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Technique Technique | Equipment Method for solid hydrocarbons in liquid and gaseous fuels
Technique Technique | Equipment Method for solid hydrocarbons in liquid and gaseous fuels
| Method for solid hydrocarbons in liquid and gaseous fuels |
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| Written by Юрий Благодаров | |
| Monday, 29 September 2008 | |
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Transferred via translate.google.com
In Russia more and more accumulated deficit of power and the gap between the needs of electric and thermal energy and the capacity of its production. Dominant fuel in Russia is a gas. It accounts for 52% of the total energy consumption country and in teplogeneratsii share of gas is 68%. For all the attractiveness of its gas monopoly power threatens the sustainability of the country. However, a source of cheap gas to Russia ends. At the basic fields of Gazprom maximum production was reached in the early 1990's, by 2012, gas production from them to fall in the 3-7 times. Because Russia has an extensive network of pipelines for transportation of liquid and gaseous fuel to the West, it is advisable to transfer solid hydrocarbons in liquid and gaseous fuels and transport it through pipelines. On the effectiveness of the use of heat, the installation exceeds the reactor, because It combines in a single device, gas and water boiler - gas produced from solid hydrocarbons of raw liquid and gaseous fuels and water boiler produces heat, hot water for space heating. There is an opportunity for local livelihoods and to the remote forest / business enterprises, heat transfer, hot water, steam, electricity in the workshop locations. The creation of new mini-power companies will reduce the tension in the deficit of power, will create competition. And, in this regard, and to reduce energy prices. All the known method prozhiganiya holes in thick wood tip heated nail. Thus, at the prozhiganiya, the tree goes from solid to a gaseous state. Are the carbon and hydrogen. Then, when in contact with atmospheric oxygen, they turn into fuel gazy.Sposob is in the process of thermochemical transformation of solid carbohydrate material in the combustible elements: carbon (C), hydrogen (H), partial oxidation of carbon (C) carbon monoxide (CO), in the presence of water vapor, with the decomposition of water vapor into hydrogen (H) and oxygen (O), to result in the combustible gases (CO), (SmNn), (H2) in the gas - a sealed tank with a boiler, furnace which includes a convex part in a sealed container and an emitter of heat energy, the saturation chamber, formed between the outer surface of gas and the surface of the fireplace, which is formed and accumulated water vapor. The device differs from that thermochemical conversion of solid hydrocarbons in the fuel elements: (C) and (H), conducted by Feed on the front surface of the fireplace, under the pressure. However, partial oxidation (C) (CO), in the presence of water vapor, with the decomposition of water vapor in the (N) and (O), are in contact the solid hydrocarbons, with the front surface of the fireplace, a full oxidation (C) (CO), in the presence of water vapor, with the decomposition of water vapor in (H) and (G), to result in the combustible gases (CO), (SmNn), (H2), held in camera saturation in a medium of superheated steam . For intensification of the oxidation (C) (CO), steam the mixture in the chamber is brought into saturation around the surface of the fireplace. The temperature at the end of the furnace is maintained at 750-850 degrees. To do this, it is made of copper, as coefficient of thermal conductivity of copper 8-fold higher than that of steel. Saturation temperature in the chamber is maintained at 650-750 degrees. A pressure of 0.7 atm. To maintain the temperature within these limits steam mixture is passed in a circle, a fan WSC. In doing so, sending a mixture of steam and condenser in a refrigerator, for receiving liquid and gaseous fuels. Pressure supported by the quantity of liquid supplied to form a pair. Analogue of the idea of a patent RU 2330214 C1, 25.10.2006
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