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Exhaust system for power generating apparatus

Inactive Publication Date: 2016-08-25
JOHNSON MATTHEY PLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The invention is a system that uses two beds of oxidation catalysts to reduce emissions during start-up and running at full load in a gas turbine. The first bed is placed at a high temperature to allow for faster reduction during start-up, while the second bed is placed at a lower temperature to complete the reduction of CO and VOCs. The system provides better overall performance, is less susceptible to poisoning, and reduces the likelihood of exhaust gas bypassing the catalyst system. The first bed promotes NOx reduction, while the second bed promotes CO and VOC oxidation and NOx reduction during the start-up phase. The system also ensures a beneficial mixture of NO and NO2 in the exhaust gas, which promotes faster NOx reduction on the SCR catalyst. The first and second beds can be located a distance apart to allow for higher conversion.

Problems solved by technology

However, as exhaust gas temperatures increases from start-up to full load operation, the equilibrium constant for the NO to NO2 reaction is shifted so that the reaction is thermodynamically limited.

Method used

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  • Exhaust system for power generating apparatus
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  • Exhaust system for power generating apparatus

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Embodiment Construction

[0025]In this invention, it has been realized that a coupled oxidation catalyst system, wherein a first bed of oxidation catalyst is placed in a higher temperature region to allow the gas turbine to begin reducing emissions during start-up, and a second bed of oxidation catalyst is placed in a lower temperature region to provide additional catalyst surface and complete the desired CO and VOC reduction once the power generating apparatus has started up, can provide superior overall performance, reduce cost, and be less susceptible to poisoning than the current approach of using a single oxidation catalyst bed.

[0026]The oxidation of CO and VOC in a catalytic system is dependent on the operating temperature and the reaction residence time. The temperature at which an oxidation catalyst begins to oxidize CO and VOCs is called the light-off temperature. The light-off temperature is related to the concentration of active catalyst material in the catalyst. The higher the concentration of t...

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Abstract

An exhaust system for a power generating apparatus comprising a heat source for combusting a fuel in air to produce power, which exhaust system being adapted to receive a flowing exhaust gas and comprising a catalyst system for treating the exhaust gas, which catalyst system comprising a first oxidation catalyst and a second catalyst, wherein the first oxidation catalyst is positioned downstream from the heat source so that the flowing exhaust gas contacts the first oxidation catalyst before the second catalyst.

Description

FIELD OF THE INVENTION[0001]The invention relates to an exhaust system for a power generating apparatus, such as a gas turbine, which exhaust system being adapted to receive a flowing exhaust gas and comprising a catalyst system for treating the exhaust gas, which catalyst system comprising a system of oxidation catalysts. In particular, the invention relates to methods of using such systems to reduce exhaust emissions from a power generating apparatus between start-up of the power generating apparatus and full-load.BACKGROUND[0002]In normal operation, gas turbine power plants generate significant amounts of carbon dioxide (CO2), water, carbon monoxide (CO), volatile organic compounds (VOCs) and oxides of nitrogen (NOx) as part of the combustion process. Various regulatory agencies world-wide, such as the U.S. Environmental Protection Agency, are charged with reducing exhaust emissions.[0003]Gas turbine engines typically operate by drawing air into a compressor to increase the gas p...

Claims

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Application Information

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IPC IPC(8): F01N3/02F01N3/20F01N3/10
CPCF22B37/008F01N3/0205F01N2570/14F01N2570/12F01N3/2066F01N2610/02F01N3/206F01N3/106F01N3/105F01N2570/10Y02E20/16F01N13/0093F01K23/10F01N3/10F02C6/18F22B1/1815
Inventor REPP, DAVID MICHAEL
Owner JOHNSON MATTHEY PLC
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