Why does combustion cause pollution
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El Morabet, R. Effects of outdoor air pollution on human health. To delay the combustion with primary air, due to the ejection caused by axial repression with higher speed of secondary air, flue gases are absorbed from the furnace through a annular transversal section, forming a separating layer between the primary step and the secondary step.
In this burner there were integrated essential components of techniques to reduce NO x emissions:. Separation of primary air from secondary air through a stream of combustion inert gases that reduces the burning rate;.
Liquid and gaseous fuels flows are adjustable allowing the control of the combustion processes to conditions of reduced NO x. Very low NO x emissions were obtained by using the ASR burner alone and by applying additional techniques such as the addition of tertiary air, external flue gas recirculation and special spray nozzles for liquid fuel. To the combustion of oils with high sulfur content, according to the quality of these fuels, for entry into the solid particles and sulfur oxides emissions standards it is required the application of post-combustion control techniques that reside in the use of desulphurization systems, filters and cyclones.
For the furnaces of boilers burning solid fuel with low volatile content and a lot of bituminous ash having the liquid discharge of ash, NOx emissions level is relatively high.
Since it is necessary to maintain a minimum value of the combustion gases temperature required for the liquids discharge of ash, NO x emission control techniques are restricted in operation.
Cyclone furnaces with second chamber downstream offer very good conditions for combustion by-steps. To the combustion by-steps the procedure is as follows:. The optimal conditions for injection with tertiary air are met when the injection nozzles are designed and located so to provide the intimate mixture of the flue gas from the cyclone furnace and air.
Further reduction in NO x emissions was achieved by applying the external flue gas recirculation. Intensifying the internal recirculation of combustion gases is done with repressed secondary air with great speed through nozzles located at the end of the entry into splay, creating an important vacuum that absorb primary combustion products.
Combustion air admission is done best in three steps to avoid local temperature increase to high values. Oil spraying is done especially with slightly overheated steam using Y-type injectors. To reduce NO x emissions and pollutants in general, it can be used the self-carburizing process for both boilers and furnaces Gaba, A low burner of original conception, with solid carbon particles formation in flame, is fitted on three condensation boilers for steam and hot water.
The main burner elements provide the formation of annular jet of combustion air mixed with natural gas and of central fuel jet, which, by thermal cracking, forms subsequently particles of solid carbon.
These particles lead to increase of flame emissivity. Having in view the NOx emission, the characteristics of this burner are the following:. Another low NOx burner of original conception, with solid carbon particles formation in flame, is fitted on forge and treatment furnaces Gaba, The main constructive elements of this low NOx recuperative burner are: a ceramic quarl, a zone for the natural gas-ventilated air mixture, a zone for fuel atomization by collision with the compressed air, an air preheater and an ejector for exhaust gases.
The ceramic quarl burner has a cylindrical combustion chamber and in the peripherical zone a few cylindrical channels for exhaust gases entrances. Between combustion chamber and cylindrical channels are another channels for exhaust gases recirculation. The zone for the natural gas-ventilated combustion air includes three concentric pipes: the central pipe with different orifices and nozzles for natural gas and two pipes for divided combustion air in primary, secondary and tertiary air.
The air preheater ensures the heat exchange from exhaust gases to combustion air. Having in view the NO x emission, the characteristics of this burner are the following:. In conclusion, the solutions for upgrading the combustion plants for fossil fuels for boilers and furnaces can be grouped into:.
Secondary procedures for reducing NO x pollutant emissions use flue gases treatment plants. The reactions presented in the literature are selective, indicating oxidation of ammonia and sulfur dioxide SO 2 may not occur, the presence of oxygen being essential in the development of some reactions.
Due mainly to use low NO x combustion technology, to the replacement of solid fuels to natural gases, to the use flue gases treatment selective non-catalytic and selective catalytic emissions of SO 2 decreased from approx. Particles released into the atmosphere come both from combustion processes and the entrainment by the combustion gases from the raw material, e. Result of the combustion processes, the black smoke is a heterogeneous mixture and variable in structure, between soft solid particulates, water vapors and gases that result from the incomplete combustion of fuels.
As a result of the reduced size of suspended solid particles, the smoke refract light and color depending on the concentration and color of substances component in it. That is why the smoke comes in large range of dark colors from the weak gray to black, depending especially by the degree of perfection of the combustion and the quality of burned fuels. The determination of the index that characterizes smoke color is used for technical control of combustion quality, in combating environmental pollution, resulted in particular from burning of solid fuels and lower oils Bacharach no.
Generally, the formation of unburned solid materials in fossil fuels flames is pointing out especially the wrong mixing between fuel with air that is insufficient to achieve combustion even before carbon oxide is obtained. To liquid fuels without mineral content these solid particles can virtually disappear by burning that if the oxygen is in adequate proportions, in warm enough areas of the furnaces and for a sufficient residence time.
In black smoke it is noticed the emergence of two categories of unburned solid: very soft particles of soot and particles much larger than the first, sometimes called cenospheres from intermediate and heavy fuel combustion, or especially flying coke by combustion of solid fuels. The mechanism of the formation process of soot particles in gaseous fuels flames is explained by theories that belong to three main groups.
Thus, the first group includes theories that explain formation by thermal decomposition of hydrocarbons in fuel in carbon and hydrogen, with subsequent polymerization of the carbon. The second group of theories explains soot formation by oxidation of hydrocarbons until peroxides are formed and then by decomposition of peroxides free radicals are divided, which favors higher hydrocarbon formation, which under the high temperatures in the flame, are decomposing to form solid carbon particles.
The third group of theories involves the formation of soot particles in flame by polymerization of the C 2 radical. All these theories have a qualitative character, experiments verifying only certain assumptions that are made.
The burner of industrial liquid fuels create the fuels spraying as drops, firstly, to increase their surface in contact with the oxidizer. These last ones having a spongy aspect and spherical form, thus called cenospheres, are more numerous as the liquid fuel is more heavy, meaning that it contains molecules with more carbon atoms. The cenospheres result from cracking hydrocarbons in liquid phase as soft drops, through decomposition reactions that lead to release of gaseous products and building of solid residue rich in carbon, but which also contains minerals from the original fuel.
Similarly, the flying coke is made from soft coal particles, sprayed with air blast at coal dust operating burners. The heavy liquid fuels, in particular, build solid tailings from sediments and organ-metallic compounds that associate with carbon cracking residues.
Overall mass of solid particles thus formed for heavy fuels may be in the order of a few decigrams per kilogram of fuel. Cenospheres are in smaller numbers than particles of soot, but their overall mass is generally much bigger. Given the size of cenospheres, their combustion is slower than the combustion of soot particles.
This combustion is essentially controlled by the diffusion phenomena. Thus, its influence is decisive on: diffusion rate of oxygen to particle, diffusion rate of gases resulted from combustion by the ambient gaseous environment, the particle temperature and the activation energy of substances at work. It should not be missed the fact that the hydrocarbon skeleton of cenospheres contains mineral elements originally present in the fuel.
When using a good quality combustion plant and properly exploited, the solid particles mostly disappear by burning, leaving behind ashes of the initial mineral mass of fuel. This prevents the excessive pollution of the environment and the excessive increase of maintenance costs associated with deposition cleaning on the heat change pipes. Oil use with high sulfur content, requires operation at low excess of air close to the stoichiometric value, to reduce corrosion at low temperature. It is favored this way the increase of losses by unburned particles related to the soot and cenospheres and flying coke respectively.
Reducing these polluting emissions is directly influenced by the ratio between carbon C and hydrogen H of the initial fuel and the presence of asfaltenes in oil. Soot production in the flame makes this to be brighter and to transfer more useable heat by radiation.
As a result of this advantage, there was developed a process called self - carburizing by which carbon particles produced in the initial zone of the flame are completely oxidized to the top of the flame. This procedure has been used on some burners of boilers and furnaces, proving at the same time with the increasing efficiency very effective to reduce the emissions of CO, NO x and partially oxidized hydrocarbons Gaba, Primary procedures for reducing particles emissions, are to replace the solid and heavy liquid fuels oil with light liquid fuel combustions and to use complete combustion methods.
Primary processes that reduce particle emissions resulting from incomplete combustion of liquid fuel are:. After spraying by mechanical injection under pressure of heavy liquid fuels, a variation of the viscosity of dozen centistokes modify essentially the spraying features, with great repercussions on the process of combustion;.
Electrical refinement by gas ionization and dispersed particles sedimentation in a high-voltage electrical field. The direct amount of PM10 were reduced from kt in to kt in , and the secondary from kt to kt.
These substantial reductions were done, due to the dusting techniques of the exhaust gases, the replacement of solid and liquid fuels with high content in sulfur with natural gases, the introduction of the primary techniques for achieving combustion with reduced NO x emissions, the use of flue gases treatment and the application in EU of new regulations which limited the content of sulfur from some liquid fuels and which used advanced catalysts in internal combustion engines for transportation EEA— EN 07, Volatile organic compounds are aliphatic and aromatic hydrocarbons, alcohols, ketones, esters, aldehydes, benzene, toluene, acetones, methanol and formaldehydes.
POPs are mainly composed of polycyclic aromatic hydrocarbons PAHs , resulted in combustion processes of fuels in a smaller extent, but with particularly harmful effects, from dioxins and furans, resulted from the incineration of waste, pesticides and products of chemical industry. Partially oxidized hydrocarbons are generated by the lack of oxygen combustion air in combustion process, or from slow oxidation.
Lack of oxygen in the combustion process can be explained locally or temporarily, because combustion installation from industry are supplied with excess of combustion air. Due to poor mixing of fuel-combustion air, in the flame can occur rich zones in fuels which are formed unsaturated hydrocarbons, aldehydes and acids and, in some cases, the process can continue until the formation of soot.
These unburned elements may evolve, behind the flame front, depending on thermodynamic parameters and the interaction of oxidants. In combustion processes, the objective of reducing VOCs is their volatilization and oxidation to CO 2 and H 2 O, by thermal oxidation, catalytic or bio-oxidation. In the case of incinerators, especially, is practiced burning in secondary outbreaks, in which the catalysts can be introduced, after the primary focus.
As a group these are called "combustion appliances. The common fuels burned in these appliances are natural or LP gas, fuel oil, kerosene, wood, or coal. The types and amounts of pollutants produced depend upon the type of appliance, how well the appliance is installed, maintained, and vented, and the kind of fuel it uses.
Some of the common pollutants produced from burning these fuels are carbon monoxide, nitrogen dioxide, particles, and sulfur dioxide. Particles can have hazardous chemicals attached to them.
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