Advanced oxidation process for coke removal: A systematic study of hydrogen peroxide and OH-derived-Fenton radicals of a fouled zeolite
[Display omitted] •Advanced oxidation processes have been applied on a coked zeolite.•Structure and texture were preserved, while acidity was improved.•Complete catalyst activity recovery was achieved.•Water treatment, followed by H2O2 and finally Fenton process are recommended as methodology guidel...
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creator | Morales, María V. Góra-Marek, Kinga Musch, Hermen Pineda, Antonio Murray, Blaine Stefanidis, Stelios Falco, Lorena Tarach, Karolina Ponomareva, Ekaterina Marsman, Jan Henk Melián-Cabrera, Ignacio |
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•Advanced oxidation processes have been applied on a coked zeolite.•Structure and texture were preserved, while acidity was improved.•Complete catalyst activity recovery was achieved.•Water treatment, followed by H2O2 and finally Fenton process are recommended as methodology guidelines.
The regeneration process of a fouled catalyst typically involves treatments at high temperature which often cause irreversible damages on the catalyst’s properties. In this work, Fenton chemistry-derived OH• species, and H2O2, are proposed as oxidizing agents to reactivate a porous catalyst at mild conditions, below 100 °C. The chosen catalyst is a microporous ZSM-5 zeolite, which is a challenging candidate due to the mass transfer limitations with possible recombination of the hydroxyl radicals; thereby being an obstacle to oxidize organics occluded in the micropores. The organics deposition over a ZSM-5 zeolite during the D-glucose dehydration reaction was confirmed by a number of characterization techniques, which revealed a considerable decrease in the surface area, pore volume and acid site density in the fouled catalyst. By properly selecting the regeneration conditions, reactivation via Fenton or H2O2 was highly effective in terms of removal of the organics as well as recovery of the initial catalytic activity. The properties of the H2O2 treated-zeolite, the optimal treatment in this case study, were preserved with similar structural and textural features and improved acidity. Hot water extraction was ineffective to remove the humins from ZSM-5. Mechanistically, the presence of Fe impurities in the zeolite structure did not allow to discriminate between a homo, heterogeneous, or a direct H2O2 pathway, or a combination of them. The exhibited conversion by the regenerated zeolite was comparable to that of the fresh one. |
doi_str_mv | 10.1016/j.apcata.2018.06.008 |
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•Advanced oxidation processes have been applied on a coked zeolite.•Structure and texture were preserved, while acidity was improved.•Complete catalyst activity recovery was achieved.•Water treatment, followed by H2O2 and finally Fenton process are recommended as methodology guidelines.
The regeneration process of a fouled catalyst typically involves treatments at high temperature which often cause irreversible damages on the catalyst’s properties. In this work, Fenton chemistry-derived OH• species, and H2O2, are proposed as oxidizing agents to reactivate a porous catalyst at mild conditions, below 100 °C. The chosen catalyst is a microporous ZSM-5 zeolite, which is a challenging candidate due to the mass transfer limitations with possible recombination of the hydroxyl radicals; thereby being an obstacle to oxidize organics occluded in the micropores. The organics deposition over a ZSM-5 zeolite during the D-glucose dehydration reaction was confirmed by a number of characterization techniques, which revealed a considerable decrease in the surface area, pore volume and acid site density in the fouled catalyst. By properly selecting the regeneration conditions, reactivation via Fenton or H2O2 was highly effective in terms of removal of the organics as well as recovery of the initial catalytic activity. The properties of the H2O2 treated-zeolite, the optimal treatment in this case study, were preserved with similar structural and textural features and improved acidity. Hot water extraction was ineffective to remove the humins from ZSM-5. Mechanistically, the presence of Fe impurities in the zeolite structure did not allow to discriminate between a homo, heterogeneous, or a direct H2O2 pathway, or a combination of them. The exhibited conversion by the regenerated zeolite was comparable to that of the fresh one.</description><identifier>ISSN: 0926-860X</identifier><identifier>EISSN: 1873-3875</identifier><identifier>DOI: 10.1016/j.apcata.2018.06.008</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>Activation ; Catalysis ; Catalysts ; Catalytic activity ; Coke ; Dehydration ; Feature extraction ; Fenton chemistry ; Fouling ; Hydrogen peroxide ; Hydroxyl radicals ; Mass transfer ; Organic chemistry ; Oxidation ; Oxidizing agents ; Reactivation ; Regeneration ; Zeolites</subject><ispartof>Applied catalysis. A, General, 2018-07, Vol.562, p.215-222</ispartof><rights>2018 Elsevier B.V.</rights><rights>Copyright Elsevier Science SA Jul 25, 2018</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c417t-5c8cea0e715809d98363bbe18dd687bf5817b4c3a7c5d45302ae1ce7207f30893</citedby><cites>FETCH-LOGICAL-c417t-5c8cea0e715809d98363bbe18dd687bf5817b4c3a7c5d45302ae1ce7207f30893</cites><orcidid>0000-0002-6907-1099 ; 0000-0003-0133-4363 ; 0000-0003-2834-0296</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0926860X18302783$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids></links><search><creatorcontrib>Morales, María V.</creatorcontrib><creatorcontrib>Góra-Marek, Kinga</creatorcontrib><creatorcontrib>Musch, Hermen</creatorcontrib><creatorcontrib>Pineda, Antonio</creatorcontrib><creatorcontrib>Murray, Blaine</creatorcontrib><creatorcontrib>Stefanidis, Stelios</creatorcontrib><creatorcontrib>Falco, Lorena</creatorcontrib><creatorcontrib>Tarach, Karolina</creatorcontrib><creatorcontrib>Ponomareva, Ekaterina</creatorcontrib><creatorcontrib>Marsman, Jan Henk</creatorcontrib><creatorcontrib>Melián-Cabrera, Ignacio</creatorcontrib><title>Advanced oxidation process for coke removal: A systematic study of hydrogen peroxide and OH-derived-Fenton radicals of a fouled zeolite</title><title>Applied catalysis. A, General</title><description>[Display omitted]
•Advanced oxidation processes have been applied on a coked zeolite.•Structure and texture were preserved, while acidity was improved.•Complete catalyst activity recovery was achieved.•Water treatment, followed by H2O2 and finally Fenton process are recommended as methodology guidelines.
The regeneration process of a fouled catalyst typically involves treatments at high temperature which often cause irreversible damages on the catalyst’s properties. In this work, Fenton chemistry-derived OH• species, and H2O2, are proposed as oxidizing agents to reactivate a porous catalyst at mild conditions, below 100 °C. The chosen catalyst is a microporous ZSM-5 zeolite, which is a challenging candidate due to the mass transfer limitations with possible recombination of the hydroxyl radicals; thereby being an obstacle to oxidize organics occluded in the micropores. The organics deposition over a ZSM-5 zeolite during the D-glucose dehydration reaction was confirmed by a number of characterization techniques, which revealed a considerable decrease in the surface area, pore volume and acid site density in the fouled catalyst. By properly selecting the regeneration conditions, reactivation via Fenton or H2O2 was highly effective in terms of removal of the organics as well as recovery of the initial catalytic activity. The properties of the H2O2 treated-zeolite, the optimal treatment in this case study, were preserved with similar structural and textural features and improved acidity. Hot water extraction was ineffective to remove the humins from ZSM-5. Mechanistically, the presence of Fe impurities in the zeolite structure did not allow to discriminate between a homo, heterogeneous, or a direct H2O2 pathway, or a combination of them. The exhibited conversion by the regenerated zeolite was comparable to that of the fresh one.</description><subject>Activation</subject><subject>Catalysis</subject><subject>Catalysts</subject><subject>Catalytic activity</subject><subject>Coke</subject><subject>Dehydration</subject><subject>Feature extraction</subject><subject>Fenton chemistry</subject><subject>Fouling</subject><subject>Hydrogen peroxide</subject><subject>Hydroxyl radicals</subject><subject>Mass transfer</subject><subject>Organic chemistry</subject><subject>Oxidation</subject><subject>Oxidizing agents</subject><subject>Reactivation</subject><subject>Regeneration</subject><subject>Zeolites</subject><issn>0926-860X</issn><issn>1873-3875</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2018</creationdate><recordtype>article</recordtype><recordid>eNp9kE1LAzEQhoMoWD_-gYeA510nm91N1oNQxC8QvCh4C2kyq6ntpiZpsf4B_7ZZ6tnTHOZ9n2EeQs4YlAxYezEv9cropMsKmCyhLQHkHpkwKXjBpWj2yQS6qi1kC6-H5CjGOQBUdddMyM_UbvRg0FL_5axOzg90FbzBGGnvAzX-A2nApd_oxSWd0riNCZc5Z2hMa7ulvqfvWxv8G-YihpGCVA-WPt0XFoPboC1ucUiZG7R1Ri_i2NGZvl7ks9_oFy7hCTno8wpP_-Yxebm9eb6-Lx6f7h6up4-FqZlIRWOkQQ0oWCOhs53kLZ_NkElrWylmfSOZmNWGa2EaWzccKo3MoKhA9Bxkx4_J-Y6bn_xcY0xq7tdhyCdVxVgreScbnlP1LmWCjzFgr1bBLXXYKgZqVK7maqdcjcoVtCorz7WrXQ3zBxuHQUXjcLTrApqkrHf_A34BlSONug</recordid><startdate>20180725</startdate><enddate>20180725</enddate><creator>Morales, María V.</creator><creator>Góra-Marek, Kinga</creator><creator>Musch, Hermen</creator><creator>Pineda, Antonio</creator><creator>Murray, Blaine</creator><creator>Stefanidis, Stelios</creator><creator>Falco, Lorena</creator><creator>Tarach, Karolina</creator><creator>Ponomareva, Ekaterina</creator><creator>Marsman, Jan Henk</creator><creator>Melián-Cabrera, Ignacio</creator><general>Elsevier B.V</general><general>Elsevier Science SA</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>JG9</scope><scope>L7M</scope><orcidid>https://orcid.org/0000-0002-6907-1099</orcidid><orcidid>https://orcid.org/0000-0003-0133-4363</orcidid><orcidid>https://orcid.org/0000-0003-2834-0296</orcidid></search><sort><creationdate>20180725</creationdate><title>Advanced oxidation process for coke removal: A systematic study of hydrogen peroxide and OH-derived-Fenton radicals of a fouled zeolite</title><author>Morales, María V. ; Góra-Marek, Kinga ; Musch, Hermen ; Pineda, Antonio ; Murray, Blaine ; Stefanidis, Stelios ; Falco, Lorena ; Tarach, Karolina ; Ponomareva, Ekaterina ; Marsman, Jan Henk ; Melián-Cabrera, Ignacio</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c417t-5c8cea0e715809d98363bbe18dd687bf5817b4c3a7c5d45302ae1ce7207f30893</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2018</creationdate><topic>Activation</topic><topic>Catalysis</topic><topic>Catalysts</topic><topic>Catalytic activity</topic><topic>Coke</topic><topic>Dehydration</topic><topic>Feature extraction</topic><topic>Fenton chemistry</topic><topic>Fouling</topic><topic>Hydrogen peroxide</topic><topic>Hydroxyl radicals</topic><topic>Mass transfer</topic><topic>Organic chemistry</topic><topic>Oxidation</topic><topic>Oxidizing agents</topic><topic>Reactivation</topic><topic>Regeneration</topic><topic>Zeolites</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Morales, María V.</creatorcontrib><creatorcontrib>Góra-Marek, Kinga</creatorcontrib><creatorcontrib>Musch, Hermen</creatorcontrib><creatorcontrib>Pineda, Antonio</creatorcontrib><creatorcontrib>Murray, Blaine</creatorcontrib><creatorcontrib>Stefanidis, Stelios</creatorcontrib><creatorcontrib>Falco, Lorena</creatorcontrib><creatorcontrib>Tarach, Karolina</creatorcontrib><creatorcontrib>Ponomareva, Ekaterina</creatorcontrib><creatorcontrib>Marsman, Jan Henk</creatorcontrib><creatorcontrib>Melián-Cabrera, Ignacio</creatorcontrib><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><jtitle>Applied catalysis. A, General</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Morales, María V.</au><au>Góra-Marek, Kinga</au><au>Musch, Hermen</au><au>Pineda, Antonio</au><au>Murray, Blaine</au><au>Stefanidis, Stelios</au><au>Falco, Lorena</au><au>Tarach, Karolina</au><au>Ponomareva, Ekaterina</au><au>Marsman, Jan Henk</au><au>Melián-Cabrera, Ignacio</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Advanced oxidation process for coke removal: A systematic study of hydrogen peroxide and OH-derived-Fenton radicals of a fouled zeolite</atitle><jtitle>Applied catalysis. A, General</jtitle><date>2018-07-25</date><risdate>2018</risdate><volume>562</volume><spage>215</spage><epage>222</epage><pages>215-222</pages><issn>0926-860X</issn><eissn>1873-3875</eissn><abstract>[Display omitted]
•Advanced oxidation processes have been applied on a coked zeolite.•Structure and texture were preserved, while acidity was improved.•Complete catalyst activity recovery was achieved.•Water treatment, followed by H2O2 and finally Fenton process are recommended as methodology guidelines.
The regeneration process of a fouled catalyst typically involves treatments at high temperature which often cause irreversible damages on the catalyst’s properties. In this work, Fenton chemistry-derived OH• species, and H2O2, are proposed as oxidizing agents to reactivate a porous catalyst at mild conditions, below 100 °C. The chosen catalyst is a microporous ZSM-5 zeolite, which is a challenging candidate due to the mass transfer limitations with possible recombination of the hydroxyl radicals; thereby being an obstacle to oxidize organics occluded in the micropores. The organics deposition over a ZSM-5 zeolite during the D-glucose dehydration reaction was confirmed by a number of characterization techniques, which revealed a considerable decrease in the surface area, pore volume and acid site density in the fouled catalyst. By properly selecting the regeneration conditions, reactivation via Fenton or H2O2 was highly effective in terms of removal of the organics as well as recovery of the initial catalytic activity. The properties of the H2O2 treated-zeolite, the optimal treatment in this case study, were preserved with similar structural and textural features and improved acidity. Hot water extraction was ineffective to remove the humins from ZSM-5. Mechanistically, the presence of Fe impurities in the zeolite structure did not allow to discriminate between a homo, heterogeneous, or a direct H2O2 pathway, or a combination of them. The exhibited conversion by the regenerated zeolite was comparable to that of the fresh one.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/j.apcata.2018.06.008</doi><tpages>8</tpages><orcidid>https://orcid.org/0000-0002-6907-1099</orcidid><orcidid>https://orcid.org/0000-0003-0133-4363</orcidid><orcidid>https://orcid.org/0000-0003-2834-0296</orcidid><oa>free_for_read</oa></addata></record> |
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subjects | Activation Catalysis Catalysts Catalytic activity Coke Dehydration Feature extraction Fenton chemistry Fouling Hydrogen peroxide Hydroxyl radicals Mass transfer Organic chemistry Oxidation Oxidizing agents Reactivation Regeneration Zeolites |
title | Advanced oxidation process for coke removal: A systematic study of hydrogen peroxide and OH-derived-Fenton radicals of a fouled zeolite |
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