Combustion-exhaust source 102 may be configured to burn fuel producing exhaust as a byproduct. Combustion-exhaust source 102 may be an engine such as a diesel engine, a gasoline engine, a natural-gas engine or any other suitable type of engine that generates exhaust. Alternatively, combustion-exhaust source 102 may be any other source of combustion exhaust that is not associated with an engine, such as a furnace.
Air-induction system 134 may introduce air into combustion-exhaust source 102. Air-induction system 134 may include an air filter 106, a throttle/mixing valve 124, an air compressor 122, and an aftercooler 128. These components may be fluidly connected in a configuration that facilitates introduction of air into combustion-exhaust source 102.
Air filter 106 may remove or trap debris from air flowing into combustion-exhaust source 102. Air filter 106 may include any type of filter such as a full-flow filter, a self-cleaning filter, a centrifuge filter, an electro-static precipitator, or any other type of filter known in the art. More than one air filter 106 may be included within air-induction system 134.
Throttle/mixing valve 124 may be configured to mix atmospheric air and exhaust gas at a predetermined ratio. Throttle/mixing valve 124 may regulate the flow of the mixture into combustion-exhaust source 102. Separate exhaust and intake throttle valves may be implemented.
Compressor 122 may compress the air flowing into combustion-exhaust source 102 to a predetermined pressure and may be fluidly connected to aftercooler 128. Compressor 122 may be a fixed-geometry-type compressor, a variable-geometry-type compressor, or any other type of compressor. More than one compressor 122 may be included. Compressor 122 may be omitted, for example, when a non-compressed, air-induction system is desired.
Exhaust system 136 may direct exhaust out of combustion-exhaust source 102. Exhaust system 136 may include a turbine 130, a particulate filter 132, a first fluid passageway 114, a second fluid passageway 116, one or more SOx-removing devices 108, and an exhaust-gas cooler 118. Additional devices may be included within exhaust system 136 such as filters, catalysts, mufflers 140, and other emission-controlling devices. These components may be fluidly connected to direct the flow of combustion exhaust throughout system 100.
Turbine 130 may be connected to and receive exhaust from combustion-exhaust source 102 and compressor 122. As hot exhaust gases exiting combustion-exhaust source 102 expand, turbine 130 may be caused to rotate, thereby rotating connected compressor 122. More than one turbine 130 may be included within exhaust system 136. Turbine 130 may alternatively be omitted and compressor 122, if present, may be directly rotated by combustion-exhaust source 102 mechanically, hydraulically, electrically, or in any other manner.
Particulate filter 132 may collect solid and liquid pollutants from exhaust emitted by combustion-exhaust source 102. Particulate filter may include a wire mesh medium, a shallow- or deep-bed ceramic medium, or any other known medium through which the engine exhaust may be passed. Particulate filter 132 may be selectively and/or periodically regenerated to reduce buildup of collected particulate matter.
First fluid passageway 114 may direct exhaust gases from the combustion-exhaust source 102 into the atmosphere. Second fluid passageway 116 may direct exhaust gases from combustion-exhaust source 102 back into combustion-exhaust source 102. The two fluid passageways may be separate and distinct and may connect directly to combustion-exhaust source 102. Alternatively, the two fluid passageways may be connected as a common passageway with one fluid passageway branching off from the other at some point downstream from combustion-exhaust source 102.
The SOx-removing device 108 may include a container composed of metal, plastic, or any other material that can withstand the environment (e.g., temperatures and chemicals) present in the system in which it is placed. The container may have an input opening and an output opening to allow connection of the device to the first 114 or second passageway 116, and to allow the combustion exhaust to flow through it.
Within SOx-removing device 108 there may be any compound that removes sulfur oxides from a chemical solution that comes into contact with it. The compound must have a reasonable capacity for the adsorption or absorption of SOx. Examples of such a compound may include Magnesium (Mg), Calcium (Ca), Strontium (Sr), Manganese(Mn), Barium (Ba) and Lithium (Li) compounds, among others.
In one arrangement, Cryptomelane (KxMn8O16) may be used as the adsorbent compound in SOx-removing device 108. The Potassium countercation, K+, provides charge compensation since Mn can assume an oxidation state of 4+, 3+ or 2+. Cryptomelane has a high relative surface area (˜80 m2/g) leading to strong adsorption kinetics and, therefore, high oxidation-reduction-reaction activity. Cryptomelane may be capable of removing SOx from exhaust gas within a temperature range of about 50° C. to 650° C. This may be in excess of the operating range of most engines used in motor-driven vehicles and most other combustion-exhaust sources. It may be advantageous to use Cryptomelane as the reactant within SOx-removing device 108 because it can be placed anywhere in the exhaust stream without degradation due to temperature. Further, there may be a significant change in the color of reacted Cryptomelane, which may be a reliable indicator of the need to replace or replenish SOx-removing device 108.
The compound within SOx-removing device 108 may be held or suspended in any form that allows maximal exposure of exhaust gas to facilitate reaction, while not impeding the flow of exhaust significantly. Examples of suitable support mechanisms may include pellets, powders, monolithic honeycomb structures (as illustrated in the example of
SOx-removing device 108 may be constructed in such a way that the trapped SOx can be cleaned from the device 108. This may require that the compound be removed from SOx-removing device 108 and used to remake the compound from scratch. However, the compounds used in SOx-removing device 108 may have such a high affinity for sulfur oxides that regeneration of SOx-removing device 108 on-board a vehicle would be impractical.
SOx-removing device 108 may be constructed in such a way that it can be removed from the exemplary system to facilitate replacement. One example may be a device constructed similarly to an automobile oil filter that can be removed, discarded, and replaced as one complete unit fastened to the exhaust system 136 with a flange or a clamp. Another example may be a SOx-removing device 108 constructed with an opening mechanism (e.g., a trap door) such that the compound and its supporting structure can be removed and replaced without removing the device from the vehicle.
SOx-removing device 108 may be constructed to include an indicator of the remaining usable life of SOx-removing device 108. The indicator may be an opening or window that allows visual inspection of the compound within the device. Alternatively, SOx-removing device 108 may be replaced according to some fixed schedule based on vehicle mileage, in-service time, calendar time, or any other reasonable measure.
SOx-removing device 108 may be disposed at any position in exhaust system 136 in a quantity that maximizes the efficiency and the benefit of SOx removal.
In another example illustrated in FIG. 4., all of the exhaust gas from combustion-exhaust source 402 may be directed into SOx-removing device 408 via a common first and second passageway 415 before any is released into the atmosphere or directed back to the combustion-exhaust source 402. This position may ensure that all exhaust (whether recycled or not) is treated before other engine components, including downstream exhaust treatment devices, can be exposed to acidic-corrosion. It may also ensure that SOx are not released into the atmosphere.
Alternatively, multiple SOx-removing devices may be used in an exemplary disclosed system as shown in the example of
As in the example illustrated in
The disclosed exhaust-treatment system may be applicable to any combustion system that incorporates an Exhaust Gas Recirculation (EGR) system. Examples may include the power source of a motor vehicle or the furnace of an electricity-generating facility and other combustion systems known in the art. The disclosed exhaust-treatment system may reduce the SOx in the exhaust gas and thereby minimize or eliminate condensation of H2SO4 and subsequent damage to all engine components that come in contact with the recycled exhaust.
The method for using the disclosed system can be illustrated by the example shown in
In removing SOx from the exhaust gas using Cryptomelane, the following reaction may take place:
8SO2+KxMn8O16+(x/4)O2→8MnSO4+(x/2)K2O
(where “x” is the amount of Mn3+ in KxMn8O16). Here the SO2 is oxidized to SO3 by Mn4+ and Mn3+. Mn4+ and Mn3+ are simultaneously reduced to Mn2+ as MnO. The SO3 then reacts with Mn2+ to form MnSO4.
Implementation of the disclosed system and method may reduce formation of sulfuric acid (H2SO4) by removing its sulfur-oxide precursors, SO2 and SO3, from the exhaust stream. This, in turn, may minimize acidic-corrosion degradation of all system components. Ultimately, this may improve the life span of the system and its components and possibly system performance.
It will be apparent to those skilled in the art that various modifications and variations can be made to the disclosed system and method. Other embodiments will be apparent to those skilled in the art from consideration of the specification and practice of the disclosed system and method. The examples used to illustrate the system show an engine used to power a motor vehicle. Alternatively, the combustion-exhaust source may be any source of combustion exhaust known in the art such as a furnace that is not associated with an engine. It is intended that the specification and examples be considered as exemplary only, with a true scope being indicated by the following claims and their equivalents.
This invention was made with government support under the terms of Contract Number DE-AC06-76-RL01830 (CRADA number PNNL/211) awarded by the U.S. Department of Energy. The government may have certain rights in this invention.