This invention pertains to a method and apparatus for particulate matter removal and for undesirable vapor scrubbing from a gas stream.
There have been continuing attempts to improve techniques for removing fine particulates from gas streams. In conventional systems, contaminated gas streams are typically cleansed of particulate matter by charging the particular matter in a charging section of an apparatus. The residence time for the gas within the charging section of such conventional apparatuses, however, is typically very low and, therefore such systems do not provide for substantial collection of particulate matter following charging. Moreover, the collection and removal of negatively-charged particles from a gas stream in conventional systems and methods typically occurs in neutral scrubbers. In this regard, the attraction forces between the negatively-charged particles and neutral collecting surfaces (packing) in conventional systems is typically very weak and, therefore, necessitates the maintenance of low gas stream velocity through the system in order to obtain efficient removal of submicron particles. This limitation, in turn, typically calls for larger and more expensive equipment.
A need remains, therefore, for improved and cost effective apparatuses and methods for eliminating all or substantially all of a particulate matter and undesirable vapors from a gas stream, while continuously cleaning the collecting surface.
In one aspect the invention provides an apparatus for removing particulate matter and undesirable vapors from a gas stream containing particulate matter and undesirable vapors, wherein the apparatus comprises at least one ionizing electrode that negatively charges the particulate matter and condensed droplets of undesirable vapors, at least one scrubbing element that includes a collecting surface, and at least one a liquid applicator operable to apply a liquid film to the collecting surface, whereby a positive charge is applied to the liquid film to attract negatively-charged particulate matter and condensed droplets of undesirable vapors to the liquid-covered collecting surface.
In another aspect the invention provides a method for removing particulate matter and undesirable vapors from a gas stream containing particulate matter and undesirable vapors, the method comprising: negatively charging the particulate matter and condensed droplets of undesirable vapors using at least one ionizing electrode; applying a liquid film to a collecting surface proximate the ionizing electrode; and positively charging the liquid film to attract the negatively-charged particulate matter.
One embodiment of the invention provides a highly efficient and compact apparatus and method for removing both particulate matter (e.g., PM-10 and PM-2.5) and undesirable vapors from a gas stream substantially simultaneously or simultaneously.
In one aspect, an apparatus is provided for removing particulate matter and undesirable vapors from a gas stream containing particulate matter and undesirable vapors. An example apparatus comprises at least one ionizing electrode that negatively charges the particulate matter and undesirable vapors, at least one scrubbing element including a collecting surface, and at least one liquid applicator operable to apply a liquid film to the collecting surface, wherein a positive charge is applied to the liquid film to attract negatively-charged particulate matter and/or undesirable vapors to the collecting surface.
In another aspect, a method is provided for removing particulate matter and undesirable vapors from a gas stream. An example method comprises the steps of: negatively charging the particulate matter and undesirable vapors using at least one ionizing electrode; applying a liquid film to a collecting surface proximate the ionizing electrode; and positively charging the liquid film to attract the negatively-charged particulate matter and vapors. Another example method includes the steps of: delivering scrubbing liquid into a scrubbing element that is appropriate for the removal of undesirable vapor from a moving gas stream; and configuring the scrubbing element in the moving gas stream to provide intimate contact between the molecules of undesirable vapors and a film of scrubbing liquid flowing on a surface of the scrubbing element for efficient absorption.
Turning now to the Figures, example apparatuses and methods are described.
The example apparatus may operate as follows: a gas stream contaminated with (or containing) particulate matter and/or undesirable vapors (e.g., acid vapors, acid gases, or toxic gases, such as, for example, SO2, NOx, or HCl) enters the apparatus through the inlet transition 1. Spray nozzles 2 that are configured in the inlet transition 1 provide continuous self-cleaning of a collecting surface (e.g., a front panel perforated plate) of the inlet scrubbing element 3 (i.e., the scrubbing element 3 that is configured proximate to the inlet transition 1) to reduce and/or remove particulate matter that may tend to accumulate on the incident collecting surface. Scrubbing elements 3, which may comprise front and back perforated plates, are filled with scrubbing packing, which can be selected, for example, according to the chemistry of the process, the particulate matter involved, and the gas scrubbing requirements, in a manner known to those of skill in the art. A scrubbing liquid is delivered by a liquid applicator 4, such as spray header, and flows downward (e.g., by gravity) film-wise or sheet-wise on the collecting surfaces of scrubbing elements 3 to the bottom of the housing and toward sump 10. The scrubbing liquid forms a substantially continuous or continuous liquid film on the collecting surfaces of the scrubbing elements 3 and enables highly active interaction between the moving gas stream and the collecting surfaces of scrubbing elements 3, thereby facilitating the removal of electrically-charged particles and/or undesirable vapors.
As illustrated in
The scrubbing liquid used in the apparatus to apply a liquid film to the collecting surface of the scrubbing elements 3 can be any suitable liquid for use in removing and/or scrubbing particulate matter and undesirable vapors from a gas stream. The scrubbing liquid may be, for example, water with a suitable scrubbing reagent (e.g. sodium hydroxide), etc. Moreover, it is preferable for the scrubbing liquid to have as a chemical property the ability to maintain or sustain electrical charges (e.g., positive charges) applied to the liquid by a contact or conductor, even when in the form of a liquid film on the collecting surface. Choice of a suitable scrubbing liquid depends, for example, on the specific particulate matter and/or undesirable vapors that are sought to be removed from a particular gas stream, as is understood by those of skill in the art. The scrubbing liquid can be delivered to the collecting surfaces of scrubbing elements 3 in any suitable manner such as spraying, gravity feed, etc.
The scrubbing elements 3 and their collecting surfaces used in the context of the present invention can be constructed of a variety of suitable materials. In an embodiment, the scrubbing elements 3 are constructed to provide a charge conducting surface to which charged (e.g., negatively-charged) particulate matter and/or undesirable vapors are attracted (e.g., through electrostatic precipitation processes). In one embodiment, the collecting surface of a scrubbing element 3 is constructed partially or entirely of a conductive material (e.g., a metal) to which an electrical charge (e.g. positive polarity) is applied. In another embodiment, for example the scrubbing elements 3 and collecting surfaces may be constructed, at least partially, of a non-conductive material (e.g., plastic). An electrical contact is provided to apply an electrical charge to the film of scrubbing liquid on the collecting surfaces of scrubbing elements 3. In either embodiment, a substantially continuous or continuous film of scrubbing liquid is preferably applied to the surface of the collecting surfaces of scrubbing elements 3 by a liquid applicator 4, which may include a spray nozzle or the like, to provide continuous cleaning of the collecting surfaces and enhanced collection operation.
An electrical contact is configured on the apparatus to charge (e.g., positively) the liquid film in a suitable manner. In an embodiment, a charge is applied to the liquid film by at least one contact that applies a charge to a liquid body in conductive contact with the film. As can be appreciated from
In another embodiment, a charge is applied to the liquid film by a contact that is located on or in direct contact with the collecting surface. The contact can be a conductive element located on the surface, or in the case of a scrubbing element made of a conductive material, the entire scrubbing element can act as a contact to the film.
Particulate matter and/or undesirable vapors of a contaminated gas stream enters the space between the scrubbing elements 3 and ionizing electrode 5 and the particulate matter in the gas stream become charged due to the high voltage being applied to the electrodes 5. A corona discharge of negative ions flowing between the ionizing electrodes 5 and the collecting surfaces 3 occurs due to the high voltage corona effect. The negatively-charged particulate matter is then attracted to the packing of scrubbing elements 3 (which can be grouped and can have positively-charged collecting surfaces) and to the scrubbing liquid film flowing thereon. A continuous downward flow of scrubbing liquid on the collecting surfaces of scrubbing elements 3 then moves the attracted particulate matter and precipitated product of reaction between the scrubbing liquid and undesirable vapors downward to the sump 10 and drain to be filtered and/or disposed of. After the treatment of the gas stream in the apparatus is complete, the gas stream exits through the outlet transition 11. The charges (electrons) from the negative ions can be circuited back to the voltage source 8, thereby completing the electrical circuit (as depicted at point 12 in
A schematic of a single pass apparatus is illustrated in
The scrubbing elements 3 and the ionizing electrodes 5 used in the context of the present invention can be configured, situated, and oriented (e.g., with respect to each other) in any manner that is suitable for the charging of particulate matter and condensed droplets of undesirable vapors contained within a gas stream and the subsequent and/or simultaneous attracting of charged particulate and/or condensed droplets of undesirable vapors to the collecting surfaces. In some embodiments, the collecting surfaces of the scrubbing elements 5 may be oriented in a direction substantially perpendicular or perpendicular to the direction of the flow of the gas stream. In an example wherein the gas stream to be scrubbed flows in a substantially horizontal direction, the scrubbing elements 5 may be substantially vertically oriented so that the scrubbing liquid flows by gravity.
An electrical field is preferably maintained between the collecting surfaces of scrubbing elements 3 (e.g., positively-charged collecting surfaces) and the negatively-charged ionizing electrodes 5. In this regard, as discussed above, when particulate matter and/or undesirable vapors enter the space between the scrubbing elements and negative high voltage electrodes, the particulate matter and/or condensed droplets of undesirable vapors become charged (e.g., by a corona discharge that is taking place between the ground and high voltage). The negatively-charged particulate matter and/or condensed droplets of undesirable vapors pass through the positive grounded collecting surfaces and are attracted to the surface of the collecting surfaces and/or to the film of scrubbing liquid on the surface of the scrubbing elements. Thus, collected particles and/or condensed droplets of undesirable vapors are removed from the gas stream and are carried from the apparatus to discharge by a recycle liquid. The presence of an electrical field between the grounded (positive) collecting surfaces and ionizing (negative) electrodes, in this regard, allows for treatment of a high-velocity flow gas stream, while maintaining high efficiency of particulate matter and undesirable vapor removal by an absorption process similar to the conventional cross flow pack-bed scrubber.
The apparatuses and methods described herein provide for excellent particulate matter removal efficiency while also providing absorption capacity for undesirable vapors (e.g., toxic acid gases), and while operating at high gas flow velocities with continuous self-cleaning of the scrubbing element. The present apparatuses and methods also provide for gas treatment in a multi-pass fashion in the same small apparatus space as is required for single pass processes. Moreover, the present invention provides for the simultaneous action of the electrostatic precipitation, inertial impaction, adsorption, and absorption—which enables a multipollution control system by a single apparatus in a cost effective fashion.
The present apparatuses and methods provide for multiple electrical fields which may act in series or parallel on a gas stream, thus providing exceptionally high efficiency, redundancy, and reliability, and thus facilitating treatment of highly toxic gases laden with heavy metal, dioxins/furans, mercury, and similar chemical moieties that are exhausted, for instance, from incinerators and other processes. The present apparatuses and methods also provide for the capacity to treat a gas stream sequentially or simultaneously for at least two different pollutants in a gas stream via introducing different scrubbing liquids or reagents, e.g., in separate scrubbing sections but within the single apparatus. Moreover, the present apparatuses and methods provide an economically-feasible apparatus for treatment of corrosive gases, due to the fact that most of the internal components of the apparatus can be constructed from plastic (non-conductive) materials, such as, for example, FRP and/or PVC.
All references, including publications, patent applications, and patents, cited herein are hereby incorporated by reference to the same extent as if each reference were individually and specifically indicated to be incorporated by reference and were set forth in its entirety herein.
The use of the terms “a” and “an” and “the” and similar referents in the context of describing the invention (especially in the context of the following claims) are to be construed to cover both the singular and the plural, unless otherwise indicated herein or clearly contradicted by context. Recitation of ranges of values herein are merely intended to serve as a shorthand method of referring individually to each separate value falling within the range, unless otherwise indicated herein, and each separate value is incorporated into the specification as if it were individually recited herein. All methods described herein can be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context. The use of any and all examples, or exemplary language (e.g., “such as”) provided herein, is intended merely to better illuminate the invention and does not pose a limitation on the scope of the invention unless otherwise claimed. No language in the specification should be construed as indicating any non-claimed element as essential to the practice of the invention.
Preferred embodiments of this invention are described herein, including the best mode known to the inventors for carrying out the invention. It should be understood that the illustrated embodiments are exemplary only, and should not be taken as limiting the scope of the invention.
This patent application claims the benefit of U.S. Provisional Patent Application No. 60/697,782, filed Jul. 8, 2005.
Number | Date | Country | |
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60697782 | Jul 2005 | US |