WO2010101261A1

WO2010101261A1 - Device for generating mixed fuel gas using ion activity

Info

Publication number: WO2010101261A1
Application number: PCT/JP2010/053700
Authority: WO
Inventors: 伸雄高山; 正和石井; 信幸宮森; 哲実川原
Original assignee: 株式会社ワールドエネテック; 理建工業株式会社
Priority date: 2009-03-02
Filing date: 2010-03-01
Publication date: 2010-09-10
Also published as: JP2010203649A; JP5315092B2

Abstract

To increase the combustion efficiency of a fuel in a combustion device. An ionized liquid (H3O++OH-) obtained by electrolysis in an electrolysis tank (11) is vaporized via adsorption in a mixing tank (12) to form an ionized active gas (H3O+:OH-). In a reaction tank (13), a fuel material (M13) is reacted by using the ionization activity function of the aforesaid ionized active gas (H3O+:OH-) to generate a mixed fuel gas (W1) comprising the fuel material (M13) and oxygen. Thus, a device (1) for generating a mixed fuel gas using ion activity, whereby the fuel material (M13) can be efficiently combusted in a combustion device (2), can be obtained.

Description

Ion activated hybrid fuel gas generator

The present invention relates to a hybrid fuel gas generator using ionic activity, and in particular, enables fuel materials such as gasoline and LPG to be efficiently burned in a combustion device.

As a technique for efficiently burning fuel raw materials, a technique for mixing so-called oxyhydrogen flame gas, which is a mixed gas containing oxygen and hydrogen in a ratio of 1: 2, has been proposed (see Patent Document 1).

JP 2005-320416 A

In the fuel combustion method using this oxyhydrogen flame gas, it is difficult to stably control the combustion state of the fuel in the combustion apparatus, and particularly when the mixed fuel gas is mixed with the fuel raw material and combusted in the combustion apparatus, the condition is particularly high temperature and high pressure. Therefore, it is desirable to be able to generate a hybrid fuel gas that has the highest possible physical and chemical stability.
The present invention has been made in consideration of the above points, and an object of the present invention is to propose a hybrid fuel gas generator based on ion activity that can stably activate fuel even under low temperature and low pressure.
In order to solve this problem, in the present invention, a hybrid gas that supplies the combustion device 21 with a hybrid fuel gas W1 obtained by reacting an ionized active gas M11 (H ₃ O ⁺ : OH ⁻ ) with a fuel raw material to be combusted. An electrolysis tank unit 11 that generates an ion synthesis liquid M1 containing dissociated (H ₃ O ⁺ + OH ⁻ ) ions by electrolyzing an electrolysis stock solution 20, and an electrolysis tank By storing the ion synthesis solution M1 delivered from the unit 11 as the liquefied layer 32, (H ₃ O ⁺ ) ions and (OH ⁻ ) from the ion synthesis solution M1 containing dissociated (H ₃ O ⁺ + OH ⁻ ) ions are stored. ) ionizing activators gas and ions are adsorbed _{^{^{(H 3 O +: OH -}}} ) and the mixing tank 12 to vaporize, ionizing activators gas delivered from the mixing tank 12 (H3O : OH @ -) by reacting the fuel feedstock using ion activity function of the ionized inert gas receiving, providing a reactor tank section 13 for generating a hybrid fuel gas W1 supplied to the combustor 2.
According to the present invention, the ion synthesis liquid (H ₃ O ⁺ + OH ⁻ ) generated by the electrolysis treatment in the electrolysis tank part is vaporized by being adsorbed in the mixing tank part to be ionized active gas (H ₃ O ^+). : OH ⁻ ), and the fuel raw material is reacted in the reaction tank section using the ion activation action of the ionized active gas (H ₃ O ⁺ : OH ⁻ ), thereby generating a hybrid fuel gas containing oxygen. By doing so, it is possible to realize a hybrid fuel gas generating device based on ion activity that can stably and efficiently burn fuel in the combustion device.

FIG. 1 is a schematic block diagram showing a hybrid fuel gas generator using ion activity according to an embodiment of the present invention.
FIG. 2 is a schematic block diagram showing a detailed configuration of the electrolysis tank unit 11 of FIG.
FIG. 3 is a schematic block diagram showing a detailed configuration of the mixing tank section 12 of FIG.
FIG. 4 is a schematic block diagram showing a detailed configuration of the reaction tank unit 13 of FIG.
FIG. 5 is a schematic diagram for explaining the ion transfer operation in the electrolysis tank unit 11 of FIG. 1.
FIG. 6 is a schematic diagram for explaining the ion transfer operation in the mixing vessel 12 of FIG.
FIG. 7 is a schematic diagram for explaining the ion transfer operation in the reaction vessel 13 of FIG.
FIG. 8 is a schematic diagram for explaining the ion transfer operation in the reaction tank section 13 of the second embodiment.
FIG. 9 is a schematic block diagram showing a hybrid fuel gas generator using ion activity according to another embodiment.

Hereinafter, an embodiment of the present invention will be described in detail with reference to the drawings.
(1) Overall Configuration In FIG. 1, reference numeral 1 denotes a hybrid fuel gas generator using ion activity as a whole, and the generated hybrid fuel gas W1 is supplied to the combustion device 2 from the output port P1.
The hybrid fuel gas generator 1 includes an electrolysis tank unit 11, a mixing tank unit 12, and a reaction tank unit 13.
(2) Electrolysis tank section As shown in FIG. 2, the electrolysis tank section 11 is placed in an electrolysis tank body 21 containing potassium hydroxide (KOH) having a concentration of 30% as a stock solution 20 for electrolysis. By connecting an electrolysis power source 25 to the anode terminal 24A and the cathode terminal 24B derived from both ends of a plurality of, for example, 111 electrode plate layers 22 that are provided, Formula KOH → K ⁺ + OH ⁻ (1)
Produces a large amount of potassium ions (K ⁺ ) and hydroxyl ions (OH ⁻ ).
In the case of this embodiment, each electrode of the laminated electrode plate layer 22 is “SUS316”, and when a voltage exceeding the critical voltage is applied between both surfaces, cations and anions are eluted in the electrolysis stock solution 20. By doing so, an electric field for electrolyzing the stock solution 20 for electrolysis is formed between adjacent electrodes.
The electrolysis action in the electrolysis tank main body 21 is further expressed with respect to the hydroxyl ion (OH ⁻ ) by the following formula: OH ⁻ → H ⁺ + O ⁻⁻ (2)
Thus, hydrogen ions (H ⁺ ) and oxygen ions (O ⁻⁻ ) are electrolyzed.
In the electrolysis state in the electrolysis tank body 21, the following formula 4H ⁺ + 2O ⁻⁻ → 2H ₂ O (3)
As shown in FIG. 4, water molecules (2H ₂ O) are generated by normal bonding of four hydrogen ions (4H ⁺ ) and two oxygen ions (2O ⁻⁻ ), or the water molecules ( 2H ₂ O) is represented by the following formula 2H ₂ O = H ₃ O ⁺ + OH ⁻ (4)
As described above, there is also an effect that the oxonium ion (H ₃ O ⁺ ) and the hydroxyl ion (OH ⁻ ) are generated by further electrolysis.
Thus, in the inside of the electrolysis tank body 21 of the electrolysis tank section 11, various molecules are separated into a plurality of ions by electrolysis or form regular bonds, but in particular, hydroxyl ions (OH ⁻ 5), as shown in FIG. 5, two water molecules (2H ₂ O) are electrolyzed to generate oxonium ions (H ₃ O ⁺ ) and hydroxyl ions ( OH ⁻ ) and the coexistence of both in a dissociated bond state (H ₃ O ⁺ + OH ⁻ ).
These operations are generally performed reversibly. However, by selecting a voltage of 200 [V] and a current of 75 [A] as a power source from the electrolysis power source 25 for the electrolysis tank body 21, the above-described operation is performed. The progression of the oxonium ion (H ₃ O ⁺ ) and the hydroxyl ion (OH ⁻ ) to the dissociative bond state according to the formula (4) occurs most remarkably (this is called a resonance state).
Thus, in a state where the electrolysis tank unit 11 maintains the resonance condition, the oxonium ion (H ₃ O ⁺ ) and the hydroxyl ion (OH ⁻ ) together with the potassium ion (K ⁺ ) and the water molecule (2H ₂ O). An electrolysis solution M1 containing an ion synthesis solution (H ₃ O ⁺ + OH ⁻ ) formed by dissociating and is sent from the output port P11 provided in the electrolysis tank section 11 to the outside through the output valve V11. It is supplied to the input port P12 of the electrolyzed liquid circulation unit 26 through the input valve V12.
The electrolytic solution circulating unit 26 includes a circulation pump 27, and the electrolytic solution M1 supplied from the electrolytic cell unit 11 is circulated through the pure water filter 28 from the output port P13 through the output valve V13. It pushes out to the input port P14 of the mixing tank part 12 as the decomposition liquid M2.
(3) Mixing tank part The mixing tank part 12 stores the supplied electrolysis solution M2 for circulation as a liquefied layer 32 in the lower layer part of the mixing tank main body 31, as shown in FIG.
Thus, the electrolyzed liquid containing the ion synthesis liquid (H ₃ O ⁺ + OH ⁻ ) stored as the liquefied layer 32 is electrolyzed and returned from the stored electrolyzed liquid circulation port P15 of the mixing tank section 12 through the output valve V14. M3 is sent back to the circulation input port P16 of the electrolysis tank section 11.
Thus, the circulation pump 27 of the electrolytic solution circulation unit 26 supplies the electrolytic solution obtained from the electrolytic cell main body 21 of the electrolytic solution tank unit 11 to the output port P11-output valve V11-input valve V12 of the electrolytic solution circulation unit 26. -Input port P12-Circulation pump 27-Filter 28 for pure water-Output port P13-Output valve V13-Input port P14 of the mixing tank section 12-Liquefied layer 32 of the mixing tank section 12-Retained electrolyzed liquid circulation port P15-Output The valve V14 is circulated through a circulation input port P16 of the electrolysis tank unit 11 and a circulation loop of the electrolysis tank unit 11.
The liquid level of the liquid level 32A of the electrolytic solution M2 stored in the liquefied layer 32 of the mixing tank unit 12 is detected by the liquid level detector 33, and the liquid level detection signal S1 is the center of the hybrid fuel gas generator 1. It is transmitted to the control device unit 34.
The central control unit 34 provides the water supply valve V29 with a liquid level control signal S2 that sets the liquid level 32A of the liquefied layer 32 to a predetermined reference liquid level based on the liquid amount detection signal S1, thereby the liquefied layer 32. When the liquid level 32A falls below the reference liquid level, the water supply valve V29 is opened and the pure water M5 is replenished to the temperature liquid level control input port P28 via the input valve V26 of the mixing tank section 12, thereby the liquefied layer 32. The liquid level 32A is always kept at the reference liquid level.
In the case of this embodiment, a viewing window 33A is provided at the position of the liquid level 32A of the mixing tank section 12, so that the operator can visually check the liquid level of the liquid level 32A of the liquefied layer 32. .
The mixing tank unit 12 stores the electrolytic solution M2 pushed out from the electrolytic solution circulating unit 26 to form a liquefied layer 32 and an ion synthesis solution (H ₃ O ⁺ + OH ⁻ constituting the liquefied layer 32). ) Is sent from the constant temperature control output port P25 to the input port P26 of the temperature adjustment unit 35 via the output valve V25, and the temperature-adjusted electrolysis solution obtained at the output port P27 is output. The temperature is returned to the temperature liquid level control input port P28 of the mixing vessel 12 through the valve V27 and the input valve V26.
The mixing tank unit 12 is provided with a temperature detector 36 for detecting the temperature of the electrolyzed liquid constituting the liquefied layer 32, and transmits the temperature detection signal S11 to the central controller unit 34 (FIG. 2).
Based on the temperature detection signal S11, the central control unit 34 sends back to the temperature adjustment unit 35 a temperature control signal S12 that brings the electrolysis solution of the liquefied layer 32 to a predetermined reaction temperature. The temperature is adjusted to a predetermined reaction temperature (for example, 20 to 22 [° C.]) set in the central control unit 34.
Thus, the mixing tank unit 12 maintains the temperature of the electrolyzed liquid stored in the liquefied layer 32 at a predetermined reaction temperature, whereby the electrolyzed liquid stored in the liquefied layer 32 is converted into the electrolyzed liquid stored in the liquefied layer 32 as shown in FIG. Oxonium ions (H ₃ O ⁺ ) and hydroxyl ions (OH) are generated from the ion synthesis solution (H ₃ O ⁺ + OH ⁻ ) by causing an ion transfer effect on the contained ion synthesis solution (H ₃ O ⁺ + OH ⁻ ). ^- )), And the ionized active gas (H3O +: OH-) composed of adsorbed molecules in which the separated oxonium ions (H ₃ O ⁺ ) and hydroxyl ions (OH ⁻ ) are adsorbed by ionic charges. Create conditions that allow state to coexist.
Thus, when the ionized active gas (H ₃ O ⁺ : OH ⁻ ) is generated in the liquefied layer 32, the mixing tank unit 12 becomes a gas bubble in the liquefied layer 32 due to the generation of the ionized active gas (H ₃ O ⁺ : OH ⁻ ). Jump out to the.
Thus, a state in which the ionized active gas (H ₃ O ⁺ : OH ⁻ ) in which the oxonium ions (H ₃ O ⁺ ) and the hydroxyl ions (OH ⁻ ) are adsorbed is generated is obtained in the vaporized layer 41 ( This is sent as an ionized active gas M11 from the ionized active gas output port P31 to the pressure adjusting unit 42 via the output valve V31.
When the ionized active gas (H ₃ O ⁺ : OH ⁻ ) is generated in the vaporized layer 41, the pressure adjusting unit 42 immediately draws it and optimizes the pressure of the ionized active gas M 11 in the reaction tank unit 13. It adjusts to a value and gives to the ionization active gas input intermediate port P32 (FIG. 4) of the reaction tank part 13 as adjustment pressure ionization active gas M12.
In the case of this embodiment, when the concentration of the ionized active gas (H ₃ O ⁺ : OH ⁻ ) in the vaporization layer 41 increases, the mutual protection action cannot be performed, and the ionized active gas (H ₃ O ⁺ : OH ⁻ ) As a result, a phenomenon occurs in which the component of 縮 contracts and returns to the component of water (2H ₂ O).
(4) Reaction tank section In FIG. 4, the ionized active gas input intermediate port P32 is provided at a higher level position than the ionized active gas input port P33 provided at a low position of the reaction tank section 13. The adjusted pressure ionized active gas M12 is temporarily lowered from the high level position of the ionized active gas input intermediate port P32 to the low level position of the ionized active gas input port P33 and supplied to the reaction tank section 13.
Similar to the method of supplying the regulated pressure ionized active gas M12 to the reaction tank unit 13, the fuel raw material M13 made of gasoline as a combustion target is received by the fuel raw material input intermediate port P35 at the high level position via the output valve V35. At the same time, the fuel raw material M13 is taken in from a fuel raw material input port P36 provided in the lower part of the reaction tank section 13.
As a result, while the regulated pressure ionized active gas introduced from the ionized active gas input port P33 passes through the fuel raw material 45 stored in the lower half of the reaction tank 13 using the negative pressure, the fuel By reacting with the raw material 45, a hybrid fuel gas 46 is generated on the liquid surface 47 of the fuel raw material 45.
The reaction tank unit 13 is provided with a viewing window 48 for an operator to visually check the liquid level of the liquid surface 47.
As shown in FIG. 7, the reaction tank unit 13 has ions of oxonium ions (H ₃ O ⁺ ) and hydroxyl ions (OH ⁻ ) that are ionized active gases with respect to gasoline (C ₆ H ₁₄ ) that is a fuel raw material. A reaction that reversibly generates oxooptane (C ₆ H ₁₈ O ₂ ) is caused by the transfer action.
This reaction is actively performed at a low pressure (0.1 [MPa]), and the pressure adjustment unit 42 adjusts the pressure.
Thus, the oxooptane (C ₆ H ₁₈ O ₂ ) generated by the ion transfer operation in the reaction tank section 13 is output from the hybrid fuel output port P37 through the output valve V37 to the output port P1 of the hybrid fuel gas generator 1 by ion activity. To the combustion device 2 as a hybrid fuel gas W1.
(5) Hybrid fuel gas generation operation In the above configuration, potassium hydroxide (KOH) put in the electrolysis tank 11 as the electrolysis stock solution 20 is supplied from the electrolysis power source 25 to the anode terminal 24A and the cathode terminal 24B. By the action of the applied voltage / current, as shown in the formulas (1) to (4), the hydroxyl ion (OH ⁻ ) undergoes an electrolysis action, so that as shown in FIG. A molecule (2H ₂ O) is generated by normal binding action.
The water molecules (2H ₂ O) are reversibly decomposed into oxonium ions (H ₃ O ⁺ ) and hydroxyl ions (OH ⁻ ) in the electrolysis tank section 11 by the separation action by electrolysis. An ion synthesis solution (H ₃ O ⁺ + OH ⁻ ) is reversibly generated by the dissociative binding action by the electric attractive force of ions.
These normal binding action, separation action and dissociative binding action occur simultaneously and thus molecules of potassium ion (K ⁺ ), oxonium ion (H ₃ O ⁺ ), hydroxyl ion (OH ⁻ ) and water. The electrolytic solution M1 containing (2H ₂ O) is drawn from the output port P11 of the electrolytic tank unit 11 by the circulation pump 27 of the electrolytic solution circulating unit 26, and the input port P14 of the mixing tank unit 12 and the stored electrolytic solution. It is circulated through the circulation port P15 to the circulation input port P16 of the electrolysis tank section 11.
In the circulation operation of the electrolysis solution, the amount of ion synthesis solution (H ₃ O ⁺ + OH ⁻ ) contained in the electrolysis solution is determined from the electrolysis power supply 25 based on the electrolysis conditions of the electrolysis tank 11. When the direct current / voltage applied between the anode terminal 24A and the cathode terminal 24B has a predetermined resonance value (in this embodiment, the applied voltage is 200 [V] and the applied current is 75 [A]), the resonance action is achieved. As a result, the production amount of the ion synthesis solution (H ₃ O ⁺ + OH ⁻ ) becomes remarkably large.
In this way, the ion synthesis liquid (H ₃ O ⁺ + OH ⁻ ) contained in the electrolysis liquid M1 drawn from the electrolysis tank section 11 passes through the lower layer of the mixing tank section 12 and the electrolysis tank section 11. The ion synthesis solution (H ₃ O ⁺ + OH ⁻ ) is partly stored as a liquefied layer 32 in the lower layer portion of the mixing tank 12 due to the pushing pressure of the circulation pump 27.
The liquefying layer 32 of the mixing tank unit 12 stores an electrolysis solution containing an ion synthesis solution (H ₃ O ⁺ + OH ⁻ ) in a stagnant state and also stores the stored ion synthesis solution (H ₃ O ⁺ + OH ⁻ ). Is extracted from the constant temperature control output port P25, controlled to a predetermined reaction temperature in the temperature adjustment unit 35, and then subjected to ion synthesis stored in the liquefied layer 32 under a temperature adjustment operation to return to the temperature liquid level control input port P28. The liquid (H ₃ O ⁺ + OH ⁻ ) is subjected to an ion exchange action as shown in FIG.
The ion transfer function in the mixing tank 12 is to reversibly separate the ion synthesis solution (H ₃ O ⁺ + OH ⁻ ) into oxonium ions (H ₃ O ⁺ ) and hydroxyl ions (OH ⁻ ) and to perform the separation. When the formed oxonium ions (H ₃ O ⁺ ) and hydroxyl ions (OH ⁻ ) are integrated by the adsorption action, the ionized active gas (H ₃ O ⁺ : OH ^{− is obtained} from the liquid surface 32A of the liquefied layer 32 by the mutual protection action. Vaporize as).
The ion transfer operation in the mixing tank unit 12 according to FIG. 6 is performed simultaneously and reversibly. However, depending on the temperature setting condition (20 to 22 [° C. in this embodiment) by the temperature adjusting unit 35, oxonium is provided. The transition action to the ionized active gas (H ₃ O ⁺ : OH ⁻ ), which is an adsorbed molecule of ions (H ₃ O ⁺ ) and hydroxyl ions (OH ⁻ ), becomes remarkable.
Thus, the ionized active gas (H ₃ O ⁺ : OH ⁻ ) vaporized from the liquefied layer 32 comes out to the vaporized layer 41 of the mixing tank unit 12.
At this time, the ion synthesis liquid (H ₃ O ⁺ + OH ⁻ ) vaporized from the liquefied layer 32 to the vaporized layer 41 is consumed from the electrolyzed liquid circulating between the electrolyzed tank part 11 and the mixing tank part 12, The concentration of potassium hydroxide (KOH), which is an electrolysis stock solution in the electrolysis tank unit 11, increases. At this time, the central control unit 34 determines the water supply valve based on the liquid level detection signal S 1 of the liquid level detector 33. By supplying the liquid level control signal S2 to V29, the pure water M5 is supplied to the mixing tank 12 through the temperature liquid level control input port P28, thereby controlling the liquid level 32A of the liquefied layer 32 to a predetermined constant value. At the same time, by circulating the ion synthesis solution (H ₃ O ⁺ + OH ⁻ ) in the liquefied layer 32 to the electrolysis tank unit 11, the concentration of the electrolysis stock solution (KOH) in the electrolysis tank unit 11 is kept constant. Control
In this way, the ionized active gas (H ₃ O ⁺ : OH ⁻ ) filling the vaporized layer 41 is sent from the mixing tank unit 12 to the reaction tank unit 13 via the pressure adjusting unit 42 from the ionized active gas input port P33. It is.
The reaction tank unit 13 reacts the fed regulated pressure ionized active gas M12 with the fuel material M13 (gasoline (C ₆ H ₁₄ ) in this embodiment) fed from the fuel material input port P36. The ion exchange effect shown in FIG. 7 is produced.
As a result, the reaction tank section 13 is activated by ionizing gasoline (C ₆ H ₁₄ ), which is a normal fuel raw material that is not activated by itself, by ionizing the oxonium ions (H ₃ O ⁺ ) And an ionized active gas (H ₃ O ⁺ : OH ⁻ ) composed of adsorbed molecules of hydroxyl ions (OH ⁻ ), under low pressure (maximum 0.1 MPa in this embodiment), By causing an active reaction, oxooptane (C ₆ H ₁₈ O ₂ ) can be generated and supplied to the combustion device 2.
The oxo-optane (C ₆ H ₁₈ O ₂ ) contains oxygen atoms (O ₂ ) compared to gasoline (C ₆ H ₁₄ ), so that the combustion efficiency in the combustion device 2 is reduced to that of ordinary gasoline (C ₆ H ₁₄ ) and can be made much higher.
According to the above configuration, by using the ionization activation function of the ionization active gas (H ₃ O ⁺ : OH ⁻ ), normal binding reaction is performed with gasoline (C ₆ H ₁₄ ) as a fuel raw material for burning oxygen. Thus, it is possible to obtain a hybrid fuel gas by ion activity that can be burned efficiently.
Accordingly, the reaction conditions for reacting the ionized active gas (H ₃ O ⁺ : OH ⁻ ) with gasoline (C ₆ H ₁₄ ) as a fuel can be stabilized at a low temperature and a low pressure.
(6) Second Embodiment FIG. 8 shows a second embodiment. In the case of FIG. 7, gasoline (C ₆ H ₁₄ ) is used as the fuel raw material M13, but in the case of FIG. Instead of this, LPG (C ₃ H ₈ ) is used as the fuel raw material M13 to be supplied to the reaction tank section 13.
In this case, the reaction tank unit 13 reacts the ionized active gas (H ₃ O ⁺ : OH ⁻ ) with LPG (C ₃ H ₈ ) to produce 1-N propanol (CH ₃ —OH—) as the hybrid fuel gas W1. (CH ₂ -CH ₂ ) is generated and sent from the hybrid fuel output port P37 to the combustion device 2 via the output valve V37.
According to the configuration of FIG. 8, ionized active gas (H ₃ O ⁺ : OH ⁻ ) composed of adsorbed molecules of ionized oxonium ions (H ₃ O ⁺ ) and hydroxyl ions (OH ⁻ ) is converted into LPG (C ₃ By reacting with H ₈ ), the ionized active gas (H ₃ O ⁺ : OH ⁻ ) is ion-activated, and compared with LPG (C ₃ H ₈ ), which is the original fuel material. Therefore, the combustion efficiency when the combustion apparatus 2 burns 1-Npropanol (CH ₃ —OH—CH ₂ —CH ₂ ), which is the hybrid fuel gas, is further increased. be able to.
Thus, by using the ionization active function of the ionized active gas (H ₃ O ⁺ : OH ⁻ ), a normal bond reaction with LPG (C ₃ H ₈ ) as a fuel to be burned with oxygen makes it possible to efficiently burn the hybrid. Fuel can be obtained.
Accordingly, the reaction conditions for reacting the ionized active gas (H ₃ O ⁺ : OH ⁻ ) with LPG (C ₃ H ₈ ) as a fuel can be stabilized at a low temperature and a low pressure.
(7) Other Embodiments (7-1) In the above-described embodiment, the case where gasoline (C ₆ H ₁₄ ) and LPG (C ₃ H ₈ ) are used as the fuel raw material to be combusted has been described. However, the fuel is not limited to this, and fuel containing hydrocarbons such as ethanol and methanol may be used.
(7-2) FIG. 9 shows a hybrid fuel gas generator 1X based on ion activity according to another embodiment. As shown in FIG. 26X is inserted into the flow path of the electrolysis return liquid M3 from the mixing tank section 12 to the electrolysis tank section 11, so that the liquefied layer 32 of the liquefied layer 32 can be supplied from the stored electrolytic solution circulation port P15 (FIG. 3) of the mixing tank section 12. The ion synthesis solution (H ₃ O ⁺ + OH ⁻ ) is drawn out as a circulating solution and pushed out to the circulation input port P16 (FIG. 2) of the electrolysis tank section 11.
Even in this case, the mixing tank section 12 can be generated from the electrolysis tank section 11 through the liquefied layer 32 of the mixing tank section 12 and returning to the electrolysis tank section 11, as described above with reference to FIG. The vaporization phenomenon of the ionized active gas (H ₃ O ⁺ : OH ⁻ ) based on the mutual protection action can be generated from the ion synthesis solution (H ₃ O ⁺ + OH ⁻ ) stored in the inside.
(7-3) In the above-described embodiment, the case where (KOH) is used as the electrolysis stock solution 20 of the electrolysis tank unit 11 has been described, but instead of this, an aqueous Li solution, (NaOH), citric acid An aqueous solution may be used.

The present invention is ionized active gas _{^{(+ H 3 O: OH -}} ) and available combustion device for combusting the fuel material to be reacted.

DESCRIPTION OF SYMBOLS 1, 1X ... Hybrid fuel gas generator by ion activity, 2 ... Combustion device, 11 ... Electrolysis tank part, 12 ... Mixing tank part, 13 ... Reaction tank part, 20 ... Electrolysis stock solution, 21... Electrolysis tank body, 22... Electrode plate layer, 24 A, 24 B... Anode, cathode terminal, 25. Power source for electrolysis, 26 and 26 X. 28 …… Pure water filter, 31 …… Mixing tank body, 32 …… Liquefaction layer, 33 …… Liquid quantity detector, 34 …… Central control unit, 35 …… Temperature adjustment unit, 36 …… Temperature detector , 41 ... vaporization layer, 42 ... pressure adjustment part

Claims

A hybrid fuel gas generator by ionic activity for supplying a hybrid fuel gas obtained by reacting an ionized active gas to a fuel to be burned to a combustion device,
An electrolysis tank unit that generates an ion synthesis solution containing dissociated (H 3 O + + OH − ) ions by electrolyzing the stock solution for electrolysis;
By storing the ion synthesis solution delivered from the electrolysis tank section as a liquefied layer, (H 3 O + ) ions (from the ion synthesis solution containing dissociated (H 3 O + + OH − ) ions) and ( A mixing vessel for vaporizing an ionized active gas (H 3 O + : OH − ) formed by adsorption of OH − ) ions;
A hybrid supplied to the combustion device by receiving the ionized active gas (H 3 O + : OH − ) delivered from the mixing tank unit and reacting with the fuel using the ionization active function of the ionized active gas. A hybrid fuel gas generator using ionic activity, comprising: a reaction tank that generates fuel gas.
The electrolysis solution circulation part which circulates the ion synthesis liquid generated in the electrolysis tank part through the mixing tank part to the electrolysis tank part using a circulation pump. 2. A hybrid fuel gas generator using ionic activity according to 1.
The temperature of the ion synthesis solution stored as a liquefied layer in the mixing vessel is vaporized from (H 3 O + + OH − ) ions of the ion synthesis solution to ionized active gas (H 3 O + : OH − ). The hybrid fuel gas generator using ion activity according to claim 1, further comprising a temperature adjusting unit that maintains the temperature.
The pressure of the ionized active gas (H 3 O + : OH − ) generated in the mixing tank part is the pressure at which the ionized active gas (H 3 O + : OH − ) reacts with the fuel in the reaction tank part. The hybrid fuel gas generator using ion activity according to claim 1, further comprising: a pressure adjusting unit that adjusts to
A hybrid fuel gas generation method based on ion activity that supplies a hybrid fuel gas obtained by reacting an ionized active gas to a fuel to be burned to a combustion device,
Generating an ion synthesis solution containing dissociated (H 3 O + + OH − ) ions by electrolyzing the stock solution for electrolysis in the electrolysis tank unit;
In the mixing tank part, by storing the ion synthesis liquid delivered from the electrolysis tank part as a liquefied layer, the ion synthesis liquid containing (H 3 O + + OH − ) ions that have been dissociated and bonded (H 3 O A step of vaporizing an ionized active gas (H 3 O + : OH − ) formed by adsorbing ( + ) ions and (OH − ) ions;
The combustion is performed by receiving the ionized active gas (H 3 O + : OH − ) delivered from the mixing tank unit in a reaction tank unit and reacting with the fuel raw material using the ionization active function of the ionized active gas. Generating a hybrid fuel gas to be supplied to the apparatus. A method for generating a hybrid fuel gas by ion activity.