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INVENTION
Russian Federation Patent RU2105169
Method of the power plant KOLBENEVA
Internal combustion engine running on hydrogen

Name of applicant: Kolbenev Igor L.
Name of the inventor: Kolbenev Igor L.
The name of the patentee: Kolbenev Igor L.
Address for correspondence:
Starting date of the patent: 1993.03.01

Use: a method of operating the power plant with combustion engine operating on hydrogen or a mixture thereof with a hydrocarbon fuel.

The inventive process comprises feeding finely divided source of energy and water to the gasifier, maintaining the mass ratio of water and an energy greater than stoichiometrically required, carrying out the reaction, obtaining steam mixture and hydrogen feed vapor gas into the engine, combustion of the combustible mixture and converting the expanding gas energy into rotational shaft energy. As an energy carrier using an alloy comprising 96-75% of aluminum; 0.5-5.0% of gallium; 0.5-5.0% indium; tin, cadmium, antimony, bismuth and magnesium - the rest, the mass ratio of water and the energy source is maintained in the range 5: 1-10: 1, the reaction is conducted at a temperature of ^60-67 o C, a mixture of steam and hydrogen in a weight ratio of 5: 1 separated combustible gas and steam from the reaction product of slag and slag is removed to a settling tank where the heat engine exhaust was heated to ^450-500 o C, the reaction neraskhodovannuyu water is recycled to the gasifier for recycling the air before entering the engine passes through a fuel, reducing the friction of the particles, heat the steam-gas heat and air supply is carried out through a gas generator.

DESCRIPTION OF THE INVENTION

The invention relates to power engineering, in particular to the propulsion of internal combustion engine operating on hydrogen or a mixture thereof with carbon fuel.

A method of operating the powerplant comprising feeding finely divided source of energy and water to the gasifier, the maintenance ratio of water and an energy greater than stoichiometrically required, carrying out the reaction, obtaining steam mixture and hydrogen feed vapor gas into the engine, combustion of the combustible mixture and converting the expanding gases energy in the rotational energy of the shaft (see. French patent N 2408728, cl. the F 02 M 21/02, F 02B 43/00, 1979, a prototype).

The main drawback of the known method of operating the powerplant is possible that the implementation of the method at a temperature in the gasifier, the ratio of water and energy source, resulting in moistening of the combustible mixture when the formed slag reduces the intensity of the hydrogen generation.

Another disadvantage is the possibility of using the limited range of energy source, directly reacting with water.

Another disadvantage is the low efficiency of use of primary energy.

Object of the invention is to eliminate the above drawbacks.

The problem is solved in that a method of operating the powerplant Kolbeneva includes supplying finely divided source of energy and water to the gasifier, the maintenance ratio of water and an energy greater than stoichiometrically required, carrying out the reaction, obtaining steam mixture and hydrogen feed vapor gas into the engine, combustion of fuel mixture and conversion of the expanding gas energy into rotational energy of the villa, and is used as an energy source alloy comprising 96-75% of aluminum; 0.5-5.0% of gallium; 0.5-5.0% indium; tin, cadmium, antimony, bismuth and magnesium - the rest, the mass ratio of water and the energy source is maintained in the range 5: 1-10: 1, the reaction is conducted at a temperature of ^60-67 o C, a mixture of steam and hydrogen in a weight ratio of 5: 1 separated combustible gas and steam from the reaction product of slag and slag is removed to a settling tank where the heat engine exhaust was heated to ^450-500 o C, the reaction neraskhodovannuyu water is recycled to the gasifier for recycling the air before entering the engine passes through a fuel, reducing the friction of the particles, heat the steam-gas heat and air supply is carried out through a gas generator.

The drawing shows a diagram of the power plant that implements the method Kolbeneva.

The power plant 1 comprises a gas generator motor 2 equipped with three inputs and four outputs 5 and 6. The first input 3 of the gasifier 2 through the supply pump 7 is connected to an energy reservoir 8 with the energy source in the form of fine powder. Water tank 9 through the plenum 10 is coupled to a second input of the gasifier 2 and is further connected to a first output 5 of the gasifier 2 and the sump 11. The first outlet 5 of the gasifier 2 and the sump 11. The first outlet 5 of the gasifier 2 by the mechanism 12 forcefully removing the slag is connected to a sump 11. a second output of the gas generator 6 to the engine 2 is connected through capacitor 1 13, a regulator 14 and pump 15 feed vapor gas. Engine exhaust tube 16 1 is connected to sump 11 through valve 17. As the energy source that fills the tank 8 is used an alloy comprising 96-75% aluminum; 0.5-5.0% of gallium, indium 0.5-5.0%; tin, cadmium, antimony, bismuth and magnesium - the rest. Starting the engine 1 is carried out on hydrocarbon fuels, hydrogen or mixtures of hydrogen and a hydrocarbon fuel. With the blower 10 is directed from the water tank 9 through the inlet 4 into the gasifier 2 and the hydrogen generation mechanism in the liquefaction of the slag 12 removal force it into the sump 11. Simultaneously, the energy source 8 from a reservoir by a pump 7 to the input 8 of the gasifier 2, wherein the mixing and crushing energy and water jets, steam-mixture formation and slag. 6 from the outlet of the gasifier 2 the water vapor, hydrogen and air flowing through a fuel, filling a reservoir 8, passes through a condenser 13 where parovodorod converted to hydrogen with a predetermined moisture content and water which is returned to the tank 9. For adjusting the mass ratio of steam and steam-hydrogen mix change "time-cross section" of the electromagnetic valve controller 14 and passed partially or completely steam-mixture through a condenser 13. The air passing through the tank 8, heated by the heat of the gas generator, eliminates briquetting energy source and reduces the friction of the particles, and is supplied to the engine 1 through pump 15 steam-gas supply.

When the gasifier temperature is maintained at 2 ^60-67 o C, and the mass ratio of water and the energy source is maintained in the range 5: 1-10: 1, depending on the composition of the energy carrier. To reduce mechanical losses during operation of the mechanism 12 by removal of the solid phase reaction product water gasifier 2, further transferred to an input mechanism 12, it dilutes the slag, making it a colloid-disperse systems which are now easily transported to settler 11. In settler 11 from moist products reaction precipitated solids and free water fed to the gasifier 2 for reuse. Waste gases of the engine 1 are directed to the sump 11 through the exhaust pipe 16 and valve 17. In settler precipitated particles heat the exhaust gases are heated to ^450-500 o C.

Thus, the set task is achieved - increasing the efficiency and effectiveness by expanding the range of energy source used; maintaining a mass ratio of water and an energy in the range 5: 1-10: 1, conducting the reaction at a temperature of ^60-67 o C, separation of the combustible gas and steam from the slag and reaction products in removing the last settler where the engine exhaust gas heat, an active alumina with the desired properties. Moreover, a positive effect is achieved through the reuse of water, the energy carrier particles reduce friction feeding to the gasifier and the supply of air through the engine gas generator.

CLAIM

A method of operating the powerplant comprising feeding finely divided source of energy and water to the gasifier, maintaining the mass ratio of water and an energy greater than stoichiometrically required, carrying out the reaction, obtaining steam mixture and hydrogen feed vapor gas into the engine, combustion of the combustible mixture and converting the expanding gases energy in the rotational energy of the shaft, characterized in that as the energy used alloy comprising 96-75% Al, 0.5-5.0% of gallium, 0.5-5.0% of indium, tin, cadmium, antimony, bismuth and magnesium else, the mass ratio of water and the energy source is maintained in the range 5: 1-10: 1, the reaction is conducted at a temperature of ^60-67 o C, a mixture of steam and hydrogen in a weight ratio of 5: 1, and the combustible gas is separated from the pair of slag reaction products and slag is removed to a settling tank where the heat of the engine exhaust gas is heated to ^450-500 o C, the reaction neraskhodovannuyu water is recycled to the gasifier for recycling the air before entering the engine passes through the energy source, reducing the friction of the particles, and the heated vapor gas heat carried air flow through the gasifier.

print version
Publication date 24.11.2006gg

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