GB1591826A - Focusing electrodes for high-intensity ionizer stage of electrostatic precipitator - Google Patents

Abstract

A gas ioniser unit having two coaxially arranged electrodes (27, 50) for generating a highly intensive electrical field (56) transversely through the flow path (arrow) of a gas loaded with solid particles is arranged upstream of an electrostatic particle precipitator. The ioniser anode is formed by a Venturi diffuser (27) through which the gas flows immediately prior to its entry into the particle precipitator. The ioniser cathode is formed by a disc-shaped discharge electrode (50) which is mounted coaxially in the taper of the Venturi diffuser (27) and has a rounded edge. A source of high voltage located between the Venturi diffuser and the discharge electrode causes a corona in the annular region between the edge of the discharge electrode (50) and the cylindrical inner surface (52) of the Venturi diffuser surrounding said discharge electrode. Focusing electrodes (53, 54) at cathode potential are provided on both sides of the discharge electrode, in order to reinforce the electrical field (56) between the said inner surface of the Venturi diffuser and the discharge electrode. As a result, the width of the surface, of the discharge electrode (50), which is subjected to the corona flow and on which particles can settle, is reduced, thus making the cleaning of the discharge electrode (50) easier. <IMAGE>

Description

(54) FOCUSING ELECTRODES FOR HIGH-INTENSITY IONIZER STAGE OF ELECTROSTATIC PRECIPITATOR (71) We, ELECTRIC POWER RE SEARCH INSTITUTE, INC., a Corporation organized under the laws of the District of Columbia, United States of America, of 3412 Hillview Avenue, Palo Alto, State of California, United States of America, do hereby declare the invention, for which we pray that a patent may be granted to us, and the method by which it is to be performed, to be particularly described in and by the following statement:- The present invention relates to highintensity ionizers which pre-charge particulate matter entrained in a contaminated gas stream prior to removal of the charged particles from the stream by electrostatic precipitation.More specifically, the invention is directed to an improved electrode configuration for a co-axial venturi ionizer wherein focusing electrodes limit the width of the current flux band upstream and downstream of the plane of the ionizer discharge electrode.

Standards for emissions of particulate in flue gases issuing from coal fired electrical power station stacks are becoming increasingly more stringent. Current air quality standards require that more than 99% of the fly ash produced by burning coal be removed prior to discharge of the combustion gases from the stack. Thus, the efficiency of particulate collection must increase in proportion to the ash content of the coal. In addition, in an effort to reduce the emission of certain gaseous pollutants, particularly the sulfur oxides, it has become increasingly necessary to use low sulfur coal in electrical power generating plants.

The - The electrostatic precipitator is the most commonly used device for the removal of particulate matter from power station stack gases. Because the size of an electrostatic precipitator is determined by the efficiency of fly ash removal required, an increase in required fly ash collection efficiency requires a corresponding increase in equipment size and cost. Moreover, because fly ash resistivity tends to be inversely related to the level of combustible sulfur in the coal burned, the use of low sulfur coals to directly reduce gaseous sulfur oxide emissions, produces highly resistive dusts. It has been demonstrated that the size of the electrostatic precipitator necessary to achieve a given level of collection efficiency increases with increasing electrical resistivity of the fly ash. The use of low sulfur coals therefore further increases the size and cost of the precipitator.

Recently, high-intensity ionizers have been developed in which a unique electrode geometry produces a stable high-intensity corona discharge through which the particulate-laden gas is passed. The ionized flue gases produced charge the particulate matter to a much higher level than is achievable with a conventional electrostatic preciptator. When the ionizer is followed with an electrostatic precipitator, the higher particle charge results in a higher collection efficiency in the precipitator due to higher migration or particle drift velocity. In such a two-stage arrangement, the ionizer acts as the charging stage and the precipitator serves as the collecting stage.

Such high-intensity ionizers utilize a coaxial pair of electrodes to generate a highintensity field expanding radially and axially parallel to the direction of gas flow. The anode in such an arrangement typically takes the form of a venturi diffuser through which the stack gases flow immediately prior to entering the precipitator stage. The cathode is a disc co-axially mounted within the venturi throat and is formed with a curved peripheral edge having a radius much smaller than the inner radius of the venturi. When a high voltage power supply is connected between the anode and cathode, a high-intensity corona discharge is established in an annular region between the arcuate periphery of the cathode disc and the surrounding cylindrical anode surface near the disc.Because the field is relatively narrow in the direction of a gas flow, a high intensity field is achievable without prohibitive electrical power requirements.

The combination of the high gas stream velocity through the venturi and the high intensity transverse electric field through which the gas stream passes produces intense ionization and very high levels of charge on the particles and results in increased collection efficiency notwithstanding the high resistivity of the particulate as in the case of fly ash from low sulfur coal.

One of the problems which has been encountered in connection with co-axial high intensity ionizers of the type described above results from the detrimental build-up of charged particles on the cylindrical anode wall near the corona discharge plane. Deposition of high resistivity particulate matter in this region results in the phenomena of back corona and excessive sparking with a resulting deterioration in the applied electric field and attendant degradation in particle charging efficiency.

Prior attempts to overcome this problem have involved "cleaning" the anode surface in the affected region to eliminate disturbances in the corona due to contaminate build-up on the outer electrode. One form of anode cleaning involves the injection of clean gas into the venturi in the corona discharge region to form a protective barrier between the anode wall and the charged particles in the gas stream.

One particularly effective clean gas injection system is described in co-pending patent application Serial No. 44277/77 (Serial No.

1,591,827) filed 25th October 1977.

According to the present invention there is proposed a high-intensity gas ionizer, for use with an electrostatic precipitator, comprising at least one venturi diffuser having an inlet connected to a source of particulate laden gases and an outlet connected to said electro static precipitator, a discharge electrode comprising a cathode disc having an arcuate periphery and being co-axially mounted within said venturi diffuser, voltage generating means interconnected between said discharge electrode and said venturi diffuser to establish a high intensity electric field within said venturi diffuser across the path of said particulate laden gases flowing therethrough, and corona discharge focusing electrodes situated adjacent the upstream and downstream sides of said discharge electrode, wherein said corona dis charge focusing electrodes are maintained at an electrical potential approximately the same as that of said discharge electrode, and each comprises a cylindrical member coaxial with, and of smaller outer diameter than, the cathode disc, and is adapted to limit the width of the corona discharge in the direction of flow of said particulate laden gas and hence the surface area of said venturi diffuser subjected to deposition of particulate from said gases.

In a high intensity gas ionizer as aforesaid, for use with an electrostatic precipitator, a method comprising the steps of generating a high intensity electrical field within said venturi diffuser across the path of particulate laden gases being passed therethrough and limiting the width of the corona discharge, and hence the surface area of said venturi diffuser subjected to deposition of particulate from said gases, by generating an additional field on the upstream and downstream sides of said discharge electrode.

In the drawings: Fig. 1 is a schematic side elevational view illustrating a multi-stage electrostatic precipitator incorporating a high-intensity ionizer according to the present invention; Fig. 2 is an enlarged side view of one ionizer stage of the apparatus of Fig. 1 partially broken away to show the ionizer array; Fig. 3 is an end elevational view of the ionizer stage of Fig. 2 with the inlet partially broken away to show the ionizer array; Fig. 4 is an enlarged partial sectional view of a single ionizer venturi illustrating the electrode arrangement.

Turning now to the drawings, Fig. 1 shows in schematic side elevational view an electrostatic precipitator system incorporating the invention. As seen in this Fig., the precipitator system includes a gas inlet 11 into which gases to be cleaned are directed as suggested by arrow 12, a gas outlet 13 from which cleaned gases are supplied to appropriate downstream apparatus, e.g. an atmospheric discharge duct, as suggested by arrow 14, and typically a cascaded pair of ionizer-precipitator units generally designed by reference numerals 15, 15'. Each ionizer-precipitator unit 15, 15' includes an ionizer stage 16 (16') and typically a pair of conventional electrostatic precipitators 17, 18 (17', 18').Each ionizer stage 16, 16' and precipitator stage 17, 17', 18, 18' is provided with a high voltage input connector 19 coupled to a suitable source of high voltage as described more fully below and a collecting bin portion 20 for collecting particulate matter precipitated from the gas as the latter flows through units 15, 15'.

In operation, gases containing particulate matter enter the Fig. 1 apparatus via inlet 11 and pass through the first ionizer stage 16 in which the particles in the gas are electrostatically charged. The gas bearing the electrostically charged particles next flows into successive precipitator stages 17, 18 in each of which the charged particles are deflected out of the flow path of the gas under the influence of an electrical field established across the flow path, the particles being deposited in the bin portions 20 of the precipitator stages 17, 18. The gas exiting from precipitator 18 is passed through ionizer stage 16', and precipitator stages 17', 18', to provide additional cleaning therefor, and the cleaned gases emerging from precipitator stage 18' are conducted via gas outlet 13 to appropriate downstream apparatus.

Figs. 2 and 3 typically illustrate the gas inlet 11 and the first ionizer stage 16 with more detail. As seen in these Figs., gas inlet 11 comprises a hollow conduit of trapezoidal or other suitable geometric configuration which is coupled at the downstream side to a gas distributor portion 22. Distributor portion 22 is coupled to an entry chamber 23 formed within the housing of ionizing unit 16 by the side and bottom walls thereof and a vertically arranged bulkhead 24.

positioned within ionizer stage 16 in a regular array are a plurality of venturi diffusers 27 and associated central electrode support members 28 each projecting into either end of the associated venturi 27 (shown here upstream) and substantially coaxially therewith.

Each member 28 is coupled to a bus bar network generally designated by reference numeral 29 and consisting of vertically arranged parallel bus bars (three shown here) interconnected at the upper end thereof by a common bus bar element 31, the element 31 being connected to a single bus bar element 32 extending from the interior of ionizer stage 16 to an external conventional high voltage connector shroud 33 to which a high voltage is supplied from a suitable power source (not shown) via high voltage connector 34. The downstream end or outlet of each venturi 27 is coupled to an exit chamber 36 which is in turn coupled to the inlet of electrostatic precipitator stage 17.

Storage bin 20 is provided with a removable door 40 for purposes of inspection and cleaning, and a vibrator bracket 41 for permitting the use of an optional conventional vibrator to assist in settling any particulate matter collecting in bin 20 towards the bottom edge 42 thereof. Bottom edge 42 is provided with suitable apertures (not shown) for enabling the particulate matter to be removed from the bin 20 in a conventional manner. Bins 20 of the remaining system elements 16', 17, 17', 18, and 18' are configured in a substantially identical manner.

Each venturi element 27 and associated coaxial member 28 generally comprises an electrode pair for generating a high intensity electric field across the path of gas flow through the ionizer stage 16. For this purpose, an electrode (described below) is carried by each member 28 and is coupled to a source of relatively high negative potential, via bus bar network 29 while each venturi conduit 27 is coupled via the framework of the structure to ground potential. Thus each venturi 27 serves as an anode and each member 28 serves as a cathode support.

In operation, with high voltage applied between the cathode and anode, particles suspended in any gas flowing through the ionizer stage 16 are electrostatically charged when passing through the throat of venturi 27.

In order to ensure that substantially all charged particles remain suspended in the flowing gas until arriving at the downstream precipitator 17 or 18, and do not adhere to the ground potential anode surface, the novel electrode configuration shown in Fig. 4 is employed.

With reference to Fig. 4, each venturi element 27 is formed with an inwardly tapering conical inlet section 45, a generally cylindrical central section or throat 46 and an outwardly tapering conical outlet portion 47.

The cathode includes a conducting disc 50 having a curved peripheral edge which projects outwardly from the outer surface of member 28. Disc 50 is mounted substantially coaxially in the throat of venturi 27 and provides a highly constricted high-intensity electric field in the form of a corona discharge between the curved periphery of disc 50 and the surrounding anode surface 52 when a high potential is applied.

Mounted on either side of cathode disk 50 are focusing electrodes 53 and 54. These electrodes are preferably of cylindrical crosssection and are co-axial with cathode disk 50.

Electrodes 53 and 54 are mounted to be in electrical contact with cathode disc 50 and thus are at cathode potential. Upstream focusing electrode 53 may be formed by appropriately sizing electrode support member 28 and maintaining electrical continuity between cathode disc 50, member 28, and bus bar 29. In this case, the downstream end of support member 28 functions as the upstream focusing electrode 53. Downstream focusing electrode 54 may be formed as an extension of support member 28 which extends a sufficient distance downstream of cathode disk 50 and is preferably terminated by a hemispherically shaped end surface 54a. Electrode 54 may be attached to electrode 53 by a threaded stud projecting from electrode 54 and passing through the center of cathode disc 50 into support member 28.

Focusing electrodes 53 and 54 increase the strength of the electric field at the fringes of the discharge current flux band (indicated at 56) upstream and downstream of the ionizer discharge plane. The increased electrical field in these areas drives the ions to the anode with higher velocity. Therefore, the ions migrate less upstream and downstream in their expansion by mutual repulsion. The net effect is that the width of the current flux band impinging on the anode surface is reduced substantially and the amount of anode surface which must be cleaned is similarly reduced. This in turn reduces cleaning gas requirements and results in an overall increase in particulate collection efficiency.

Focusing electrodes 53 and 54 extend upstream and downstream from cathode disc 50 a distance approximately equal to the interelectrode separation between the periphery of cathode disc 50 and the surrounding anode wall. For purposes of the invention, the focusing electrode cylinders can be terminated beyond that distance if desired such as by hemispherically capping the downstream cylinder 54 as described above to prevent corona leakage there, however, extension of the electrode beyond that distance will still pro vide satisfactory results as indicated by the fact that the physical structure of electrode 53 is formed in the depicted embodiment by cathode support element 28 which extends out of the inlet side of venturi 27 terminating at bus bar 29.

The diameter of the focusing electrode cylinders is preferably between 0.2 and 0.4 of the inside diameter of the anode surface surrounding cathode disk 50. If the diameter is larger or smaller the electric field at the focusing electrode surface is increased promoting surface corona leakage. However, even outside the preferred range, focusing electrodes of the present invention provide improved performance as compared with prior art devices not employing such electrodes.

While a preferred embodiment of the present invention has been shown and described above, it will be readily apparent to those skilled in the art that numerous modifications and adaptations thereof may be made.

WHAT WE CLAIM IS:- 1. A high-intensity gas ionizer, for use with an electrostatic precipitator, comprising at least one venturi diffuser having an inlet connected to a source of particulate laden gases and an outlet connected to said electrostatic precipitator, a discharge electrode comprising a cathode disc having an arcuate periphery and being co-axially mounted within said venturi diffuser, voltage generating means interconnected betweeen said discharge electrode and said venturi diffuser to establish a high-intensity electric field within said venturi diffuser across the path of said particulate laden gases flowing therethrough, and corona discharge focusing electrodes situated adjacent the upstream and downstream sides of said discharge electrodes, wherein said corona discharge focusing electrodes are maintained at an electrical potential approximately the same as that of said discharge electrode, and each comprises a cylindrical member coaxial with, and of smaller outer diameter than, the cathode disc, and is adapted to limit the width of the corona discharge in the direction of flow of said particulate laden gas and hence the surface area of said venturi diffuser subjected to deposition of particulate from said gases.

2. A gas ionizer as claimed in claim 1 wherein one of said focusing electrodes comprises a support member co-axially mounted with said venturi diffuser and having said discharge electrode mounted thereon.

3. A gas ionizer as claimed in claim 2, wherein the other of said focusing electrodes is an extension of said support member, said extension passing through said cathode disc and terminating downstream thereof in a hemispherical cap.

4. A gas ionizer as claimed in any one of claims 1 to 3 wherein the diameter of said focusing electrodes is between 20% and 40% of the inside diameter of the venturi diffuser surface surrounding said discharge electrode, but less than the diameter of said discharge electrode.

5. A gas ionizer as claimed in any one of claims 1 to 4, wherein said focusing electrodes extend on either side of said cathode disc a distance at least equal to the distance between the disc periphery and the surrounding venturi diffuser surface.

6. A gas ionizer as claimed in any one of the preceding claims, further comprising a plurality of individual venturi diffusers arranged in an array with their axes aligned and their inlets connected to said source of particulate-laden gases, each of said venturi diffusers being provided with associated corona current focusing electrodes.

7. A high-intensity gas ionizer, for use with an electrostatic precipitator, substantially as hereinbefore described with reference to and as illustrated in the various figures of the accompanying drawings.

8. An electrostatic precipitator in combination with a high intensity gas ionizer as claimed in any one of the preceding claims.

9. In a high-intensity gas ionizer according to claim 1, for use with an electrostatic precipitator, a method comprising the steps of generating a high intensity electrical field within said venturi diffuser across the path of particulate laden gases being passed therethrough and limiting the width of the corona discharge, and hence the surface area of said venturi diffuser subjected to deposition of particulate from said gases, by generating an additional electrical field on the upstream and downstream sides of said discharge electrode.

10. In a high-intensity gas ionizer according to claim 1 for use with an electrostatic precipitator, a method of limiting the width of the corona discharge and hence the surface area of the venturi diffuser subjected to particulate deposition substantially as hereinbefore described with reference to and as illustrated in the various figures of the accompanying drawings.

**WARNING** end of DESC field may overlap start of CLMS **.

Claims (10)

**WARNING** start of CLMS field may overlap end of DESC **. vide satisfactory results as indicated by the fact that the physical structure of electrode 53 is formed in the depicted embodiment by cathode support element 28 which extends out of the inlet side of venturi 27 terminating at bus bar 29. The diameter of the focusing electrode cylinders is preferably between 0.2 and 0.4 of the inside diameter of the anode surface surrounding cathode disk 50. If the diameter is larger or smaller the electric field at the focusing electrode surface is increased promoting surface corona leakage. However, even outside the preferred range, focusing electrodes of the present invention provide improved performance as compared with prior art devices not employing such electrodes. While a preferred embodiment of the present invention has been shown and described above, it will be readily apparent to those skilled in the art that numerous modifications and adaptations thereof may be made. WHAT WE CLAIM IS:-

1. A high-intensity gas ionizer, for use with an electrostatic precipitator, comprising at least one venturi diffuser having an inlet connected to a source of particulate laden gases and an outlet connected to said electrostatic precipitator, a discharge electrode comprising a cathode disc having an arcuate periphery and being co-axially mounted within said venturi diffuser, voltage generating means interconnected betweeen said discharge electrode and said venturi diffuser to establish a high-intensity electric field within said venturi diffuser across the path of said particulate laden gases flowing therethrough, and corona discharge focusing electrodes situated adjacent the upstream and downstream sides of said discharge electrodes, wherein said corona discharge focusing electrodes are maintained at an electrical potential approximately the same as that of said discharge electrode, and each comprises a cylindrical member coaxial with, and of smaller outer diameter than, the cathode disc, and is adapted to limit the width of the corona discharge in the direction of flow of said particulate laden gas and hence the surface area of said venturi diffuser subjected to deposition of particulate from said gases.

2. A gas ionizer as claimed in claim 1 wherein one of said focusing electrodes comprises a support member co-axially mounted with said venturi diffuser and having said discharge electrode mounted thereon.

3. A gas ionizer as claimed in claim 2, wherein the other of said focusing electrodes is an extension of said support member, said extension passing through said cathode disc and terminating downstream thereof in a hemispherical cap.

4. A gas ionizer as claimed in any one of claims 1 to 3 wherein the diameter of said focusing electrodes is between 20% and 40% of the inside diameter of the venturi diffuser surface surrounding said discharge electrode, but less than the diameter of said discharge electrode.

5. A gas ionizer as claimed in any one of claims 1 to 4, wherein said focusing electrodes extend on either side of said cathode disc a distance at least equal to the distance between the disc periphery and the surrounding venturi diffuser surface.

6. A gas ionizer as claimed in any one of the preceding claims, further comprising a plurality of individual venturi diffusers arranged in an array with their axes aligned and their inlets connected to said source of particulate-laden gases, each of said venturi diffusers being provided with associated corona current focusing electrodes.

7. A high-intensity gas ionizer, for use with an electrostatic precipitator, substantially as hereinbefore described with reference to and as illustrated in the various figures of the accompanying drawings.

8. An electrostatic precipitator in combination with a high intensity gas ionizer as claimed in any one of the preceding claims.

9. In a high-intensity gas ionizer according to claim 1, for use with an electrostatic precipitator, a method comprising the steps of generating a high intensity electrical field within said venturi diffuser across the path of particulate laden gases being passed therethrough and limiting the width of the corona discharge, and hence the surface area of said venturi diffuser subjected to deposition of particulate from said gases, by generating an additional electrical field on the upstream and downstream sides of said discharge electrode.

10. In a high-intensity gas ionizer according to claim 1 for use with an electrostatic precipitator, a method of limiting the width of the corona discharge and hence the surface area of the venturi diffuser subjected to particulate deposition substantially as hereinbefore described with reference to and as illustrated in the various figures of the accompanying drawings.