1. Field of Invention
This invention relates to treatment of exhausts of internal combustion engines, and more particularly to reduction of nitrogen oxides, carbon monoxide and hydrocarbons prevalent in the exhausts of internal combustion engines, particularly spark-ignited, gaseous-fueled internal combustion engines.
2. Description of the Prior Art
Spark ignited (SI) internal combustion (IC) engines operated with gaseous fuels produce small amounts of undesirable chemical compounds in the combustion chamber, compounds which are exhausted from the engine at high temperatures (800°-1250° F.). For fuels composed primarily of methane and other light hydrocarbons, the commonly regulated chemicals are nitrogen oxides (NO, NO2, or generally NOx) and carbon monoxide (CO). Nitrogen oxides are formed when nitrogen (N2), a major component of air, reacts with oxygen (O2), another major component of air, when both are exposed to high temperatures and pressures in an engine combustion chamber. Carbon monoxide, on the other hand, is the consequence of failure of the fuel to completely react with oxygen, resulting in the formation of carbon dioxide (CO2). CO and NOx are problematic pollutants inasmuch as their regulated values are in many geographical regions set at or below the limits of current technology.
In strictly regulated regions, current practice to control the emissions from SI/IC engines fueled by methane-rich fuels (natural gas, bio-fuels, landfill gas, etc.), is to install systems in the engine exhaust ducting to eliminate, to the extent required by regulations, such chemicals. For smaller engines (less than 1000 bhp), the common aftertreatment system is a single stage catalyst. In these small systems, the products of combustion exiting the engine are forced through a catalyst monolith (honeycomb structure with precious metal coating) which facilitates the desirable oxidation and reduction reactions:
NOx yields N2+O2
CO+O2 yields CO2
The nitrogen oxides are reduced to gaseous nitrogen (N2) and oxygen (O2), both benign, while the carbon monoxide (CO) is completely oxidized, forming carbon dioxide (CO2), likewise non-harmful and unregulated.
Current catalyst-based emissions systems rely on very accurate control of engine operating parameters to maximize the conversion efficiency of the reactions noted above. Specifically, the simultaneous elimination of NOx and CO through such reactions in a catalytic converter requires a precise operating window of the engine combustion process relative to the mixture of air and fuel. This is depicted in
Referring still to
Stationary SI/IC engines operating in most applications in the U.S. and elsewhere are highly regulated relative to allowable CO and NOx emissions, which are becoming increasingly controlled. Most notably, the California Air Resource Board (CARB) now recommends limits of 0.07 lb/MWh and 0.1 lb/MWh CO as part of their 2007 standard for Combined Heat and Power (CHP) applications. Applying a heat recovery credit for maintaining a minimum 60% overall system effeciency and assuming a 27% electrical effficiencey, the emissions limits stated in terms of actual concentration in the exhaust gas are 3.7 PPM NOx and 8.9 PPM CO. As used herein, “PPM” means parts per million by volume corrected to a standard air dilution factor (15% oxygen equivalent). The area of Southern California under the jurisdiction of the South Coast Air Quality Management District (SCAQMD) has adopted the “CARB 2007” standard for NOx, while restricting CO emissions to a value close to the CARB limit. Other regions in California are likewise adopting similar standards, while other regions of the country are phasing in regulations approaching the CARB 2007 standards (MA, NY, and NJ, for example).
Compliance with the newer standards requires extremely high conversion efficiency in the catalyst for both CO and NOx. Extra-large conversion monoliths are needed in addition to extreme precision in controlling the air/fuel mixture.
A possible method for expanding the control window for engine operation to attain acceptable emissions from both CO and NOx, is to modify the system such that two stages of catalyst systems are used, each operating in distinctly different chemical atmospheres. Early catalyst systems commonly used a two-stage design with inter-stage air injection. In this era, single purpose catalyst monoliths-oxidation or reduction, but not both, were employed. Later, as multi-purpose, single stage catalysts (TWC) were developed, these became the dominant style. The early two-stage systems were employed in stationary gaseous fueled SI/IC engines with success but under far less strict standards. Presumably, the NOx reformation problems encountered with the two-stage systems were present in the earlier era, but were inconsequential relative to the regulated limits at that time.
Tests utilizing the two-stage system demonstrated that the two-stage strategy with air injection was not only ineffective, but actually detrimental to catalyst performance. NOx emissions from the two-stage system were found to be generally higher than a single-stage system of comparable size and catalyst material loading. This surprising result indicated that a mechanism exists such that NOx is formed in the second stage, made possible by the oxygen rich environment, coupled also with conditions conducive to chemical reaction, i.e., high temperature and an abundance of a catalytic material.
An object of the invention is, therefore, to provide assemblies and methods for consistently and reliably removing nitrogen oxides and carbon monoxide from the exhausts of spark-ignited gaseous-fueled internal combustion engines.
With the above and other objects in view, a feature of the invention is the provision of assemblies and methods for effectively reducing nitrogen oxides, carbon monoxide and hydrocarbons in spark-ignited, gaseous-fueled internal combustion engine exhausts, by presenting the gases entering a catalytic converter second stage at a lower temperature.
In accordance with the invention, the gases entering the second catalytic converter stage are cooled immediately following stage one, from the extremely high temperatures normally exiting the engine (800°-1250° F.) to a lower value. An intermediate temperature, or range of temperatures, provide desirable chemical reactions (CO and hydrocarbon removal) and are highly favored over those that are undesirable because of NOx formation. This is deemed to be a particularly viable approach in combining heat and power (CHP) applications, inasmuch as the gases are cooled in the heat reclaim process. Doing so in a CHP application requires only that (1) the cooling stage be reoriented to cool between stages, and (2) the cooling effectiveness be altered to reside in a favorable temperature range.
The above and other features of the invention, including various novel details of construction and combinations of parts and method steps, will now be more particularly described with reference to the accompanying drawings and pointed out in the claims. It will be understood that the particular assemblies and methods embodying the invention are shown by way of illustration only and not as limitations of the invention. The principles and features of this invention may be employed in various and numerous embodiments without departing from the scope of the invention.
Reference is made to the accompanying drawings in which are shown illustrative embodiments of the invention, from which its novel features and advantages will be apparent.
In the drawings:
Testing of a two-stage system with inter-stage cooling was conducted using an apparatus depicted in
The combustion gases from the engine 20 enter the first stage 24 at a normal engine exhaust temperature (approximately 1200° F.), after which the exhaust flow is spilt into two streams 26, 28. One stream 26 is cooled to approximately 280° F. as it passes over cooling means 30, or through a conduit subject to an injected cooling medium adapted to vaporize and substantially reduce the stream temperature. The other stream 28 bypasses the cooling coils 30 and is injected with a controlled quantity of air from an air injector 32. The two streams 26, 28 rejoin, as at junction 34, then are piped into a second catalytic stage (Cat. 2) 46. The extent of the exhaust gas cooling can be adjusted with a temperature adjusting valve 36.
Three tests were conducted with this apparatus that demonstrate the disclosed invention, the tests being summarized below.
In a first experiment, the engine 20 was operated a high output (156 bhp and 2500 rpm) and fueled by natural gas. The temperature adjusting valve 36 was set such that most of the gases bypassed the cooling coils 30. Under steady state engine operation, and with the engine AFR fixed at a condition favoring NOx reduction out of the Stage 1 catalysts 24, the experiment summarized in
During the first 200 seconds and with no inter-stage air injection, the concentrations of NOx, CO, and 02 in the exhaust system, as well as the inter-stage exhaust temperature (“Tmix”) were measured at port S1 (
At 520 seconds inter-stage air injection was initiated, as is clearly indicated in
As air injection was increased stepwise at 800, 1100, and 1400 seconds, the NOx improved slightly, but remained highly noncompliant. At 1660 seconds, a change in the engine combustion was made to a richer value, which only worsened the NOx emissions.
At 1950 seconds, the air injection was discontinued, essentially returning the process to a single stage. In this final time segment, operating as a single stage system with a rich AFR, the NOx concentration was measured to be low, while the CO was found to be high, the expected result (see
In a second experiment, Test 1 was repeated, but with inter-stage cooling increased to achieve lower “Tmix” values (400° F. range). The results, shown in
The air injection, which had substantially negative effect on emissions at the higher temperature, was highly effective in improving the process when inter-stage cooling was substantially increased. It is important that the NOx reduction was not anticipated and is a very significant benefit of the process.
In a third test, the system was first adjusted to a steady state condition that provided near optimum performance, namely inter-stage cooling to approximately 520° F. with air injection equal to approximately 1% of the primary combustion air. Next, an engine air to fuel ratio controller was adjusted stepwise to alternate steady state operating points, both richer and leaner, to determine the tolerance of the process to maladjustment. The results, shown in
The new assembly and method provides, therefore, both lower emissions and greater tolerance for excursions in engines with air-fuel ratio under steady-state (non-dithering) fuel control. The same phenomenon and conclusions are applicable to dithering fuel control strategies, but with increases in the AFR compliance window, as measured by post-catalyst exhaust oxygen or lamda sensors.
There is thus provided by the present invention an assembly 10, shown in
The assembly further includes a first outlet conduit 27 for facilitating movement of the cooled first portion stream 26 of engine exhausts from the first stage catalytic converter means 24, a second outlet conduit 29 for facilitating movement of the second stream 28 of engine exhausts received from the first stage catalytic converter means 24, an air injection conduit 37 which receives air from the air injector 32 and is in communication with the second outlet conduit 29 for cooling the second portion of engine exhausts, a second exhaust gas conduit 33 in communication with the first outlet conduit 27 and the air injection conduit 37,and a second stage catalytic converter 46 in communication with the second exhaust gas conduit 33 and having an exhaust emitting outlet 48. The first outlet conduit 27 may optionally be provided with a temperature adjusting valve 36.
In operation of the assembly of
The air injector 32 injects air into the second outlet conduit 29. The hot exhaust gas of the second exhaust stream 28 and injected air proceed through the air injection conduit 37 and merge with the cooled stream 26 of exhaust gas and proceed to the second catalytic converter stage 46 and exit therefrom at outlet 48.
There is further provided an alternative embodiment 15 of the assembly for reducing nitrogen oxides, carbon monoxide and hydrocarbons in internal combustion engine exhausts, the alternative assembly 15 being shown in
The assembly 15 further includes a cooling means by-pass 64 in communication with the output of the first stage catalytic converter means 54 and the conduit 62 for cooled exhaust.
A second stage catalytic converter means 66 is in communication with the cooled exhaust conduit 62 and the cooling means by-pass conduit 64. An air injection conduit 68 is in communication with the cooled exhaust conduit 62. An exhaust outlet 70 extends from the second stage catalytic converter means 66.
In operation of the assembly of
There is further provided in conjunction with the assembly 10, shown in
The method further comprises directing the exhaust in the exhaust gas conduit 33 to a second stage catalytic converter 46, and discharging exhaust from the second stage catalytic converter 46, whereby to provide engine exhausts of less nitrogen oxides and less carbon monoxide content.
There is further provided in conjunction with the assembly 15, shown in
The method comprises the steps of conveying the engine exhausts to a first stage catalytic converter 54 and conveying the engine exhaust from the first stage catalytic converter 54 in part to a cooling means 58 and in part to a cooling means by-pass 64, and mixing exhausts from the cooling means 58 and the cooling means by-pass 64 in a cooled exhaust conduit 62, injecting air through an air injection conduit 68 into the cooled exhaust conduit 62, and directing the exhaust from the cooling means 58, and from the cooling means by-pass 64, and from the injected air conduit 68, to a second stage catalytic converter 66, and discharging through an outlet 70 the engine exhausts thus treated, whereby to provide engine exhausts of less nitrogen oxides and less carbon monoxide content.
In accordance with a still further feature of the invention there is provided a method for reducing nitrogen oxides, carbon monoxide and hydrocarbons in exhausts of spark-ignited gaseous fueled internal combustion engines. The method comprises the steps of directing the exhausts from an engine 20 to a first stage catalytic converter 24, 54, directing a first portion of exhaust output from the first stage catalytic converter 24, 54 to a cooling means 30, 58 and thence to a cooled exhaust conduit 26, 62, directing a second portion of exhaust output from the first stage catalytic converter 24, 54 to a non-cooled exhaust gas conduit 28, 64, uniting the first and second portions of exhaust gas and directing the united first and second portions to a second catalytic converter 46, 66 and injecting air into a selected one of (1) the non-cooled exhaust conduit 29 and (2) the united cooled and non-cooled exhausts after the uniting thereof.
In an alternative embodiment 16 of the system of
Similarly, an alternative embodiment 18 (
Thus, the alternative embodiment of the
The method for reducing nitrogen oxides, carbon monoxide and hydrocarbons in exhaust from internal combustion engines utilizing the assembly shown in
The alternative embodiment of
The method for reducing nitrogen oxides, carbon monoxide and hydrocarbons in exhausts from internal combustion engines utilizing the assembly shown in
It is to be understood that the present invention is by no means limited to the particular construction and method steps herein disclosed and/or shown in the drawings, but also comprises any modification or equivalent within the scope of the claims.
This application claims priority from U.S. Provisional Patent Application 61/343,392, filed Apr. 28, 2010, in the names of Joseph B. Gehret, Robert A. Panora, and Ranson Roser.
Number | Date | Country | |
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61343392 | Apr 2010 | US |