Patent Publication Number: US-6709490-B1

Title: Combined system for removing contaminants from gas effluents

Description:
FIELD OF THE INVENTION 
     The present invention is related to the techniques for the elimination of pollutants, and more particularly, it is related to a combined system for the elimination of pollutants from gaseous effluents. 
     BACKGROUND OF THE INVENTION 
     Pollution has existed since man began to modify his environment by using tools, managing fire, and performing agriculture, thus differentiating himself from other predators. For instance, the arrival of agriculture gave place to alterations in the existing ecosystems. However, it was in a very similar way to what happened in natural phenomena. 
     Although such changes in the environment surrounding man are very ancient, it was until the industrial revolution when man obtained enough control over the environment as to deteriorate it. Even though such deterioration is relatively recent with respect to human history, there had to pass almost two hundred years before solutions started to be sought. In view of this, the new challenge that civilization has to face nowadays consists of knowing how to make maximum the availability of necessary goods as the cost in terms of pollution, use of natural resources and other related issues is minimized. 
     Other of the most affected resources, mainly in big cities, is air, which is polluted with all kind of gases and floating particles. Against what could be thought, molecules of inorganic nature are the most common pollutants in atmosphere, except for partially burnt hydrocarbons and other substances coming regularly from combustion processes. For example, in the treatment of metallic sulfur minerals, the toasting processes can be an important pollution source if there is no effort to catch the sulfur dioxide that is discharged as byproduct. 
     A classical example of this problem is described in the article of C. R. Hursh in 1935 in the brochure: “Local Climate of Cooper Basin of Tenessee as Modified by Removal of Vegetation”, USDA, number 774. There, it is described what happened in Copperhill, Tenn., where the products of metallic sulfur minerals toasting have altered the woods in an area of almost 220 km 2 . The woods have disappeared almost completely, although some zones with grass in a girdle covering approximately 7000 hectares still exist, thus leaving a remaining area of 28000 hectares completely without vegetation. 
     Less known is the damage caused by a zinc foundry in Leigh gap, Pa. It is presented in the article of M. J. Jordan in 1975 in the magazine “Ecology”, number 56, volume 78. The damage was caused by emissions of sulfur dioxide, zinc, cadmium, copper and lead. The samples of the ground, taken approximately two kilometers away from the foundry, contained more than 8% of zinc. 
     As it can be seen from the latter, air pollutants can also produce pollution of the ground and ecosystems due to the fact that they travel easily and rapidly. Air pollutants can be classified in different ways, considering both the emitting source and the physical and chemical features of the emissions. 
     It is quite difficult to characterize the pollution producing sources. There has been estimated that in the United States 60% of the air pollution comes from engine driven vehicles and 14% comes from electricity generating plants, as industry produces about 17%, the remaining 9% coming from air conditioning. The annual emission of pollutants in the United states is very meaningful since, as mentioned, engine driven vehicles contribute with about 60% of the total pollution, from which almost all is carbon monoxide, two thirds of hydrocarbons, one half of nitrogenous oxide and little fractions of other compounds. 
     The pollution due to combustion engine driven vehicles is a much bigger problem in big cities, and even more in the largest such as Mexico City. In big cities the extent of urban areas and the intense economic and social life forces people to travel great distances in order to perform their ordinary activities. 
     It is estimated that in Mexico City, vehicle emissions represent about 76% from the total pollutants emitted to the atmosphere; private vehicles emit more than half the pollutants of vehicular origin, and when using gasoline, they also produce lead oxides, sulfur and suspended particles. 
     Nevertheless, it is necessary to consider that pollutants come from fixed sources as well as from mobile sources. In developing countries it has been found that environmental pollution comes mainly from industries that throw their wastes illegally during the night, i.e., pollution comes from fixed sources. 
     On the other hand, in its simplest form, control of air pollution needs basic knowledge for establishing adequate criteria in order to maintain the freshness of air; ability to relate air quality to emission levels; establishment of emission limits or other control standards; means for measuring emissions and air quality and availability of practical techniques for reducing the emissions that pollute it. 
     In regard to the practical techniques for reducing emanations, even though it has been given attention to process changes that reduce polluting emissions, a great confidence has been given also to physical processes for eliminating such pollutants therefrom. 
     Within the existing techniques, a distinction is made between those developed for appliance on mobile sources directly and those developed to be used in fixed sources. It is worth mentioning that most of them have focussed on the treatment and control of emissions coming from fixed sources. This is probably due to the easiness of installation, operation and maintenance and to the pressure exerted by governments over industries, thus forcing them to install apparatus that enable them to comply with the increasingly strict rules in regard to the pollutants emitted to the atmosphere. 
     The apparatus used to clean the air from particles coming from fixed sources are based basically on aerodynamic catch, such as inertial impact, direct interception and diffusion. However, some apparatus use electrical and thermal forces, chemical reactions, and apply principles such as absorption, adsorption, condensation, etc. 
     Filtration is one of the most used methods, in which various types of filters are incorporated in direct interception processes as well as in diffusion processes, in a way that there can be achieved very high efficiencies not only with big particles but with the small ones. The use of these principles has resulted in the development of various technologies. For instance, Mexican Patent No. 131020 is related to an air purifying apparatus. It comprises at least one particle-filtering module in one of its walls and an activated carbon filter module, wherein the particle-filtering module comprises a filter for fine particles and one for bulky particles. 
     Another example is the portable air purifier of Mexican Patent Number 188350 which comprises one chamber with an air intake and an air outlet, as well as a filtration means provided inside the chamber between the air intake and the air outlet. They are assembled in such a way that when air crosses through the chamber, the particles are retained due to the filtration means. 
     Among the possible variations there can be found bag filters, which are capable of managing particles having diameters of less than 1 micron. However, they show the disadvantage of having a maximum operating temperature of 500° F. and generating pressure drops higher than 4 in H2O, although they can achieve efficiencies around 99% and need little space for its operation. An additional inconvenient of these filters is the great sensitivity of the bags to humidity, filtration rates and temperature. 
     Obviously, there can be used different types of filters to achieve a better separation of the pollutants, as described in Mexican Patent Application number 9101571. The method is based on a filtration system comprising pre-filters, absolute filters and activated carbon filters that purify and sterilize polluted air, which is forced to pass through the same by means of one or more fans; thus achieving a retention efficiency of the filters of about 95%. 
     There have been made some efforts in order to achieve better results in collection by electrically charging the particles to be eliminated. These filters operate with a collecting efficiency of about 99.9%. This can be seen in the electrostatic filter air purifier shown in Mexican Patent Application No. 9501387, which comprises an electrode and an electrostatic filter that enhance separation and collection on pollutant emissions. 
     Another widely used technique is damp collectors that separate particles and operate due to the contact between particles contained in a gas stream with a liquid. Damp collectors generally use water, in the form of little drops, which is put in contact with the pollutants of the gas stream; the separation is due to the collision between the particles suspended in the gas stream and the little drops of water. Among damp collectors there can be found mainly spray towers, which can achieve efficiencies around 80%. Examples of use of these techniques can be found in the Mexican Patent Applications Nos. 9603017, 9600105 and 9301564. 
     Electrostatic precipitation is the most important technique in particle separation. In general terms, the particles present in a gas stream are electrically charged by means of a high voltage discharge coming from an electrode and are collected in collecting plates having an inverse polarity. Electrostatic precipitators can achieve efficiencies of 99% at optimal conditions, but its performance is still low under non-favorable conditions. Electrostatic precipitators are capable of retaining particles having diameters of less than 1 micron, operating within a temperature range between 40 and 850° F. Electrostatic precipitators generally have pressure drops of less than 1 in H 2 O and operate with efficiencies close to 99%. 
     There can be considered as principal components of electrostatic precipitators the electrical discharge plate and the particle-collecting surface. Charging the particles with a high voltage, whether positively or negatively, produces the separation, and then let the charged particle to be attracted by the collecting surface, which has an opposite charge than the particle. 
     Within the existing electrostatic filtering apparatus are found those described in U.S. Pat. Nos. 3,967,939, 4,140,498, 4,194,888, 4,202,674, 4,626,262, 4,675,029, 5,039,318, 5,050,377, 5,121,601, 5,147,423, 5,248,324, 5,302,190 Y 5,439,508, among others. 
     Under the same principle, there are known apparatus operated by means of changes in the resistance as a method for the retention and separation of particles, which is found in U.S. Pat. No. 4,779,207, as U.S. Pat. Nos. 5,039.313 and 5,704,955 make use of conventional filters for the retention of such pollutants. Another similar method is the electrodynamic separation as described in U.S. Pat. No. 3,973,932. 
     Is worth mentioning, however, that filters in general are only used for eliminating suspended particles and not for eliminating other kinds of pollutants, such as gaseous type pollutants, for example. 
     On the other hand, condensation and precipitation principles are also useful methods for the separation of polluting emissions. As an example of the latter it is possible to mention Mexican Patents Nos. 186045 and 188200. They refer to processes for eliminating emissions by condensing and precipitating that comprise collecting the moisture charged air stream containing the emissions, of oil in this case, to be separated; cooling the moisture charged air that contains the emissions, which is collected at a moist saturation temperature at which the moisture contained in the air is condensed so as to form a liquid in such a way that an aqueous condensed liquid stream is formed and an outlet air stream containing moisture saturated air and liquid droplets; eliminating from the air stream the liquid droplets of the emissions in order to form a second condensed liquid stream containing an important part of the oil emissions; and heating the outlet air stream at a temperature over its moist saturation temperature in order to eliminate the humidity from the air and obtain an outlet air stream that can be discharged to the atmosphere. However, in this method is required the pollutant to be easily condensed, otherwise it would be maintained as gas and could not be eliminated by this method. 
     In general terms, most of the current techniques for treating gaseous polluted effluents of high efficiency present the inconvenience of requiring a liquid for the treatment, which in turn has to be post-treated to avoid pollution of effluents and ground. Additionally, the use of liquids generates corrosion in the apparatus and can be very sensitive to changes in particle properties thus decreasing its efficiency; and in general, they can only be used for certain kinds of pollutants. On the other hand, the apparatus that need not an additional fluid present low efficiency. 
     Nowadays, there are some apparatus capable to manage various types of 35 polluting emissions, both coming from fixed sources and from mobile sources. This ability is determined by the arrangement of its components and by the use of several of theabove-described techniques together. For instance, Mexican Patent No 180969 refers to an apparatus for separating environment-polluting agents. It is characterized by comprising a series of consecutive chambers that separate and retain polluting particles; a first chamber for the air reception which is provided with horizontal grilles with its openings covered with pre-filters that are maintained humid by means of a system of water spraying tubes; a second chamber that directs air and avoids the generation of turbulence; a third chamber comprising a plurality of deposit trays previously bath in a solution that enables it to retain such solid particles, as well as a steel mesh covered with filtrating means in order to trap the solid particles that were not retained by the mentioned trays; and a fourth chamber receiving the clean air coming from the third chamber to discharge it outside as a siphon. 
     From the above it can be observed that is possible to use some apparatus in a combined form and which combination results in a decrease of various types of pollutants present in a gas stream. Therefore, it is possible to use in the same method filters, pre-filters, washing techniques, precipitation, reaction, etc. 
     In Mexican Patent Application No 9603012 the improvements made to the last described apparatus are referred to, which consist of including a plurality of electrodes that allow the molecular breaking of the pollutants, which leads to a more efficient operation of the apparatus. Such electrodes perform an electronic bombardment on the effluent; thus generating ionization due to said electronic bombardment. Due to this reason this technique is also known as ionization. Actually, ionization by itself is used in air purifying apparatus. However, the efficiency of these apparatus is rather low and they are barely used for industrial gaseous effluent treatment. 
     Now then, in regard to mobile sources such as the combustion gases of automobiles, the most used apparatus are those of the catalytic type, which in addition to be expensive due to the noble metal content, they tend to be easily poisoned, thus decreasing its efficiency in a great extent. 
     In the specific case of engine combustion gases, although it has been achieved a decrease in the quantity of nitrous oxides, hydrocarbons, sulfur compounds and other polluting gases, the acid pH of the water expelled from the vehicle gas escapes has not been decreased. It is known that such water has pH values of approximately 4, this value being a very acid one for water. As it is easy to suppose, this phenomenon does not favor the elimination of acid rain nor of its harmful effects on health. 
     Consequently, for long it has been sought to overcome the inconveniences of prior art techniques for eliminating pollutant from gaseous streams by means of a combined system for the elimination of pollutants from gaseous effluents that allows to eliminate suspended particles such as gas pollutants, mainly coming from a combustion, without needing additional fluids for the treatment, which in addition has a high efficiency of pollutants removal. 
     OBJECTIVES OF THE INVENTION 
     Having in mind the drawbacks of the prior art, it is an object of the present invention to provide a combined system for the elimination of pollutants from gaseous effluents of easy and economic construction but with high efficiency and reliability for retaining in a great extent diverse solid pollutant particles suspended in air. 
     Another object of the present invention is to provide a combined system for the elimination of pollutants from gaseous effluents able to operate satisfactorily at extreme environmental conditions without presenting any changes or considerable variations regarding its efficiency. An additional object of the present invention is to provide a combined system for the elimination of pollutants from gaseous effluents that by means of a rapid and easy operation allows the maintenance and/or interchange of its internal parts. 
     It is also another object of the present invention to provide a combined system for the elimination of pollutants from gaseous effluents resulting to be very flexible in its manufacturing from a great variety of materials and shapes according to specific requirements. 
     Likewise, it is another object of the present invention to provide a combined system for the elimination of pollutants from gaseous effluents that allows to reduce the organic compounds expelled to the atmosphere, specially lower hydrocarbon chains. 
     Another object of the present invention is to provide a combined system for the elimination of pollutants from gaseous effluents that makes disappear the visible polluting particles that can be found suspended in the atmosphere. 
     Additionally, it is an object of the present invention to provide a combined system for the elimination of pollutants from gaseous effluents that allows to diminish the temperature of the gases expelled to the atmosphere. 
     It is also an object of the present invention to provide a combined system for the elimination of pollutants from gaseous effluents that allows a decrease of acidity in pluvial water as well as in the condensed water of the gas outlets of combustion engines. 
     Another object of the present invention is to provide a combined system for the elimination of pollutants from gaseous effluents that allows a decrease in the physical annoyances of people, generated by the exposure to atmospheres having high pollutant concentration. 
     In addition, another object of the present invention is to provide a combined system for the elimination of pollutants from gaseous effluents that can be used in both mobile sources and fixed sources. Still another object of the present invention is to provide a combined system for the elimination of pollutants from gaseous effluents that can be used in modular form. 
     It is also another object of the present invention to provide a combined system for the elimination of pollutants from gaseous effluents with a high particle retention level, specially for those toxic particles suspended in the environment. Another object of the present invention is to provide a combined system for the elimination of pollutants from gaseous effluents that allows a reduction in the amount of pollutant precursors expelled to the atmosphere. 
     It is an additional object of the present invention to provide a combined system for the elimination of pollutants from gaseous effluents that requires very low energy consumption for its operation. An additional object of the present invention is to provide a combined system for the elimination of pollutants from gaseous effluents that do not require additional fluids for the treatment but still having a high efficiency in pollutants removal. 
     A further object of the present invention is to provide an apparatus incorporating the combined system for the elimination of pollutants from gaseous effluents mentioned above. 
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS 
     The novel features that are considered characteristic of the present invention are set forth particularly in the appended claims. However, the invention, as well as other objects and advantages thereof, will be best understood in the following detailed description of an specific embodiment, when read in connection with the accompanying drawings, in which: 
     FIG. 1 is a block diagram of the combined system for the elimination of pollutants from gaseous effluents, built according to the principles of the present invention. 
     FIG. 2 is a top view of a preferred embodiment of an apparatus for the elimination of pollutants from gaseous effluents that works in accordance with the system of FIG.  1 . 
     FIG. 3A is a left side view of the gas supply module of the apparatus in FIG.  2 . 
     FIG. 3B is a front view of the gas supply module of the apparatus in FIG.  3 A. 
     FIG. 4A is a side view of the heat diffusion and molecular destabilization module of the apparatus in FIG.  2 . 
     FIG. 4B is a cross section view of the heat diffusion and molecular destabilization module of FIG.  4 A. 
     FIG. 5A is a side view of the electronic bombardment module of the apparatus in FIG.  2 . 
     FIG. 5B is a top plan view of the electronic bombardment module of FIG.  5 A. 
     FIG. 5C is a front view of the electronic bombardment module of FIG.  5 A. 
     FIG. 5D is a back view of the electronic bombardment module of FIG.  5 A. 
     FIG. 5E is a schematic diagram of the Venturi principle used in the electronic bombardment module of FIG. 5A for generating turbulence. 
     FIG. 6 is a side view of the magnetic molecular rearrangement module of  20  the apparatus in FIG.  2 . 
     FIG. 7 A is a side view of the electrostatic interaction module of the apparatus in FIG.  2 . 
     FIG. 7B is a front view of the electrostatic interaction module of FIG.  7 A. 
     FIG. 8A is a left side view of the gas expulsion module of the apparatus in  25  FIG.  2 . 
     FIG. 8B is a front view of the gas expulsion module of the apparatus in FIG.  8 A. 
    
    
     DETAILED DESCRIPTION OF THE INVENTION 
     It has been surprisingly found that by incorporating two physical principles in the purification techniques of electronic bombardment and electrostatic interaction, directed to produce changes in the molecules comprising a gas stream, there can be achieved a much higher retention and decomposition of pollutant particles and molecules suspended in such gas stream than those obtained by means of the known techniques of electronic bombardment and electrostatic precipitation. 
     The combined system for the elimination of pollutants from gas effluents of the present invention has the main function of changing the primary composition of a gas stream, giving its molecules physical features that allow their retention and/or transformation in a high degree, thus achieving a considerable pollutant reduction. 
     Having now more particular reference to the enclosed drawings, and more specifically to FIG. 1 thereof, it shows a block diagram of the combined system for the elimination of pollutants from gaseous effluents of the present invention. It comprises, in general, means for performing the following operations: heat diffusion and molecular destabilization  100 ; electronic bombardment  200 ; magnetic molecular rearrangement  300 ; and, electrostatic interaction  400 . 
     The system functions by subjecting a polluted gas stream  1  to a molecular destabilization  100 , where the gas flow is restricted in such a way that the gas molecules and the particles suspended thereof tend to separate and electronically destabilize, at the time the gas temperature is decreased. This operation  100  allows electronic bombardment operation  200  to increase its efficiency in a great extent, due to the fact that the bombarded electrons can affect the molecules more easily. Additionally, electronic bombardment  200  is performed under such voltages and current intensities that enough energy is provided to form chemical bonds, even ionic, between the gas molecules, thus forming compounds that by the combined effect of the decrease in temperature due to operation  100  and the increase in molecular weight can condense or precipitate. The latter happens in addition to the ionization generated inherently to the electronic bombardment in such molecules that do not achieve condensation. 
     Once electronic bombardment  200  is performed, a magnetic molecular rearrangement operation  300  is performed. It consists of subjecting the gases to a magnetic field having such force that allows a rearrangement of sub-particles and molecules of higher weight, and therefore, that allows a selective separation that separates the gas stream for electrostatic interaction operation  400 . The electrostatic interaction  400  is improved due to the selective separation made by the magnetic molecular rearrangement  300 . Once the electrostatic filtration is made, a treated gas stream  2  having low levels of pollutants is obtained. 
     As can be seen from FIG. 1, treated gases  2 , can be subjected again to electronic bombardment  200 , magnetic molecular rearrangement  300  and electrostatic filtration  400  operations as many times as wished, achieving with each repetition a higher decrease in the pollutants concentration, the only limitation being the economical convenience. 
     In a preferred embodiment of the system of the present invention, the heat diffusion and molecular destabilization operation is designed to decrease temperature in the polluted gas stream  1  to a range of about 30 to 50° C. and to generate a turbulent flow having a Reynolds number of about 10.12 to 1; the electronic bombardment  200  is designed to use direct current having a voltage within the range of 500 to 80000 Volts, approximately, and an approximate current intensity of 2 mA to 2A; and, the magnetic molecular rearrangement  300  is designed to generate a magnetic field of 0.5 to 3 militeslas. It is worth to further mention that it has been surprisingly found that by using such preferred current intensities and voltages, the achieved results are better than those achieved until now by means of prior art electronic bombardment systems. 
     By using the system of the present invention in gas streams coming from direct combustion of various materials, an elimination of 60% to 96%, approximately, of the present hydrocarbons and non-aromatic compounds is reached, and inclusively a decrease in the content of carbon dioxide of 25% is achieved. The system of the present invention does not produce ozone provided that an important amount of present molecular oxygen does not exist, i.e., when the gases getting into the system contain less than 15% of oxygen. 
     Likewise, the system of the present invention allows the elimination of those hydrocarbons that participate in the ozone formation reactions in the atmosphere, thus avoiding pollution by atmospheric ozone. 
     The system of the present invention can be used for manufacturing an apparatus for the elimination of pollutants from gaseous effluents  1000 , which can be observed in FIG.  2 . FIG. 2 shows a top plan view of apparatus  1000 , wherein the following modules can be seen: A gas supply module  1100 ; heat diffusion and molecular destabilization module  1200 ; an electronic bombardment module  1300 ; a magnetic molecular rearrangement module  1400 ; an electrostatic interaction module  1500 ; and, a gas expulsion module  1600 . 
     The gas supply module  1100  has the function of generating a positive pressure in order to let the gases that will be treated to flow there through. As can be seen in FIGS. 3A and 3B, in the described embodiment, the gas supply module  1100  is preferably a blower that includes an helix with a plurality of vanes  1111 , which is coupled to motor means  1120 , preferably an electric engine, that have the ability of introducing the gases into apparatus  1000 , said blower being preferably contained inside a rectangular chamber  1130 . 
     In an additional embodiment, the gas supply module includes control means to adjust the volumetric flow of gases to an adequate value for the treatment of thereof. 
     In regard to the heat diffusion and molecular destabilization module  1200 , it has the function of decreasing the gas temperature and increasing its flow turbulence in order to generate a molecule destabilization. This is achieved, as can be seen on FIGS. 4A and 5B, by making the gases pass through a plurality of micro-tubes  1210  located inside a duct  1220 . In the embodiment shown on FIGS. 4A and 4B, the duct  1220  includes  3  sections of micro-tubes, such micro-tubes preferably having an internal diameter of 0.5 to 5 mm, approximately. However, the dimensions of duct  1220  and micro-tubes  1210  are a function of the volumetric flow of the gases that are subjected to treatment, although it is preferred to change only the dimensions of duct  1220 . In the described embodiment, duct  1220  has a circular cross section, as observed on FIG. 48, and also includes a 3-pass arrangement of the micro-tubes. In addition, the heat diffusion and molecular destabilization module  1200 , includes first coupling means  1230  and second coupling means  1240 , in order to allow the union of module  1200  with module  1100  and with module  1300 . 
     On the other hand, as may be observed from FIGS. 5A and 5E, the electronic bombardment module  1300 , in accordance with the described embodiment, is formed by a plurality of joined hermetic chambers  1310  serially connected by a plurality of flow restriction means  1320 . Said restriction means, in addition, generate a better distribution of the gases in each chamber, direct the flow of gases so as to require the least space for the pass of gases through as most the chambers  1310  as possible. Such chambers have a dimension depending upon the volumetric flow of the gas stream and include at least a pair of elements for electronic bombardment  1330 . The dimensions of the chambers are preferably such that provide a residence time of the gases in each chamber within the range of 0.3 to 10 seconds, approximately. 
     The electronic bombardment elements  1330 , are electrically connected to a direct current source  1360  (shown in FIG. 2) that provide a voltage within the range of 50 to 80000 volts, approximately, and an approximated current intensity of 2 t to 2A. Preferably, an alternate current to direct current rectifier is used to provide the electrical energy needed for the performance of module  1300 . 
     In a preferred embodiment of the present invention, electronic bombardment elements  1330  are produced by using materials preferably selected from copper, gold, nickel, tungsten, silver, wolframium, platinum, palladium, stainless steel, and combinations and/or alloys thereof. 
     Chamber  1311 , which receives the gases coming from module  1200 , includes a gas inlet orifice  1312  to the electronic bombardment module  1300 , while the last chamber  1313  includes a gas outlet orifice  1314 . Orifices  1312  and  1314  are respectively coupled to assembly means  1340  and  1350 , to allow the interconnection of module  1300  with modules  1200  and  1400 . 
     Is important to mention that flow restriction means  1320  allow the formation of a flow pattern as shown on FIG. 5E, i.e., Venturi type turbulence. In a preferred embodiment of the present invention the flow restriction means are selected among orifices and valves, preferably check valves. 
     Likewise, the collocation of chambers  1310  as well as of electronic bombardment elements  1330  is defined in such a way that voltaic arcs formation or circuit breakage is avoided, maintaining a geometry that allow the generation of an adequate electronic bombardment atmosphere. 
     In an additional embodiment, chambers  1310  include liquid drainage means by which the liquids that were condensed due to the electronic bombardment are eliminated. 
     Referring now to FIG. 6, it shows the configuration for magnetic molecular rearrangement module  1400 , which comprises a duct  1410  and magnetic field generating electromagnetic means. In the embodiment under description, a duct  1410  with circular transverse section including a plurality of coils  1420  so as to form a plurality of solenoid type electromagnetic arrangements by means of the unit duct-coils. The coils have a distance between themselves equivalent to the internal diameter of duct  1410 . Electric energy is supplied to the described arrangement in such a way that a positive (south) magnetic pole  1430  is formed at the side of module  1400 , which is connected to module  1300 , while at the side connected to module  1500 , a negative (north) magnetic pole  1440  is formed (see also FIG.  2 ). 
     Magnetic rearrangement module  1400  also includes an electric current source (not shown in the figures) that provides the electric current necessary to generate a magnetic field of 0.05 to 3 militeslas, thus achieving a rearrangement of sub-particles and heavier molecules, and therefore, a selective separation that prepares the gas stream for entrance to module  1500 . 
     On the other hand the electrostatic interaction module  1500 , shown in FIGS. 7A and 78 comprises, in general, an electrostatic filter  1510 ; first coupling means  1520  and second coupling means  1530 . In the described embodiment, the electrostatic filter comprises a pair of filters  1511  and  1512  electrically charged by opposite charges, respectively. The filters have preferably a mesh of 5 to 50 microns, approximately, preferably 10, in the middle of which a mechanic filter  1513  is found, preferably with a mesh of 95% to 98.5% less than the used mesh to the pair of filters  1511  and  1512 . The material used to produce the filters is any suitable of being electrically charged, preferably steel. 
     In the described embodiment, the first coupling means  1520  allow to connect module  1500  with module  1400 , isolating both modules in order to avoid any electrical interference, while the second coupling means  1530  allow the union of module  1500  with module  1600 . In an additional embodiment of the present invention, first and second coupling means  1520  and  1530  have a design that allows the easy release of the electrostatic filter. This is due to the fact that the electrostatic attraction generated by the positive and negative charges causes filters  1511  and  1512  to become saturated by the association of oppositely charged particles with the material thereof, thus making necessary its replacement. 
     Electrostatic interaction module  1500  also includes a current source (not shown on figures) that provides the electrical current needed to generate a positive charge of +5 to +50 kV, approximately, as well as a negative charge between −5 and −50 kV, approximately. Preferably, it generates a positive charge of approximately +25 KV and a negative charge of approximately −15 KV. 
     Finally, FIGS. 8A and 8B show gas expulsion module  1600 , which has the  20  function of generating a negative pressure to induce the outlet of the treated gases towards the outside of the apparatus. In the described embodiment, gas expulsion module  1600  is preferably a blower including a fan  1610  with a plurality of vanes  1611  that is coupled to motor means  1620 , preferably an electrical engine, having the ability of inducing the outlet of the gases from apparatus  1000 . The blower is preferably within a rectangular chamber  1140 . 
     In an additional embodiment, the gas supply module includes control means to adjust the volumetric flow of gases to an adequate value suitable for the treatment thereof. 
     In another additional embodiment, the treated gases coming out from the gas expulsion module  1600 , are introduced again into an apparatus that does not include a heat dispersion and molecular destabilization module  1200 , and therefore, module  1600  includes coupling means  1630 . 
     The coupling means of the different modules are preferably selected from fastening and/or joining means. The preferred means are flanges, bearings, assemblies, screws, welding, threads, chamfers, rivets and/or combinations thereof. 
     Likewise, in a preferred embodiment of the present invention, each one of the electrical current sources of the modules of the apparatus includes a computer control and various electronic circuits and electronic protection in order to achieve a performance of the type considered as intrinsically safe. Likewise in an additional embodiment, the same energy source is shared to supply all the modules of the apparatus requiring the same. 
     Although an specific embodiment of the present invention, the advantages and applications of the same will be more clearly illustrated by means of the following examples, which are presented with illustrative but not limiting purposes. 
     EXAMPLES 
     For the execution of the examples, gases coming from various sources were treated in order to observe the effect that the combined system for the elimination of pollutants from gaseous effluents had over the generated gases, as well as the disadvantages of a combined system that does not incorporate the heat diffusion and molecular destabilization and the magnetic molecular rearrangement operations. 
     Following table 1 is presented, wherein the size of the peaks obtained in accordance with the results of a gas spectrophotometry, using a chromatographic column of the type PORAPAK-N@ 200C at the Nuclear Investigation National Institute (ININ), is shown. Chromatograms showing the presence of the various compounds before and after being treated by diverse methods were obtained. Likewise, the total amounts were determined by means of a column type AT-1000. 
     
       
         
           
               
               
               
               
               
               
             
               
                   
                   
               
               
                   
                 EXAMPLE 1 
                 EXAMPLE 2 
                 EXAMPLE 3 
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                 EXAMPLE 5 
               
               
                   
                   
               
             
            
               
                   
               
            
           
           
               
               
               
               
               
               
            
               
                 GASES 
                 Toluene 
                 Combustion 
                 Combustion 
                 Combustion 
                 Combustion 
               
               
                 ORIGIN 
                 Degradation 
                 of Gasoline 
                 of Gasoline 
                 of 
                 of 
               
               
                   
                   
                 Magna 
                 Magna 
                 Hydrosoluble 
                 Hydrosoluble 
               
               
                   
                   
                   
                   
                 Oil 
                 Oil 
               
               
                 SYSTEM 
                 Combined 
                 Combined 
                 Combined 
                 Combined 
                 System with 
               
               
                 EMPLOYED 
                 System of 
                 System of 
                 System of 
                 System of 
                 electronic 
               
               
                 FOR THE 
                 the present 
                 the present 
                 the present 
                 the present 
                 bombardmen 
               
               
                 TREATMEN 
                 invention 
                 invention 
                 invention 
                 invention 
                 t and 
               
               
                 T OF GASES 
                   
                   
                   
                   
                 electrostatic 
               
               
                   
                   
                   
                   
                   
                 filtration only 
               
               
                   
                 REDUCTION 
                 REDUCTION 
                 REDUCTION 
                 REDUCTION 
                 REDUCTION 
               
               
                 C1 
                 98.15% 
                 80.00% 
                 −6.25% 
                 N.D. 
                 N.D. 
               
               
                 C2 
                 99.62% 
                 79.00% 
                 73.53% 
                 N.D. 
                 N.D. 
               
               
                 C3&#39;s 
                 99.45% 
                 99.83% 
                 88.64% 
                 N.D. 
                 N.D. 
               
               
                 C4&#39;s 
                 96.55 
                 90.91% 
                 65.85% 
                 N.D. 
                 N.D. 
               
               
                 C5&#39;s 
                 97.06% 
                 98.86% 
                 82.09% 
                 N.D. 
                 N.D. 
               
               
                 C6&#39;s 
                 11.32% 
                 92.42% 
                 89.06% 
                 N.D. 
                 N.D. 
               
               
                 CO 2   
                 21.43% 
                 N.D. 
                 N.D. 
                 N.D. 
                 N.D. 
               
               
                 Others 
                 N.D. 
                 75.00% 
                 60.00% 
                 N.D. 
                 N.D. 
               
               
                 Total 
                 N.D. 
                 91.43% 
                 91.36% 
                 91.50% 
                 66.5% 
               
               
                   
               
               
                 Total = Percentage of diminishment of pollutants due to the treatment, as determined by means of column AT-1000.  
               
            
           
         
       
     
     Total=Percentage of diminishment of pollutants due to the treatment, as determined by means of column AT-1000. 
     As may be seen from table 1, by using the combined system of the present invention, it is possible to obtain the elimination of light hydrocarbons, as well as a decrease of pollutants in some cases of up to 91.50%. 
     Is important to stress the effect of the heat diffusion and molecular destabilization module, as well as of the magnetic molecular rearrangement module, which increase the pollutants removal, as shown in the results of examples 4 and 5. However, the preferred embodiment of the electronic bombardment barely achieves a reduction in 66.50% of pollutants. Nevertheless, it is evident to those skilled in the art that these results are better than those obtained up to the date by means of a prior art devices comprising electronic bombardment and electrostatic precipitation, due to the preferred voltages and current intensities used in example 5. 
     In accordance to the above description, it can be observed that both the combined system for the elimination of pollutants from gaseous effluents and the apparatus for the elimination of pollutants from gaseous effluents, have been designed for increasing in a great extent the efficiency of pollutants removal from gas effluents when using the electronic bombardment and electrostatic filtration techniques. It will be evident for those skilled in the art that the embodiments described herein before and illustrated in the enclosed drawings, are only illustrative but not restrictive of the present invention, since there are a lots of possible changes in its details without going beyond the scope of the invention. 
     Likewise, it is to be emphasized that there are possible many modifications to the invention as described and illustrated, such as different voltages, current intensities, or turbulence in the combined system for the elimination of pollutants from gaseous effluents, as well as of different construction materials, geometric shapes, energy sources and assembly embodiments for of each module that comprise the apparatus for the elimination of pollutants from gaseous effluents. The present invention, therefore, is not to be restricted except insofar as it is necessitated by the prior art and by the spirit of the appended claims.