Method of solid fuel combustion intensification

a solid fuel combustion and intensification technology, applied in the field of power engineering and metallurgy, can solve the problems of unproductive oxidizer loss, precious oxidizer, and the necessity of obtaining oxidizers using additional complex and metal consuming technologies, and achieve the effects of increasing the rate of oxidation, reducing energy expenditure, and increasing the degree of carbon burning

a solid fuel combustion and intensification technology, applied in the field of power engineering and metallurgy, can solve the problems of unproductive oxidizer loss, precious oxidizer, and the necessity of obtaining oxidizers using additional complex and metal consuming technologies, and achieve the effects of increasing the rate of oxidation, reducing energy expenditure, and increasing the degree of carbon burning

US20080044781A1Inactive Publication Date: 2008-02-21LIMITED LIABILITY RES AND PRODION COMPANY UKRTRANSKOM +1

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  • Method of solid fuel combustion intensification
  • Method of solid fuel combustion intensification
  • Method of solid fuel combustion intensification

Examples

Experimental program
Comparison scheme
Effect test

Embodiment Construction

[0021]The air flow containing pulverized solid fuel comes into the combustion chamber 1. It passes through the grid 7, bottom grate 5, and arrives into the zone 2. Electric ignition 3 provides the ignition temperature of the fuel-air mixture and after that it is switched off. The stationary combustion process is established which is defined by the heating rate of the precisely measured volume of the heat-transfer medium 4 (water in our case). The 5 to 20 kV voltage is supplied from the power supply 8, 9 to the grid 7 coated with the catalyst enhancing the combustion process. This mode is defined by the heating rate of the equal volume of the heat-transfer medium.

[0022]FIG. 2 shows dependence of the water temperature variation from the time when carrying out idle experiment and with the discharge. When coal is combusted with the discharge water heating is accelerated which is evidence of the release of a larger amount of heat as compared to the idle experiment. (On the curves shown t...

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Abstract

The substance of the invention consists in the combustion of the fuel-air mixture in the electric field by means of the catalyst located in the combustion zone and to which high voltage is applied, which results in reduction of activation energies of all endothermic combustion phases due to the formation of oxygen atoms, carbon radicals and oxygen-containing radicals.Technical result: introduction of the catalyst in the combustion zone minimizes energy expenditure for creation of the low-temperature plasma, allows to increase the temperature in the combustion zone, to reduce activation energy of all endothermic processes taking place at the initial phase of combustion and to reduce carbon content in the ash and to achieve considerable fuel economy.

Description

BACKGROUND OF THE INVENTION[0001]The method relates to the power engineering, metallurgy, and namely, to the solid fuel combustion: coal, peat, wood.[0002]The process of solid fuel combustion is well known. So far, a considerable number of methods of solid fuel intensification are known. One of the methods consists in combustion intensification by increasing oxygen concentration in the flame, resulting in increasing of atoms and oxygen-containing radicals in the combustion zone.[0003]The method of oxygen-convector steel melting is known (see Kazakov N. F., Osokin A. M., Sishkova A. P. Technology of metals and other structural materials, 1975-688 p.). The substance of this method consists in the iron oxygen blow through the lance. During the high-temperature mass oxygen blowing oxidation of hardly oxidized additives is achieved. The highest oxidation of additives takes place at the oxygen jet-metal interface.[0004]The disadvantages consist in the use of a precious oxidizer, unproduct...

Claims

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Application Information

Patent Timeline
21 Feb 2008
Publication
US20080044781A1
IPC
F23Q11/00; F23B90/00
CPC
F23B7/00; F23C99/001; F23C13/00; F23B90/00
Inventors
STOLYARENKO, HENNADIY STEPANOVYCH; VIAZOVIK, VITALII MYKOLAYOVYCH