NO Reduction Studies in the FCC Process. Evaluation of NO Reduction Additives for FCCU in Bench- and Pilot Plant-Scale Reactors
During FCC catalyst regeneration, part of the nitrogen in coke forms NO x , which makes up a significant part of the total NO x refinery emissions. The addition of a small percentage (≤1 wt %) of catalytic additive(s) in the FCC inventory can reduce the NO x emissions from the flue gases of the FCC...
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creator | Efthimiadis, E. A Iliopoulou, E. F Lappas, A. A Iatridis, D. K Vasalos, I. A |
description | During FCC catalyst regeneration, part of the nitrogen in coke forms NO x , which makes up a significant part of the total NO x refinery emissions. The addition of a small percentage (≤1 wt %) of catalytic additive(s) in the FCC inventory can reduce the NO x emissions from the flue gases of the FCC regenerator. In this paper, experimental techniques are considered for evaluating, in laboratory reactors, the performance of two commercially available NO x removal additives. It has been shown that in an FCC regenerator the gas residence time and the concentration of CO in the flue gases are key parameters in controlling NO x emissions. For example, pilot plant experiments showed that the addition of a CO oxidation promoter (CP-3) in the catalytic inventory decreases the CO emissions significantly and increases the NO x emissions about 4 times. Replacement of the active CO oxidation promoter (CP-3) with an additive (XNO x ) with moderate CO oxidation activity reduced the NO x emissions by 78%. Comparison of regeneration results performed in bench-scale reactors with those measured in our FCC pilot plant unit showed that it is possible to evaluate NO x reduction additives in bench-scale experiments. The proposed protocol for this evaluation is to mix spent FCC catalyst with the NO x reduction additive and to load this mixture in a fluidized bed reactor. The above mixture is then regenerated at 700 °C by 2% O2 diluted in N2. |
doi_str_mv | 10.1021/ie020265h |
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Evaluation of NO Reduction Additives for FCCU in Bench- and Pilot Plant-Scale Reactors</title><source>ACS Publications</source><creator>Efthimiadis, E. A ; Iliopoulou, E. F ; Lappas, A. A ; Iatridis, D. K ; Vasalos, I. A</creator><creatorcontrib>Efthimiadis, E. A ; Iliopoulou, E. F ; Lappas, A. A ; Iatridis, D. K ; Vasalos, I. A</creatorcontrib><description>During FCC catalyst regeneration, part of the nitrogen in coke forms NO x , which makes up a significant part of the total NO x refinery emissions. The addition of a small percentage (≤1 wt %) of catalytic additive(s) in the FCC inventory can reduce the NO x emissions from the flue gases of the FCC regenerator. In this paper, experimental techniques are considered for evaluating, in laboratory reactors, the performance of two commercially available NO x removal additives. It has been shown that in an FCC regenerator the gas residence time and the concentration of CO in the flue gases are key parameters in controlling NO x emissions. For example, pilot plant experiments showed that the addition of a CO oxidation promoter (CP-3) in the catalytic inventory decreases the CO emissions significantly and increases the NO x emissions about 4 times. Replacement of the active CO oxidation promoter (CP-3) with an additive (XNO x ) with moderate CO oxidation activity reduced the NO x emissions by 78%. Comparison of regeneration results performed in bench-scale reactors with those measured in our FCC pilot plant unit showed that it is possible to evaluate NO x reduction additives in bench-scale experiments. The proposed protocol for this evaluation is to mix spent FCC catalyst with the NO x reduction additive and to load this mixture in a fluidized bed reactor. 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A</creatorcontrib><creatorcontrib>Iliopoulou, E. F</creatorcontrib><creatorcontrib>Lappas, A. A</creatorcontrib><creatorcontrib>Iatridis, D. K</creatorcontrib><creatorcontrib>Vasalos, I. A</creatorcontrib><title>NO Reduction Studies in the FCC Process. Evaluation of NO Reduction Additives for FCCU in Bench- and Pilot Plant-Scale Reactors</title><title>Industrial & engineering chemistry research</title><addtitle>Ind. Eng. Chem. Res</addtitle><description>During FCC catalyst regeneration, part of the nitrogen in coke forms NO x , which makes up a significant part of the total NO x refinery emissions. The addition of a small percentage (≤1 wt %) of catalytic additive(s) in the FCC inventory can reduce the NO x emissions from the flue gases of the FCC regenerator. In this paper, experimental techniques are considered for evaluating, in laboratory reactors, the performance of two commercially available NO x removal additives. It has been shown that in an FCC regenerator the gas residence time and the concentration of CO in the flue gases are key parameters in controlling NO x emissions. For example, pilot plant experiments showed that the addition of a CO oxidation promoter (CP-3) in the catalytic inventory decreases the CO emissions significantly and increases the NO x emissions about 4 times. Replacement of the active CO oxidation promoter (CP-3) with an additive (XNO x ) with moderate CO oxidation activity reduced the NO x emissions by 78%. Comparison of regeneration results performed in bench-scale reactors with those measured in our FCC pilot plant unit showed that it is possible to evaluate NO x reduction additives in bench-scale experiments. The proposed protocol for this evaluation is to mix spent FCC catalyst with the NO x reduction additive and to load this mixture in a fluidized bed reactor. The above mixture is then regenerated at 700 °C by 2% O2 diluted in N2.</description><subject>Applied sciences</subject><subject>Crude oil, natural gas and petroleum products</subject><subject>Energy</subject><subject>Exact sciences and technology</subject><subject>Fuels</subject><subject>Processing of crude oil and oils from shales and tar sands. Processes. Equipment. 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A</creator><general>American Chemical Society</general><scope>BSCLL</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20021030</creationdate><title>NO Reduction Studies in the FCC Process. Evaluation of NO Reduction Additives for FCCU in Bench- and Pilot Plant-Scale Reactors</title><author>Efthimiadis, E. A ; Iliopoulou, E. F ; Lappas, A. A ; Iatridis, D. K ; Vasalos, I. A</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a362t-1108e63f3818f4c122dfffd696d81388272c9799528024d74b56c9406a9f50903</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2002</creationdate><topic>Applied sciences</topic><topic>Crude oil, natural gas and petroleum products</topic><topic>Energy</topic><topic>Exact sciences and technology</topic><topic>Fuels</topic><topic>Processing of crude oil and oils from shales and tar sands. Processes. Equipment. Refinery and treatment units</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Efthimiadis, E. A</creatorcontrib><creatorcontrib>Iliopoulou, E. F</creatorcontrib><creatorcontrib>Lappas, A. A</creatorcontrib><creatorcontrib>Iatridis, D. K</creatorcontrib><creatorcontrib>Vasalos, I. A</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><jtitle>Industrial & engineering chemistry research</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Efthimiadis, E. A</au><au>Iliopoulou, E. F</au><au>Lappas, A. A</au><au>Iatridis, D. K</au><au>Vasalos, I. A</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>NO Reduction Studies in the FCC Process. Evaluation of NO Reduction Additives for FCCU in Bench- and Pilot Plant-Scale Reactors</atitle><jtitle>Industrial & engineering chemistry research</jtitle><addtitle>Ind. Eng. Chem. Res</addtitle><date>2002-10-30</date><risdate>2002</risdate><volume>41</volume><issue>22</issue><spage>5401</spage><epage>5409</epage><pages>5401-5409</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><coden>IECRED</coden><abstract>During FCC catalyst regeneration, part of the nitrogen in coke forms NO x , which makes up a significant part of the total NO x refinery emissions. The addition of a small percentage (≤1 wt %) of catalytic additive(s) in the FCC inventory can reduce the NO x emissions from the flue gases of the FCC regenerator. In this paper, experimental techniques are considered for evaluating, in laboratory reactors, the performance of two commercially available NO x removal additives. It has been shown that in an FCC regenerator the gas residence time and the concentration of CO in the flue gases are key parameters in controlling NO x emissions. For example, pilot plant experiments showed that the addition of a CO oxidation promoter (CP-3) in the catalytic inventory decreases the CO emissions significantly and increases the NO x emissions about 4 times. Replacement of the active CO oxidation promoter (CP-3) with an additive (XNO x ) with moderate CO oxidation activity reduced the NO x emissions by 78%. Comparison of regeneration results performed in bench-scale reactors with those measured in our FCC pilot plant unit showed that it is possible to evaluate NO x reduction additives in bench-scale experiments. The proposed protocol for this evaluation is to mix spent FCC catalyst with the NO x reduction additive and to load this mixture in a fluidized bed reactor. The above mixture is then regenerated at 700 °C by 2% O2 diluted in N2.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/ie020265h</doi><tpages>9</tpages></addata></record> |
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subjects | Applied sciences Crude oil, natural gas and petroleum products Energy Exact sciences and technology Fuels Processing of crude oil and oils from shales and tar sands. Processes. Equipment. Refinery and treatment units |
title | NO Reduction Studies in the FCC Process. Evaluation of NO Reduction Additives for FCCU in Bench- and Pilot Plant-Scale Reactors |
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