gas and the steam collision flame were compared with the LNG flame.

Table 2 below gives the conditions used for variable studies. In the variable study, the reference flame was set as LNG flame (Case 1). Various methods can be used for comparison with such LNG flames. Specifically, for example, there is a method of equalizing the calorific value, and a method of controlling the flow rate and momentum of the nozzle may be used. However, if the amount of heat is the same, the temperature of the flame may be substantially different if the type of product and the number of moles differ.

Figure pat00002

Therefore, in this experiment, we first consider the heat value, the number of moles and the specific heat of the product (case 1) when the temperature of LNG flame (Case 1), water electrolysis gas and water vapor amount are mixed 1:

And the temperature of the flame was set to be similar. In case 3 and 4, the amount of water vapor to be mixed is controlled to observe the change of flame characteristics. But in all cases

In the central burner corresponding to the primary inlet, the amount of water electrolytic gas and water vapor was fixed to 1: 1, and the amount of water vapor to the water electrolytic gas in the secondary burner located around the primary inlet was doubled The characteristics of the flame and the change of the temperature were investigated. In the case of the LNG flame used in the above verification, firing air was used. However, in this case, no firing air was injected to observe the flame characteristics while excluding the effect of the firing air on the flame. Also, a sensible heat loss model was used for the wall.

(4) Experimental results

1) In Figure 8a, Case 1 (case 1) and Case 2 (Case 1), in which the combustion temperature is set to be similar to that of Case 1, were compared firstly (water electrolysis gas to water vapor ratio 1: 1).

In this case, the temperature of the outlet is 1594 ℃ for Case1 and 1588 ℃ for Case2.

However, the distribution of temperature inside the flame was found to be relatively wide and gentle in the case of LNG flame, whereas the flame temperature gradient was formed substantially in the case of fuel mixed with water vapor and water electrolysis gas.

This is because although the water electrolytic gas is mixed with water vapor, the water electrolytic gas itself is stoichiometrically totally premixed with hydrogen and oxygen. Therefore, the turbulent flow in which the reaction is determined by the mixing rate of the oxidant and the fuel , But it is considered that the reaction proceeded relatively quickly.

2) In FIG. 8b, the velocity fields for the above four cases are presented. In the case of LNG flames, it is evident that a strong central recirculation zone is formed by the swirling flow, but in the case of the water electrolytic gas and the steam mixture, the central swirling flow is not generated despite the same swirling intensity . This is presumably due to the effect of the initial flame expansion due to the rapid chemical reaction of the water electrolytic gas.

3) The above results show that pre-mixing of water electrolytic gas and water vapor makes it possible to control unstable combustion characteristics such as flame reversal and thin flame or flame lift-off while maintaining the function of clean fuel.

In addition, combustion characteristics of water electrolytic gas and water vapor mixed fuel were stable and physically consistent. Therefore, the mixed fuel of water electrolytic gas and water vapor suggests the potential as a clean fuel without emission of nitrogen oxides or other pollutants.

When a mixed-type fuel and a combustion system according to the present invention is used to completely incinerate a refrigerant such as Freon with excess air, a large amount of water vapor introduced in the present invention is highly toxic fluorine generated by a deacon reaction Or chlorine gas into less toxic hydrofluoric acid or hydrochloric acid.

The present invention provides a mixed fuel, a mixed composition fuel, and a combustion system using the same, wherein the structure, function, action, and effect described above are exhibited.

INDUSTRIAL APPLICABILITY The present invention is very useful for industries that produce, manufacture, sell, research, and distribute combustion devices such as boilers and internal combustion engines.

In particular, the present invention is very useful for an industry that produces, manufactures, sells, researches, and distributes fuel provided in a combustion apparatus such as a boiler, an internal combustion engine, or the like.

100: Fossil fuel supply device 200: Water electrolytic gas generator
300: steam generator 400: combustion device
500: gas mixing device 600: fuel mixing device
620: mixed composition space part 110: fossil fuel inflow control part
530: Mixed fuel inflow control unit 610: Mixed composition fuel injection control unit

Claims (4)

A water electrolytic gas generating device (200), a water vapor generating device (300), a gas mixing device (500), and a combustion device (400).
The method according to claim 1,
Wherein a mixed fuel obtained by mixing 100 parts by weight of water electrolytic gas with 1 to 1,000 parts by weight of water vapor is used.
A combustion system 400 including a water electrolytic gas generator 200, a water vapor generator 300, a gas mixing device 500, a fossil fuel supply device 100, a fuel mixing device 600, .
The method of claim 3,
Wherein 1 to 1,000 parts by weight of water vapor is mixed with 100 parts by weight of water electrolytic gas, and 1 to 1,000 parts by weight of fossil fuel is mixed with 100 parts by weight of mixed fuel.
KR1020140009580A 2014-01-27 2014-01-27 a combustion system using the mixture fuel of water electrolysis gas and water vapor, and a combustion system with this mixture blended fossil fuel KR20150089221A (en)

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KR102534915B1 (en) * 2022-04-26 2023-05-30 주식회사 헤즈 Engine combustion method and its system by the homogeneous mixing of ultra small amount of water electrolysis gas with combusting air
KR20230152194A (en) * 2022-04-26 2023-11-03 주식회사 헤즈 combustion air premixing device that mixes water electrolysis gas and air
CN117165343A (en) * 2023-03-13 2023-12-05 江苏与奏实业有限公司 Fuel mixed by water electrolysis gas and catalyst and turbine prime motor power generation system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102534915B1 (en) * 2022-04-26 2023-05-30 주식회사 헤즈 Engine combustion method and its system by the homogeneous mixing of ultra small amount of water electrolysis gas with combusting air
KR20230152194A (en) * 2022-04-26 2023-11-03 주식회사 헤즈 combustion air premixing device that mixes water electrolysis gas and air
CN117165343A (en) * 2023-03-13 2023-12-05 江苏与奏实业有限公司 Fuel mixed by water electrolysis gas and catalyst and turbine prime motor power generation system

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