Multi-stage collector for multi-pollutant control

Abstract

A multi-stage collector for multi-pollutant control that contains alternating narrow and wide sections with glow discharge electrodes in some narrow sections, a uniform electric field in wide sections for collecting particles charged by the glow discharge and streamer discharge electrodes in wide or narrow sections that convert and destroy harmful gaseous pollutants such as SO2, NOx and volatile organic compounds as well as convert heavy metals such as mercury into a particulate form. Steady state streamer discharge is supported by non-pulsed power supply. The streaming discharge can convert the polluting gases into nitric and sulfuric acid which can be removed by combining it with ammonia to form solid salts.

Description

DESCRIPTION OF THE FIGURES

Attention is directed to several figures that illustrate embodiments of the present invention:

FIG. 1 shows a cross-section of an embodiment of the present invention.

FIG. 2 shows an enlargement of one element in the embodiment of FIG. 1

FIG. 3 shows a typical I-V curve.

FIG. 4 shows a curve of I/V vs V curve.

FIG. 5 shows a way of mounting electrodes.

Several illustrations and drawings have been presented to aid in understanding the present invention. The scope of the present invention is not limited to what is shown in the figures.

DESCRIPTION OF THE INVENTION

The present invention makes use of non-thermal plasmas (NTP) to destroy harmful gaseous components. An NTP can be created by different gas discharges (DC, AC or pulsed) at atmospheric pressure. Prior art methods of creating an NTP are dielectric barrier discharge (DBD) and pulsed corona discharge (PCD). DBD and PCD have intrinsic limitations associated with necessity to use very narrow inter-electrode gaps and very short high voltage pulses (for DBD and PCD respectively) that results in difficulties under introducing these sources into real practice. An NTP in flue gas is a quasi-neutral mixture of charged particles (electrons, positive and negative ions), chemical active particles like radicals and photons. Photons are created due to collisions of energetic electrons with molecules of the background gas. A very useful property of an NTP is that the majority of the electric energy deposited in the treated gas goes into heating the electrons rather than heating the gas. The typical average electron energy (or electron temperature) in an NTP is around 30,000 to 50,000 degrees K (around 3-4 eV), but the average temperature of the background gas is around 300-500 degrees K. In the case of a gas flow containing N₂, O₂ and H₂O, most of the primary radicals generated in an NTP are O and OH. These radicals are generated due to plasma reactions initiated by energetic electrons and excited species like molecular nitrogen N*₂ and atomic oxygen O(¹D) as following:

e+O ₂→O+O+e

e+O ₂→O+O(¹D)+e

O(¹D)+H₂O→OH+OH

e+H ₂O→OH+OH+e

e+N ₂→N₂*+e

N₂*═N₂(A³Σ,B³π,C³π, . . . )

N₂*+O₂→N₂+O+O

N₂*+O₂→N₂+O+O(¹D)

O and OH radicals rapidly oxidize NO and SO₂ to form NO₂ and SO₃ which become nitric and sulfuric acids as well as forming the acids directly. The gaseous acids can be transformed into salts with gaseous ammonia. The salts can be removed as solids. For example,

NO+OH+M−>HNO₂+M(where M is a third particle).

m can be an N₂ molecule for example (where the rate coefficient is k=6.7×10(−31) cm̂6/s. Nitrous acid HNO₂ is further converted:

HNO₂+OH−>NO₂+H₂O.

In the case of O radicals, the formation of NO₂ takes place in a single step:

NO+O+M−>NO₂+M.

Nitrogen dioxide NO₂ forms nitric acid upon reacting with OH:

NO₂+OH+N₂−>HNO₃+N₂(k=2.6×10(−30))

A set of similar reactions convert SO₂:

SO₂+OH−>HSO₃+O₂−>SO₃.

Sulfur trioxide SO₃ is converted by water to sulfuric acid. Gaseous nitric and sulfuric acid is converted by ammonia to ammonium nitrate and ammonium sulfate respectively. Both of these are solid salts that can be collected and removed. The present invention can simultaneously treat SO_x and NO_x pollutants. In this case, there is an interplay for intermediate species of these pollutants that results in a positive synergy effect in the destruction of both of them. It should also be noted that a non-thermal plasma promotes the formation of H₂SO₄ molecules in a gas flow polluted with SO_x. It is possible to increase the concentration of these molecules more than the threshold for condensation of gaseous sulfuric acid into small droplets of liquid acid. Precipitation of these conductive droplets onto a layer of high resistive particles collected by the a collector electrode can result in diminishing the surface charge on the dust layer and therefore in preventing a back-corona effect. This leads to an increase in the effectiveness of precipitation of high resistive particles.

Control of heavy metals is also important. Joint gas phase reactions of radicals and ammonia with gaseous mercury provided by an NTP can effectively transform 80-90% of the Hg into fine particles that can be collected by precipitators or fabric filters.

The molecular temperature of flue gases at the inlet to a cleanup device is about 150 degrees C. In an NTP system, the increase in temperature of the gas at the outlet due to glow discharge or corona discharge does not exceed several tens of degrees. This slight temperature increase is entirely acceptable because it is not enough to induce generation of harmful molecules like NO_x and SO₂ in the effluent gas stream. It is well known in the art that reactions that produce such products from N₂ and O₂ require from 1,000-2,000 degrees C. The NTP system of the present invention also does not produce much ozone. This is because the humidity of flue gases is around 10% by volume (relatively high). With a temperature of around 150 degrees C., the temperature/humidity combination result in a strong suppression of ozone generation from O atoms.

Turning to FIGS. 1-2, an embodiment of the NTP system of the present invention is shown. FIG. 1 shows a cross-section of a precipitator, while FIG. 2 shows a single narrow-wide region. Generally, narrow and wide regions alternate. In a first narrow region of the precipitator 1, a high tension, low current glow discharge realized with the use of individually ballasted electrode 16 interacts with the gas stream. This glow discharge replaces the negative corona discharge of a conventional precipitator. Due to special shape of the electrodes glow discharge is stable with respect to addition in treated gas of water vapor, small admixtures like NH₃ and dust and therefore can drastically increase the efficiency of charging dust particles. A region of linear electric field in a subsequent wide section 2 allows collection of the charged dust particles. Further into a wide section, a high tension, high current steady state positive streamer discharge realized with use of special shape and individually ballasted electrode 14 causes a generation of chemically active species providing the conversion and destruction of harmful pollutants. It should be understood that the sequence of glow discharge and streamer corona in narrow and wide sections can be varied to maximize the efficiency of the device. Any disposition of glow discharge and streamer corona is within the scope of the present invention.

The initial glow discharge increases the electric field strength in those states of the system that are devoted to dust collection, and the steady-state positive streamer corona is used in those stages dedicated to destruction of pollutants. The geometric shape of the regions is generally similar to the shapes shown in FIG. 2, which is a blowup of one of the areas from FIG. 1. The narrower regions are used to generate corona, while the wider regions contain a uniform electric field and are used for particle collection. Collectors and filters can be made with conductive surfaces. The present invention works particularly well with high resistivity ash such as the high calcium ash that results from the burning of Powder River Basin coal. Such high resistivity ash is very difficult to collect using prior art techniques.

The operation of a typical embodiment of the present invention operates as follows: Ash laden flue gas enters the system from a combustion section that is normally fossil fuel-fired with water cooled inserts to control the gas temperature leaving the burner section. The effluent gas containing particles passes through an alternating series of glow discharge regions 8, constant field collection regions 2 and streamer discharge regions 13 in narrow 1 and wide 12 areas. Electrodes 16 protruding from a glow-discharge module 3 cause the discharge. A non-pulsed power source supplies steady state current through an entry conductor 6 and through individual ballast resistors 7 to produce the glow discharge regions 8 from the electrodes 16. Similarly, the streamer discharges are produced from current entering through an entry conductor 10 inside a barrier filter 4 (with interior 9). The higher current flows through the individual ballast resistors 11 to electrodes 14 that create steady state streamer corona regions 13.

Numerous streamers of steady state corona starting from the electrode 14 time after time with high frequency travel chaotically across the streamer section 13. Due to this, energetic electrons are created abundantly and constantly in whole volume of the treated gas that results in transfer of energy to the dominate gas molecules (N₂, O₂, H₂O, CO₂) by collisions. This results in the formation of primary radicals (O, N, OH), positive and negative ions and excited molecules. Later the electron-ion, ion-ion, radical-radical reactions like O+OH→HO₂, and electron detachments create more secondary radicals (HO₂, etc.). Large amounts of O, O₂, OH, and H radicals are easily generated in the coronas. The radicals either oxidize SO₂ and NO_x or react with them to form aerosols. Since the formation energy of the radicals is approximately 10 eV, the energy of the corona discharge is sufficient to produce the radicals. The result is that gaseous nitric and sulfuric acid is produced. Ammonia can be introduced into the effluent stream at a point downstream from the streamer discharge that is acid-rich. The ammonia salts can be collected with filters or the like in cooler sections. The ammonia can be injected as a gas or in the form of urea or other amine. Barriers 4 and filters (not shown) in the apparatus of the present invention can be cleaned in standard ways such as polarity reversal and rapping.

FIG. 3 shows a current vs. voltage graph for a streamer corona discharge system that displays voltage in kV on the horizontal axis and current in mA on the vertical axis. Plots at two different temperatures are shown, 21 degrees C. and 66 degrees C. All of the data was taken at 2% H₂O. FIG. 4 shows the reduced discharge currents I/U vs applied voltages U. The linear portions of the curves at low currents correspond to normal corona discharges. Non-linear portions of the curves with dramatic increasing currents correspond to novel regimes of high-current steady state streamer corona realized in this invention due to special shape of the electrodes and using of individual ballast resistors. A preferred operating point in the system measured would be around 20-22 kV. The graphs of FIGS. 3-4 are merely an example of operation of the present invention. The exact corona region and current vs. voltage curves depend on many variables including geometry, humidity, temperature and gas content and can be optimized for each specific conditions.

FIG. 5 shows a way of mounting electrodes on a substrate 14. An inner pointed electrode 15 protrudes through a hole 16 in the surface. This pointed electrode 15 can be a copper rod. A flared section of copper tube 17 runs through the hole 16. The flare angle can be around 60 degrees; however, many other angles will work. A bare section 18 of the electrode 15 can run away from the inner surface of the cylinder. At some point under the surface, the electrode can turn and enter a jacket of TEFLON™ or other high voltage insulation 19. A group of these insulated electrode feeders can run to individual ballast resistors as discussed and shown in other figures. It should be noted that while copper has been specified as a preferred electrode metal, any other conductor or metal can be used and is within the scope of the present invention.

Several descriptions and illustrations have been provided to aid in the understanding of the present invention. One skilled in the art will realize that numerous changes and variations are possible without departing from the spirit of the invention. Each of these changes and variations is within the scope of the present invention.

Claims

1. A method for multi-pollutant control of gaseous and particle pollutants in mixture of gases comprising the steps of: passing said mixture of gas through an alternating series of glow discharge regions, constant field collection regions, and corona streamer discharge regions in narrow and wide areas defined by spaced electrodes;causing steady state dissipation in said regions of non-pulsed electrical power of sufficiently high voltage to establish therein a continuous glow discharge and a streamer corona discharge, whereby SO2 and/or NOx and/or heavy metals are converted to acid mist and/or particle aerosols;collecting said acid mist and/or particle aerosols.

2. The method of claim of 1 wherein said mixture of gases contains air.

3. The method of claim of 1 wherein said mixture of gases is a stack gas.

4. The method of claim of 1 wherein said mixture of gases is effluent from an industrial process.

5. The method of claim of 1 wherein said mixture of gases is exhaust from an internal combustion engine.

6. The method of claim of 1 wherein said mixture of gases contains volatile organic compounds.

7. The method of claim 1 wherein said narrow regions contain glow discharge electrodes.

8. The method of claim 1 wherein said wide regions contain constant field regions and corona streamer discharge regions.

9. The method of claim 1 wherein said corona streamer discharge regions contain corona streamer electrodes.

10. The method of claim 1 wherein ammonia is introduced into said mixture of gases.

11. An apparatus for removing pollutants from a flow stream comprising alternating narrow and wide regions, said narrow regions containing first electrodes driven by a first voltage to produce a glow discharge, said wide regions biased to create a relatively constant electric field between an outer boundary and an inner boundary, said wide regions also containing second electrodes driven by a second voltage to produce a corona streamer discharge between said second electrodes and said outer boundary.

12. The apparatus of claim 11 wherein said first and second electrodes are electrically connected to ballast resistors.

13. The apparatus of claim 11 wherein said inner boundary is a barrier filter.

14. The apparatus of claim 11 wherein ammonia is introduced into said flow stream upstream of said narrow and wide regions.

15. The apparatus of claim 11 wherein said first and second voltage is AC.

16. An apparatus for removing pollutants from a flow stream comprising a plurality of narrow and wide regions formed intro rows from boundaries laterally offset such that portions of a boundary that forms a wide region on one row forms a narrow region on a next row, said narrow regions including first electrodes driven by a first voltage to produce a glow discharge,said wide regions biased to create a relatively constant electric field between an outer boundary and an inner boundary,said wide regions including second electrodes driven by a second voltage to produce a corona streamer discharge between said second electrodes and said outer boundary.

17. The apparatus of claim 16 wherein said first and second electrodes are electrically connected to ballast resistors.

18. The apparatus of claim 16 wherein said inner boundary is a barrier filter.

19. The apparatus of claim 16 wherein ammonia is introduced into said flow stream upstream of said narrow and wide regions.

20. The apparatus of claim 16 wherein said first and second voltage is AC.