In-Line Localized Monitoring of Catalyst Activity in Selective Catalytic NOx Reduction Systems

Abstract

Localized catalyst activity in an SCR unit for controlling emissions from a boiler, power plant, or any facility that generates NO x -containing flue gases is monitored by one or more modules that operate on-line without disrupting the normal operation of the facility. Each module is positioned over a designated lateral area of one of the catalyst beds in the SCR unit, and supplies ammonia, urea, or other suitable reductant to the catalyst in the designated area at a rate that produces an excess of the reductant over NO x on a molar basis through the designated area. Sampling probes upstream and downstream of the designated area draw samples of the gas stream for NO x analysis, and the catalyst activity is determined from the difference in NO x levels between the two probes.

1 . A test module for evaluating localized catalytic activity in a selected section of a solid catalyst layer in a selective catalytic NO x  reduction (SCR) unit, said section having lateral area that is less than the full lateral area of said catalyst layer, said test module comprising:
 first and second sampling probes, means for mounting said first and second sampling probes to said SCR unit upstream and downstream, respectively, of said catalyst section, and means for drawing samples of gas through said first and second sampling probes for analysis; and   a reductant supply probe, means for mounting said reductant supply probe to said SCR unit upstream of said catalyst section at a location causing reductant from said reductant supply probe to selectively strike said catalyst section, and means for supplying reductant to said reductant supply probe.   
   
   
       2 . The test module of  claim 1  further comprising a reductant injection grid and means for mounting said reductant injection grid between said reductant supply probe and said catalyst section. 
   
   
       3 . The test module of  claim 1  wherein said reductant supply probe is an atomizer. 
   
   
       4 . The test module of  claim 1  further comprising an air inlet and means for mounting said air inlet upstream of said catalyst section at a location causing air from said air inlet to strike said catalyst section. 
   
   
       5 . The test module of  claim 1  further comprising a temperature sensor and means for mounting said temperature sensor to said SCR unit at a location whose temperature will be at least approximately equal to the temperature of said catalyst section. 
   
   
       6 . The test module of  claim 1  further comprising a velocity sensor and means for mounting said velocity sensor to said SCR unit at a location where the velocity of gas will be at least approximately equal to the velocity of gas through said catalyst section. 
   
   
       7 - 11 . (canceled) 
   
   
       12 . The test module of  claim 1  wherein said catalyst section occupies a lateral area of from about 0.1 m 2  to about 1 m 2 . 
   
   
       13 . The test module of  claim 1  wherein said catalyst section occupies a lateral area of from about 0.2 m 2  to about 0.5 m 2 . 
   
   
       14 - 15 . (canceled) 
   
   
       16 . The test module of  claim 1  further comprising a portable NO x  analyzer and means for mounting said analyzer to said first and second sampling probes. 
   
   
       17 . A method for monitoring localized catalyst activity in a selective catalytic NO x  reduction (SCR) unit in which a NO x -containing gas stream is passing at a known area velocity through a body of catalyst arranged in a layer that is oriented transverse to said NO x -containing gas stream, said method comprising:
 (a) feeding reductant to a selected, laterally delineated, section of said body of catalyst, said selected section having a lateral area that is less than the full lateral area of said body of catalyst, through a reductant supply probe upstream of, and selectively directed to, said selected section, to achieve a molar excess of reductant over NO x  in said NO x -containing gas stream entering said selected section;   (b) drawing samples of said NO x -containing gas stream from sites upstream and downstream of said selected section and analyzing said samples for a difference in NOx content between said samples; and   (c) from said difference in NO x  content and said area velocity, determining a value representative of the catalyst activity of the catalyst in said selected section.   
   
   
       18 . The method of  claim 17  wherein said reductant is ammonia gas. 
   
   
       19 . The method of  claim 17  wherein said reductant is aqueous urea. 
   
   
       20 . (canceled) 
   
   
       21 . The method of  claim 17  further comprising detecting the temperature of said NO x -containing gas stream passing through said selected section. 
   
   
       22 . The method of  claim 17  further comprising detecting the velocity of said NO x -containing gas stream passing through said selected section. 
   
   
       23 . The method of  claim 17  comprising performing steps (a), (b), and (c) at a plurality of mutually distinct, laterally delineated sections of said body of catalyst and determining a value representative of the catalyst activity of the catalyst in each of said sections. 
   
   
       24 . The method of  claim 17  wherein said NO x -containing gas stream is passing through a plurality of bodies of catalyst arranged in separate layers oriented transverse to said NO x -containing gas stream, said method comprising performing steps (a), (b), and (c) at a plurality of mutually distinct, laterally delineated catalyst sections in different layers and determining a value representative of the catalyst activity of the catalyst in each of said sections. 
   
   
       25 . (canceled) 
   
   
       26 . The method of  claim 17  wherein said selected section of said body of catalyst occupies a laterally delineated area of from about 0.1 m 2  to about 1 m 2 . 
   
   
       27 . The method of  claim 17  wherein said selected section of said body of catalyst occupies a laterally delineated area of from about 0.2 m 2  to about 0.5 m 2 . 
   
   
       28 . (canceled) 
   
   
       29 . (canceled) 
   
   
       30 . The method of  claims 23  or  24  further comprising:
 feeding reductant from a single source of reductant through a first stepping valve having a separate outlet port for each of said catalyst sections;   drawing samples of said NO x -containing gas stream from paired sites upstream and downstream of each of said catalyst sections into separate pairs of inlet ports of a second stepping valve, and   advancing said first and second stepping valves in coordinated manner to feed reductant to and draw NO x -containing gas stream samples from each of said catalyst sections in succession.   
   
   
       31 . A selective catalytic NO x  reduction unit with on-line monitoring of localized catalyst activity, said unit comprising:
 a flow-through reaction vessel having a flow direction therethrough and comprising a body of solid catalyst arranged therein in a layer transverse to said flow direction;   an inlet sampling probe and an outlet sampling probe mounted inside said reaction vessel upstream and downstream, respectively, of a selected section of said body of catalyst, said selected section having a lateral area that is less than the full lateral area of said layer, at locations such that samples of gas drawn through said sampling probes have the same composition as gas entering and leaving said selected section, respectively, and means for drawing samples of gas through said inlet and outlet sampling probes and for analyzing samples so drawn for NO x  content;   a reductant supply probe mounted inside said reaction vessel upstream of said selected section to selectively direct reductant to said selected section; and   a data processor for receiving a signal representative of a difference in NOx content between samples of gas drawn through said inlet and outlet sampling probes, and for determining from said signal and from the area velocity of gas through said reaction vessel a value representative of the catalyst activity of the catalyst in said selected section.   
   
   
       32 . The selective catalytic NO x  reduction unit of  claim 31  further comprising a temperature sensor mounted to said reaction vessel at a location whose temperature is substantially equal to that of gas flowing through said selected section. 
   
   
       33 . The selective catalytic NO x  reduction unit of  claim 31  comprising a plurality of monitoring modules, each module comprising a single pair of inlet and outlet sampling probes and a single reductant supply probe, each module feeding reductant to and drawing samples from a laterally delineated section of said layer of catalyst that is distinct from sections so fed and drawn from by all other modules. 
   
   
       34 . The selective catalytic NO x  reduction unit of  claim 32  comprising a plurality of monitoring modules, each module comprising a single pair of inlet and outlet sampling probes, a single reductant supply probe, and a single temperature sensor, each module feeding reductant to and drawing samples from a laterally delineated section of said layer of catalyst that is distinct from sections so fed and drawn from by all other modules. 
   
   
       35 . The selective catalytic NO x  reduction unit of  claim 33  wherein said modules are positioned at distinct laterally delineated sections of a single layer of said body of catalyst. 
   
   
       36 . The selective catalytic NO x  reduction unit of  claim 33  wherein said flow-through reaction vessel comprises a plurality of layers of said body of solid catalyst, and said modules are distributed among different layers. 
   
   
       37 . The selective catalytic NO x  reduction unit of  claims 35  or  36  further comprising a common source of reductant for all of said modules. 
   
   
       38 . (canceled) 
   
   
       39 . The selective catalytic NO x  reduction unit of  claim 31  further comprising a reductant injection grid mounted inside said reaction vessel between said reductant supply probe and said catalyst section. 
   
   
       40 . The selective catalytic NO x  reduction unit of  claim 31  further comprising an air inlet mounted inside said reaction vessel upstream of said catalyst section at a location causing air from said air inlet to strike said catalyst section. 
   
   
       41 . (canceled) 
   
   
       42 . The selective catalytic NO x  reduction unit of  claim 31  further comprising a static mixer mounted to said reaction vessel between said ammonia supply probe and said catalyst section. 
   
   
       43 . The selective catalytic NO x  reduction unit of  claim 31  further comprising a gas flow guide arranged to direct gas entering said catalyst section to a substantially parallel flow direction that is substantially perpendicular to said layer of solid catalyst. 
   
   
       44 . (canceled) 
   
   
       45 . (canceled) 
   
   
       46 . The selective catalytic NO x  reduction unit of  claim 33  further comprising:
 a first stepping valve having a plurality of ports, each port communicating with the reductant supply probe of a different module;   a second stepping valve having a plurality of pairs of ports, each pair communicating with the inlet and outlet sampling probes, respectively, of a different module; and   means for advancing said first and second stepping valves in coordinated manner to feed reductant to, and draw samples of gas from, each of said modules.   
   
   
       47 . The test module of  claim 1  wherein the ratio of said lateral area of said selected section to said lateral area of said catalyst layer is about 0.25 or less. 
   
   
       48 . The test module of  claim 1  wherein the ratio of said lateral area of said selected section to said lateral area of said catalyst layer is about 0.1 or less. 
   
   
       49 . The method of  claim 17  wherein the ratio of said lateral area of said selected section to said lateral area of said body of catalyst is about 0.25 or less. 
   
   
       50 . The method of  claim 17  wherein the ratio of said lateral area of said selected section to said lateral area of said body of catalyst is about 0.1 or less. 
   
   
       51 . The selective catalytic NO x  reduction unit of  claim 31  wherein the ratio of said lateral area of said selected section to said lateral area of said layer of catalyst is about 0.25 or less. 
   
   
       52 . The selective catalytic NO x  reduction unit of  claim 31  wherein the ratio of said lateral area of said selected section to said lateral area of said layer of catalyst is about 0.1 or less.