Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
  • B03C3/02—Plant or installations having external electricity supply
  • B03C3/04—Plant or installations having external electricity supply dry type
  • B03C3/08—Plant or installations having external electricity supply dry type characterised by presence of stationary flat electrodes arranged with their flat surfaces parallel to the gas stream
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
  • B03C3/02—Plant or installations having external electricity supply
  • B03C3/04—Plant or installations having external electricity supply dry type
  • B03C3/12—Plant or installations having external electricity supply dry type characterised by separation of ionising and collecting stations
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
  • B03C3/34—Constructional details or accessories or operation thereof
  • B03C3/40—Electrode constructions
  • B03C3/41—Ionising-electrodes
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
  • B03C3/34—Constructional details or accessories or operation thereof
  • B03C3/40—Electrode constructions
  • B03C3/45—Collecting-electrodes
  • B03C3/47—Collecting-electrodes flat, e.g. plates, discs, gratings
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
  • B03C3/34—Constructional details or accessories or operation thereof
  • B03C3/86—Electrode-carrying means
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C2201/00—Details of magnetic or electrostatic separation
  • B03C2201/04—Ionising electrode being a wire
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
  • B03C2201/00—Details of magnetic or electrostatic separation
  • B03C2201/24—Details of magnetic or electrostatic separation for measuring or calculating parameters, efficiency, etc.

Definitions

• the present invention regards an electrostatic filter for purifying a flow of gas and in particular air, according to the preamble of the main independent claim.
• the electrostatic filter object of the present invention, is intended to be advantageously employed for removing, from a flow of gas or of a mixture of gases, such as air, suspended particles, whether these are constituted by inorganic material, fibers or even biological substances such as bacteria, molds, fungi, spores, viruses etc.
• the present electrostatic filter can be intended for multiple applications both in industrial and civil field; it can for example be employed in the civil field for purifying the air of residential buildings, or in industrial field in order to limit the levels of pollution by filtering the air expelled from production sites, or for treating gaseous flows of industrial processes.
• the filter, object of the present invention can be incorporated in a device for domestic use, or in an industrial plant of a production process.
• the present invention is therefore generally inserted in the field of production of apparatuses for removing pollutants from gaseous flows.
• suspended solid particulate is defined as the set of solid and liquid particles with diameter smaller than 100 ⁇ that remain in suspension in the air, including mechanical precipitators (such as cyclones), mechanical filters (such as hose filters) and electrostatic filters.
• the functioning principle of the latter provides for charging the particles suspended in the gaseous flow subjected to filtration, usually due to ionization caused by high voltages over filaments or networks of small-diameter filaments, and their subsequent capture on plates power supplied (or not) at a different potential, towards which the particles are directed by forces of Coulomb type produced by the electric field.
• Such principle therefore provides for the generation of an ionization field, susceptible of generating a flow of charges that charge the particles in suspension, and of an electric field susceptible of pushing the charged suspended particles towards at least one capture plate at a different potential with respect to the charged particles.
• the electrostatic filters are generally obtained in two different configurations, i.e.: the single- stage filters, in which the ionization electrodes for charging the particles are arranged in the space that separates the capture plates, hence being situated in the electric field susceptible of determining the capture of the particles; and the two-stage filters, in which the capture field is obtained from electrodes of different form and power supply with respect to the field responsible for the ionization.
• such configuration of electrostatic filter provides that the first stage, responsible for loading the particles, is constituted by a filament that is transversely crossed by the air flow, and that the second stage is instead constituted by parallel plates arranged longitudinal to the air flow, for example alternately placed at zero potential and at a potential with the same sign as that applied on the electrode in the first stage, so as to repel the loaded particles towards the capture plates with opposite sign.
• the claimed application takes under consideration electrodes charged with positive potential, generating lower concentrations of ozone in case of air filtration. In such condition, the atoms and molecules close to the electrode, previously neutral, lose electrons, becoming positive.
• the charges (hereinbelow, the term charges will indicate electrons and ions, not to be confused with the term particles which are those to be captured, suspended in the air), present in the area of the electrode, are accelerated to speeds such to cause the emission of further electrons and ions in the collision with other atoms or molecules, without losses of kinetic energy.
• the phenomenon occurs in a very thin layer around the electrode at high voltage, and proceeds in the creation of increasingly more charges which form a "crown" around the filiform electrode, even physically visible in the form of a weak bluish luminescence.
• the collisions between the electrons, gas molecules and positive ions produce the emission of light photons with specific wavelength, which in turn generates free electrons, thus participating in the ionization of the gas.
• An electric current is established between the plate at zero potential (grounded) and the filiform electrode (such current measurable in microamperes), as a function of the potential difference between the electrode and the grounded plate as well as of the environmental conditions. These environmental conditions actually affect the dielectric rigidity of the air, which in turn will have an impact on the intensity of the current made possible by the crown effect, which passes into the ionized air.
• the free electrons generated in the ionized layer are attracted towards the surface of the electrode, while the positive ions are repelled towards the plates at zero potential.
• the high speed of the electrons in the zone close to the electrode, and the consequent avalanche effect that is easily formed on the surface of the electrode facilitate the attainment of the limit condition which brings the field to trigger the crown effect. Consequently, gaseous ions are produced, and an ionization current is attained.
• the charges exiting from the ionization stage are repelled in the capture stage by the electric field in the direction of the collection plates, usually at zero potential.
• the charges in the inter-electrode space collide with the particles suspended in the transiting air flow, and are charged by these particles, creating charged particles subjected to the action of the present field which tends to repel them towards the collection plates.
• the original charge, along with the charge imparted by an ion, is not sufficient for ensuring an effective separation of the particles from the gas. Nevertheless, the particles can collect numerous ions; the particles being able to form an electric field capable of deflecting the original field lines. In such case, this is termed saturation charge, which increases with the particle size; in other words, notwithstanding the greater inertia, large particles can house greater charge and are thus subjected to higher forces (and efficiency).
• saturation charge which increases with the particle size; in other words, notwithstanding the greater inertia, large particles can house greater charge and are thus subjected to higher forces (and efficiency).
• the described phenomenon takes the name "field charging".
• the ions, being charged, precisely follow the force lines due to the electric field, except for the collisions with the gas molecules.
• the mechanisms for charging the particles coexist: while the field charging prevails in the case of particles with diameter greater than 0.5-1.0 ⁇ ⁇ ⁇ , the diffusion charging is the predominant mechanism for charging particles with diameter smaller than 0.1 -
• the capture of the charged particles that are still suspended in the gas is the second essential step of the filtration process.
• the following are present: the turbulent motion of the gas (on its own, it would have a small effect) and an electrostatic field capable of applying a force of Coulomb type.
• positive DC power supply is the most recommended for the lowest production of ozone physically possible with the containment of the electrons in the ionized layer and the lowest capacity of the positive ions to trigger reactions typical of ionization.
• the ozone generation is mainly determined from the equilibrium of the following reactions:
• M in the second reaction indicates a third molecule (e.g. present in the atmosphere, such as N 2 or 0 2 ), which transports away the excess energy and allows the ozone to remain intact.
• a third molecule e.g. present in the atmosphere, such as N 2 or 0 2
• the electrostatic filters present on the market do not contemplate an effective regulation of the filter operation parameters, adapted to avoid the onset of dangerous conditions due to the ozone emission; i.e. likewise, they do not provide for the possibility of an optimized operation, given the need to always maintain a safety margin.
• a further drawback lies in the space required for housing the two stages, which involves rather large bulk.
• An electrostatic filter is known from the patent US 3,664,092, for purifying a gas, or a mixture of gases, flowing inside the electrostatic filter itself and containing impurities.
• the electrostatic filter is provided with two electrodes at zero potential in perforated plate form, between which a negative electrode in perforated plate form is interposed. The electrodes are arranged orthogonal to the flow of the gas to be purified.
• a two-stage electrostatic filter is also known from patent WO 01/64349, for purifying a gas, or a mixture of gases, flowing inside the electrostatic filter itself and containing impurities.
• the electrostatic filter comprises a first ionization stage of the impurities contained in the gas, or in the mixture of gases, and a second stage of precipitation of the impurities.
• the first ionization stage is provided with at least one negative ionization with needle form, facing an electrode with zero potential in perforated plate or grating form.
• the electrodes of the first ionization stage are arranged orthogonal to the flow of the gas to be purified.
• the second precipitation stage is provided with at least one negatively-charged repulsion plate, facing at least one capture plate at zero potential.
• the repulsion plate and the capture plate of the second precipitation stage are arranged parallel to the flow of the gas to be purified.
• the patent US 2005/150384 describes an electrostatic filter of known type comprising a capture stage placed to intercept a gas flow and provided with multiple repulsion electrodes and with multiple collection electrodes parallel to each other, and power supply means adapted to charge each repulsion electrode to a negative potential with respect to the collection electrodes.
• the collection electrodes of the electrostatic filter are provided with sharp protuberances adapted to create, in the gas flow, turbulence zones and settling zones where the impurity particles suspended in the gas flow itself are accumulated.
• the repulsion electrodes are provided with openings arranged facing the protuberances of the adjacent collection electrodes, and adapted to facilitate a turbulent motion of the air flow and to avoid the formation of an excessive increase of the electric field at the edges of the protuberances of the collection electrodes.
• the latter solution of known type has drawbacks due to the non-optimal performances and to a high structural complexity.
• the problem underlying the present invention is therefore that of eliminating the problems of the abovementioned prior art, by providing an electrostatic filter for purifying a flow of gas and in particular air, which is capable of removing high quantities of particles from the gas flow, with high efficiency.
• Another object of the present invention is to provide an electrostatic filter for purifying a flow of gas and in particular air, which is capable of removing the particles with a high energy efficiency.
• Another object of the present invention is to provide an electrostatic filter for purifying a flow of gas and in particular air, which is entirely safe for the environment and for man, releasing zero ozone or in any case very low amounts of ozone.
• Another object of the present invention is to provide an electrostatic filter for purifying a flow of gas and in particular air, which is simple and inexpensive to make and entirely reliable in operation.
• Another object of the present invention is to provide an electrostatic filter for purifying a flow of gas and in particular air, which allows being employed in a versatile manner in different application settings, both for industrial processes and for apparatuses for civil use, such as for sanitizing the air of airflow ducts.
• Another object of the present invention is to provide an electrostatic filter for purifying a flow of gas and in particular air, which is capable of automatically maintaining the optimal operating conditions.
• Another object of the present invention is to provide an electrostatic filter, single or multiple stage, for purifying a flow of gas and in particular air, which is provided with a specific stage for eliminating the ozone, without causing load losses greater than those due to a stage constituted by capture and repulsion plates.
• FIG. 1 schematically shows the electrostatic filter, object of the present invention, in a first perspective view and in accordance with a possible embodiment thereof of two-stage type;
• FIG. 2 schematically shows an enlarged portion of the electrostatic filter of figure 1 , object of the present invention, in a second perspective view;
• FIG. 3A schematically shows the electrostatic filter, object of the present invention, in a third perspective view, with some parts in exploded view in order to better indicate other parts;
• FIG. 3B schematically shows a second embodiment of the electrostatic filter, object of the present invention, relative to a filter of single-stage type, with some parts in exploded view in order to better indicate other parts;
• figure 3C shows the electrostatic filter of single-stage type of figure 3B in assembled condition
• figure 3D shows the electrostatic filter of single-stage type of figure 3B. with the succession of plates schematically indicated;
• - figures 4 and 5 show two different lateral perspective views of a portion of the filter of figure 1 , object of the present invention, in which the means for supporting the different electrodes are visible and in with the perimeter edges are made in serrated form;
• - figure 6A shows a detail of the electrostatic filter, object of the present invention, relative to a perforated repulsion plate advantageously of the filter of two-stage type;
• FIG. 6B shows a detail of the electrostatic filter, object of the present invention, relative to a perforated repulsion plate advantageously of the filter of single-stage type;
• figure 7 shows an enlarged portion of the perforated repulsion plate of figure 6;
• FIG. 8 shows the circuit diagram of provided power supply means of the electrodes of the electrostatic filter, object of the present invention.
• an embodiment of an electrostatic filter, object of the present invention is indicated with the reference number 1 in its entirety, such filter being susceptible of purifying a gaseous flow indicated with F.
• the electrostatic filter 1 is adapted to be employed for purifying gaseous fluids, such as in particular air, removing contaminant particles from such fluids that are suspended therein.
• particles will generically indicate any contaminant present in a gaseous fluid F to be treated, which are capable first of being associated with charges and then being affected by the presence of an electric field.
• the contaminant particles will therefore comprise not only inorganic material and fibers, but also biological substances such as bacteria, molds, fungi, bacteria spores, fungus spores etc., hence both micro-pollutant substances in general and organic substances.
• the particles can have an intrinsic electric charge as well as be susceptible of being associated, in the filter 1 , with a charge, before then being affected by an electric field as indicated hereinbelow.
• the electrostatic filter 1 according to the present invention can also be obtained with a filter of single-stage type (of which only the overall view of figure 3B is provided) or of the type with at least three stages (three-stage or multi-stage), whose characteristics will be clarified hereinbelow,
• the electrostatic filter 1 of single- stage type only one capture stage S2 is present, given that the filter 1 lacks ionization electrodes, since the particular nature of the plate-like electrodes of the capture stage allows an efficient operation even without requiring an ionization stage and without the need for a final ozone removal stage.
• the provided power supply means of the plate-like electrodes of the capture stage allow maximizing the voltage on the same electrodes of such stage, also with the variation of the dielectric rigidity of the air.
• an ionization stage is present upstream of the capture stage.
• the power supply means voltage-drive the electrodes of such ionization stage in order to maintain a constant ionization current optimized for charging the particulate present in the air, without production of ozone or with a reduced production and within the limits of current law.
• the capture stage functions in the same way that the single-stage electrostatic filter functions, but the presence upstream of the ionization stage allows reducing the size and bulk of the plate-like electrodes of the capture stage.
• the operation is analogous to that of the filter of two-stage type, with the further presence of a final stage of ozone removal placed downstream of the capture stage, which causes extremely small load losses upon the passage of the air and a complete removal of the ozone.
• the electrostatic filter 1 is generally adapted to operate for purifying gaseous fluids of industrial processes and for purifying air in particular of airflow networks for civil use.
• the electrostatic filter 1 object of the present invention, comprises, in a per se known manner, at least one capture stage S2, which is placed to intercept the gas flow F that proceeds in an advancement direction, and is provided with at least one plate-like repulsion electrode 5 and with at least one plate-like collection electrode 6.
• Such electrodes 5, 6 are arranged parallel to each other and in a manner substantially parallel to the advancement direction of the gas flow F.
• the plate-like repulsion electrodes 5 and the plate-like collection electrodes 6 have plate form, in particular each being provided with two corresponding flat faces.
• the plate-like repulsion electrodes 5 delimit, with the plate-like collection electrodes 6 adjacent thereto, passage channels which are extended along an extension direction thereof with constant thickness. Through such passage channels, the gas flow F is susceptible of passing, with its advancement direction parallel to the extension direction of the passage channels themselves.
• each passage channel is defined by the distance between the face of the corresponding plate-like repulsion electrode 5 and the face of the plate-like collection electrode 6 arranged facing the aforesaid face of the plate-like repulsion electrode 5 itself.
• the electrostatic filter 1 then has power supply means adapted to supply such electrodes 5, 6 with a DC direct voltage potential difference, charging the plate-like repulsion electrode 5 to a positive potential V2 with respect to the plate-like collection electrode 6, preferably placed at ground potential, naturally determining the formation of an electric field between the aforesaid two electrodes.
• each plate-like repulsion electrode 5 is provided with a plurality of holes 12 preferably uniformly distributed in at least one area opposite the plate-like collection electrode 6.
• edges of connection of the aforesaid holes 12 with the two faces of the repulsion plate 5 have radii of curvature with localized concentrations of the electric field with consequent emission of positive electric charges 4 in the gas flow F, which participate in the ionization of the particles suspended in the same gas flow F.
• the plate-like collection electrodes 6 lack holes and are thus solid, with their surface substantially lacking interruption.
• the holes 12 of the plate-like repulsion electrode 5 are arranged facing corresponding solid areas of the collection electrode 6.
• the plate-like repulsion electrode 5 repels, towards the plate-like collection electrode 6, the impurity particles present in the gas flow F and which were positively charged, at least partially also with the positive electric charges 4 emitted by the edges of the plurality of holes 12.
• edges of the holes 12 therefore act as optimal field concentrator, locally at points distributed on the surfaces of the plate-like repulsion electrodes 5, capable of locally emitting charges and supplying the process, above all the field charging of the particles suspended in the gas flow F.
• Capture efficiency obtained by only power supplying the plates in two prototypes, one with perforated plates and one with solid plates, at two voltage levels, one below the trigger voltage and one close to discharge.
• the perforated plates have a higher efficiency, up to 10% higher than the solid plates due to the shape of the edges of the holes 12.
• the edges of the holes 12 create zones of localized and concentrated field in the aforesaid capture stage S2.
• This concentration of the electric field is not sufficient for producing ozone but is sufficient for creating a field charging greater than the case with the solid plates.
• these points of concentrated and localized field are numerous and distributed (preferably in a uniform or otherwise random manner) on the surface (over most of the surface) and in particular at the center of the repulsion plates 5. From the obtained results, it is inferred that the largest particles, also considering the statistical validity of the results, are those which are more greatly affected by the variation of the force due to the holes 12, as would be expected if the effect was actually due to the phenomenon of field charging in the capture stage S2.
• the holes 12 of the aforesaid plurality of holes therefore have for such purpose the edges with sufficiently small curvature radius, so as to allow locally concentrating the electric field to a value sufficient for generating charges but insufficient for generating micro-discharges such to produce ozone.
• the holes 12 can have, at their edge on at least one of the two faces of the repulsion plate 5, a projecting lip orthogonal to the surface of the same repulsion plate 5 susceptible of further concentrating the electric field to a value capable of generating charges.
• Such lip will be easily obtained by means of punching the repulsion plates 5 and due to the action of deformation of the punch, which projectingly pushes the metal of the plate 5 orthogonal to its lying plane.
• the aforesaid holes 12 have circular form with diameter comprised between 1 and 10 mm and advantageously substantially around 3 mm.
• the holes 12 of the plate-like repulsion electrode 5 have equilateral triangle arrangement.
• the holes 12 of the plate-like repulsion electrode 5 define, in the latter, a solid over void ratio comprised between 2 and 5.
• Such solid over void ratio corresponds with a configuration of the edges of the holes 12 (obtained in the plate-like repulsion electrode 5) that involves electric field concentrations such to emit positive charges 4 in an amount such to charge the impurity particles suspended in the gas flow F.
• the aforesaid solid over void ratio corresponds to a number (or a density) of holes 12 of the plate-like repulsion electrode 5 such that the edges of the holes 12 have overall length which causes field concentration sites distributed over a significant area of the platelike repulsion electrode 5 itself.
• the holes 12 of the plate-like repulsion electrode 5 are organized in a plurality of rows, in particular with a dense distribution in the corresponding area of the plate-like repulsion electrode 5 itself.
• the positive potential V2 to which the plate-like repulsion electrodes 5 are charged is in any case less than the avalanche discharge trigger value in the gas flow F in order to prevent the formation of ozone, though it can still be sufficient for triggering crown effect phenomena.
• the repulsion electrodes 5 ionize the air due to the holes 12, creating a flow of positive charges which are directed towards the grounded collection plates 6.
• such particles collide with particles suspended in the air or with molecules constituting the air itself, electrically charging them so as to be able to apply thereon the Coulomb force due to the electric field.
• the collection plates 6 are metal plates placed at zero potential so as to generate an electrostatic field that attracts the impurities present in the air, once they have been positively charged due to the flow of charges also exiting from the repulsion electrodes 5; such impurities, which are accumulated on the collection plates 6, must therefore be periodically removed so as to maintain the filter 1 performance and hygiene levels.
• the electrostatic filter 1 object of the present invention, also comprises at least one ionization stage S I , which is placed to intercept the gas flow F, upstream of the aforesaid capture stage S2, and is provided with at least one ionization electrode 2 and with at least one opposite field concentration electrode 3.
• Such electrodes 2, 3 are power-supplied with a DC direct voltage potential difference with the ionization electrode 2 to a positive potential V I , and the field concentration electrode 3 to a lower potential, preferably at ground potential.
• the ionization electrode 2 is at a positive potential VI greater than the potential V2 of the plate-like repulsion electrode 5.
• the function of the ionization electrodes 2, as the name suggests, is that of ionizing the air in a layer of thin thickness close to the electrode.
• Such ionization known as crown effect, creates a flow of charges of the same sign of the electrode potential which are directed towards the grounded collection plates 6 such that, if in their path of travel they collide with particles suspended in the air or with molecules constituting the air itself, these are electrically charged and the Coulomb force due to the electric field can be applied thereon.
• the collection plates 6 are solid metal plates placed at zero potential, so as to generate an electrostatic field that attracts the impurities present in the air once they have been charged due to the flow of charges also exiting from the ionization electrode 2; such impurities that are accumulated on the collection plates 6 must therefore be periodically removed, so as to maintain the filter 1 performance and hygiene levels.
• aluminum collection plates with 0.5 mm thickness can be employed.
• the electrical continuity between the collection plates 6 can be ensured by rods 7 which also act as support in order to provide strength to the structure, as better specified hereinbelow.
• Such embodiment is in any case subjected to variations, which all have the same object of maintaining an electrical continuity between all the repulsion plates 5, different from that for the collection plates 6 which are also maintained at an identical ground potential, or with potential of opposite sign with respect to the repulsion potential.
• the positively-charged, metal perforated repulsion plates 5 are interposed between two collection plates 6, preferably at ground potential, and have the function of repelling the positively-charged particles towards the collection plates 6, facilitating the capture thereof: the same potential in fact allows obtaining a field with the same direction as the field created by the ionization electrode 2.
• the potential V2 of the repulsion plate 5 has the same positive polarity as the potential of the ionization electrode 2 in order to repel, towards collection plate 6, the impurity particles charged both with the charges 4 emitted by the ionization electrode 2 and with the charges 4 emitted by the edges of the holes 12 of the repulsion plate 5.
• the ionization electrode 2 comprises at least one wire made of conductive material, arranged transverse to the air flow F opposite the field concentration electrode 3 formed by at least one metal plate parallel to the repulsion plate 5 and to the collection plate 6.
• the plates of the field concentration electrodes 3, repulsion plate 5 and capture plate 6 are all obtained (both in the embodiment of single-stage type and in that of multiple-stage type) with metal blades, preferably made of aluminum, with thickness of about 0.5 mm, equidistant from each other and which are sequentially repeated in order to suitably treat an air flow F.
• the plates of the same type are electrically connected together by means of rods 7, 7 which simultaneously act as support and as spacers, and which traverse the plates of different type due to holes 8 provided therein in order to be mechanically connected to the ends of the support structure 20 of the electrostatic filter 1.
• end plates 60 are provided at ground potential, in order to keep the plates assembled together, and tie rods 61 are provided that are connected to the support structure 20 in order to compact the plate assembly.
• the filiform ionization electrodes 2 may be provided, mainly due to production costs, only for each group of multiple plates, repulsion 5 and capture 6 plates, since they are able to generate charges susceptible of traversing the multiplicity of chambers defined between the aforesaid pairs of repulsion 5 and capture 6 plates.
• the ionization electrodes 2 will be advantageously obtained with tungsten wires with diameter equal to 0.1 mm - 0.5 mm.
• the ionization electrodes 2 of filiform type are visible.
• the latter are mechanically connected to the support structure 20 through coupling means advantageously comprising a pair of transverse rods 9, supporting the terminals 10 of the wires 2 that are arranged taut through the springs 1 1.
• power supply means comprising two separate power supplies, in order to power supply the ionization electrodes 2 at the positive operating potential V I with respect to the field concentration electrodes 3 placed at the ground potential and in order to power supply the repulsion plates 5 at the positive operating potential V2 with respect to the collection plates 6 also placed at the ground potential.
• the power supply means thus comprise a first power supply 13, which is current-driven in order to power supply the ionization electrode 2 at the aforesaid operating potential V I , which will be varied in order to maintain the ionization current I I at a value lower than a preset Imax, capable of preventing an excessive formation of ozone, and advantageously comprised between two preset values Imin and Imax.
• the power supply means also comprise at least one second power supply 14, which is voltage-driven in order to power supply the repulsion plate 5 at an operating potential V2 which will be varied so as to maintain the maximum possible potential without triggering discharges between the plates 5 and 6 of the capture stage S2.
• the potential VI is selected for example with value higher than the crown effect trigger voltage for a considerable production of charges 4 in the gas flow F, but with value lower than the avalanche effect trigger potential which would lead to a consequent high production of ozone.
• the first power supply 13 applies a potential VI to the ionization electrodes 2, as seen preferably filiform and made of conductive material, capable of bringing field concentrations (dependent on the specific configuration of electrodes and on the specific environmental conditions) susceptible of triggering the crown effect, without pushing this potential to levels corresponding to a production of ozone, or an excessive production of ozone.
• a weak electric current is generated in the gas flow F which traverses the electrostatic filter, such current made possible by the ions generated by the same crown effect.
• This current is itself a source of ion generation in the air, and hereinbelow is termed with the expression ionization current I I .
• the electrode 2 is the stressed electrode or ionization electrode.
• the potential V I must be regulated in order to allow attaining the ionization current II and maintaining it stable below a value that does not produce ozone, or which does not cause the avalanche discharge effect.
• This ionization current 11 stable, it is possible to maximize the filtration efficiency, even with the variation of the dielectric rigidity of the gas that transits in the filter, for example caused, in the case of air, by the variation of the humidity level, by the pressure, by the temperature and by the presence of gaseous ions.
• the driving of the first power supply 13 is aimed to maintain the ionization current II at a specific level, and to stably keep it at this level, even if there is a change of the physical conditions (temperature, pressure, humidity, load of ions, etc.) of the gas that traverses the filter, and at a level where ozone is not produced.
• the physical conditions temperature, pressure, humidity, load of ions, etc.
• the ionization current II could decrease for a specific potential difference V I .
• the first power supply 13 will then automatically react, increasing the potential V I in a manner so as to re-establish the current II to the preset level, while not exceeding a dangerous value for the production of ozone. This characteristic therefore allows maintaining the filtration efficiency constant, maintaining constant the generation of ions in the air to be filtered.
• the described control and procedure can be obtained with a very low cost and with a very simple algorithm, such that it can also be obtained in an analogue manner.
• the possibility of considering, in the control algorithm, also other parameters such as the environmental state (temperature, pressure, humidity, etc.) and state of the air (concentration of ozone, C02, etc.) in any case leads to the preference for the electronic-digital control, where sensors for the abovementioned quantities can be easily integrated.
• a control on the current also allows monitoring other parameters necessary for the good operation of the filter and of the associated electronics such as:
• the discharge is in fact identified by a sudden current increase: monitoring the current, e.g. above a certain threshold, signifies knowing when and how many discharges have been verified. In the presence of the discharge, it is possible to reduce the electrode voltage and bring the current to lower values where the discharge does not occur;
• the second power supply 14 of the power supply means is employed in the capture stage S2 and is adapted to maintain the voltage V2 on the plate-like repulsion electrodes 5 at the maximum possible potential, without triggering electrical discharges between repulsion 5 and capture 6 plates, thus optimizing the capture efficiency.
• the driving of the operating voltage V2 for this second power supply 14 is based on the detection of the voltage between the platelike repulsion electrodes 5 and the grounded capture electrodes 6, maintaining it below a presettable maximum potential V2max.
• the potential V2 is for such purpose modulated so as to be fixed each time on the maximum possible voltage, without causing electrical discharges between repulsion plates 5 and grounded collection plates 6.
• the attainment of the maximum possible voltage, as a function of a specific dielectric rigidity of the air, which is subjected to variations during the day according to the current environmental conditions, allows maintaining the filter efficiency always at the maximum, with regard to the removal of particulate from the air.
• the second power supply 14 regulates the voltage V2 by means of feedback on the stability of the current 12, i.e. over the time progression thereof; as soon as micro-discharges are detected with unstable progression with little current peaks, the voltage V2 on the repulsion plates 5 is lowered.
• the voltage V2 is then automatically regulated through a control board that sets the current 12 at a level just lower than that susceptible of generating the maximum V2, at which the discharges occur.
• the holes 12 of the perforated repulsion plates 5 do not cause any increase of ozone.
• the repulsion plate 5 is power-supplied at an operating potential V2 less than 6 V (and preferably less than 5.5 KV) with distance between the repulsion plates 5 and the collection plates 6 of less than 5 mm.
• the operating potential V2 of said repulsion plate 5 will also be substantially preferably in the order of magnitude of half the operating potential VI applied to the ionization electrode 2.
• the synergy between two modulation mechanisms, on V I and V2, allows maintaining the efficiency of the filter 1 at maximum levels, in any environmental conditions.
• the electrostatic filter 1 also comprises a third stage for removing the ozone S3 provided with reducing means 40 constituted by plates substantially parallel to the advancement direction of said gas flow (F) and placed to intercept the air flow F downstream of the capture stage S2 in order to reduce the ozone present in the air flow F.
• reducing means 40 constituted by plates substantially parallel to the advancement direction of said gas flow (F) and placed to intercept the air flow F downstream of the capture stage S2 in order to reduce the ozone present in the air flow F.
• Ozone is a very reactive and highly oxidizing gas, reason for which it is dangerous; by placing it in contact with a good reducing agent, it reacts and disappears from the gases that exit from the filter.
• coal has been advantageously selected, in the form of graphite plates with which it is possible to construct a third stage, connected in cascade to the second stage.
• the ozone possibly produced in the first stage and possibly in extremely small (or zero) quantities by the holes of the second stage, would pass, after having been recombined to minimum extend, into the third stage where the presence of the coal-based reducing agent would transform it into C0 2 .
• a very low electric potential may be applied on the coal plates, which in such a manner are able to change the outcome of the reaction with the ozone from carbon dioxide to oxygen.
• the relatively low concentration of ozone to be removed would ensure the operation of the third stage for various months before being substituted, thus allowing the optimization of the ordinary maintenance interventions.
• the electrostatic filter 1 can be constituted in accordance with a first embodiment of the invention, by a single capture stage S2, with perforated repulsion plates 5 and with a single power supply which will drive the positive voltage V2 on the same perforated plates.
• Said plates 5 for this particular single-stage embodiment will have to have size greater than that of a multi-stage filter, in order to compensate for the absence of the ionization stage in the production of positive charges.
• the electrostatic filter 1 can be constituted in accordance with a second embodiment of the invention, by two stages including an ionization S 1 and a capture S2 stage, both power-supplied by separate power supplies controlled in a different manner as expressed above, in order to minimize the production of ozone in the ionization stage and maximize the repulsion force on the charged particles in the capture stage.
• the electrostatic filter 1 can comprise, in accordance with a third embodiment, also a third stage for removing the ozone, advantageously placed downstream of the capture stage, mainly in the case of the simultaneous presence of an ionization stage upstream, but, in the more general case, simply provided downstream of the capture stage even if the latter is not preceded by the ionization stage.
• electrostatic filter 1 in the practical achievement thereof, can also assume shapes and configurations that are different from that illustrated above, without departing from the present protective scope.

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• 2015
  • 2015-10-08 EP EP15798543.3A patent/EP3204164B1/en active Active
  • 2015-10-08 CN CN201580066430.6A patent/CN106999949B/zh active Active
  • 2015-10-08 WO PCT/IB2015/001862 patent/WO2016055850A1/en active Application Filing

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