Kinetics Study of Al Extraction from Desilicated Coal Fly Ash by NaOH at Atmospheric Pressure

The most promising source of alumina in the 21st century is the coal fly ash (CFA) waste of coal-fired thermal plants. The methods of alumina extraction from CFA are often based on the pressure alkaline or acid leaching or preliminary roasting with different additives followed by water leaching. The...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:Materials 2021-12, Vol.14 (24), p.7700
Hauptverfasser: Shoppert, Andrei, Loginova, Irina, Valeev, Dmitry
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page
container_issue 24
container_start_page 7700
container_title Materials
container_volume 14
creator Shoppert, Andrei
Loginova, Irina
Valeev, Dmitry
description The most promising source of alumina in the 21st century is the coal fly ash (CFA) waste of coal-fired thermal plants. The methods of alumina extraction from CFA are often based on the pressure alkaline or acid leaching or preliminary roasting with different additives followed by water leaching. The efficiency of the alumina extraction from CFA under atmospheric pressure leaching is low due to the high content of acid-insoluble alumina phase mullite (3Al O ·2SiO ). This research for the first time shows the possibility of mullite leaching under atmospheric pressure after preliminary desilication using high liquid to solid ratios (L:S ratio) and Na O concentration. The analysis of the desilicated CFA (DCFA) chemical and phase composition before and after leaching has been carried out by inductively coupled plasma optical emission spectrometry (ICP-OES) and X-ray diffraction (XRD). The morphology and elemental composition of solid product particles has been carried out by scanning electron microscopy with energy-dispersive X-ray spectroscopy (SEM-EDX). An automated neural network and a shrinking core model (SCM) were used to evaluate experimental data. The Al extraction efficiency from DCFA has been more than 84% at T = 120 °C, leaching time 60 min, the L/S ratio > 20, and concentration of Na O-400 g L . The kinetics analysis by SCM has shown that the surface chemical reaction controls the leaching process rate at T < 110 °C, and, at T > 110 °C after 15 min of leaching, the process is limited by diffusion through the product layer, which can be represented by titanium compounds. According to the SEM-EDX analysis of the solid residue, the magnetite spheres and mullite acicular particles were the main phases that remained after NaOH leaching. The spheric agglomerates of mullite particles with non-porous surface have also been found.
doi_str_mv 10.3390/ma14247700
format Article
fullrecord <record><control><sourceid>proquest_pubme</sourceid><recordid>TN_cdi_pubmedcentral_primary_oai_pubmedcentral_nih_gov_8707349</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>2612803872</sourcerecordid><originalsourceid>FETCH-LOGICAL-c406t-4cbab859ed77531e4db6d8f3561722c766ffc14b999a22600af5133bf82d2c13</originalsourceid><addsrcrecordid>eNpdkVtLAzEQhYMoKtoXf4AEfBGhmls3mxeh1HpBsYK-SshmExvZ3dQkK_bfm-LdeZmB-TicmQPAHkbHlAp00irMCOMcoTWwjYUohlgwtv5r3gKDGJ9RLkpxScQm2KJMME4R3QaP164zyekI71NfL6G3cNzA6VsKSifnO2iDb-GZia5xWiVTw4lXDTxvlnAc57Bawls1u4QqwXFqfVzMTXAa3gUTYx_MLtiwqolm8Nl3wMP59GFyObyZXVxNxjdDzVCRhkxXqipHwtScjyg2rK6KurR0VGBOiOZFYa3GrBJCKEIKhJQdYUorW5KaaEx3wOmH7KKvWlNr02X7jVwE16qwlF45-XfTubl88q-y5IjnX2SBw0-B4F96E5NsXdSmaVRnfB8lKfKTaSZJRg_-oc--D12-bkWREtGSr6ijD0oHH2Mw9tsMRnKVm_zJLcP7v-1_o18p0XfQ_ZH0</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>2612803872</pqid></control><display><type>article</type><title>Kinetics Study of Al Extraction from Desilicated Coal Fly Ash by NaOH at Atmospheric Pressure</title><source>MDPI - Multidisciplinary Digital Publishing Institute</source><source>PubMed Central</source><source>Free Full-Text Journals in Chemistry</source><source>EZB Electronic Journals Library</source><source>PubMed Central Open Access</source><creator>Shoppert, Andrei ; Loginova, Irina ; Valeev, Dmitry</creator><creatorcontrib>Shoppert, Andrei ; Loginova, Irina ; Valeev, Dmitry</creatorcontrib><description>The most promising source of alumina in the 21st century is the coal fly ash (CFA) waste of coal-fired thermal plants. The methods of alumina extraction from CFA are often based on the pressure alkaline or acid leaching or preliminary roasting with different additives followed by water leaching. The efficiency of the alumina extraction from CFA under atmospheric pressure leaching is low due to the high content of acid-insoluble alumina phase mullite (3Al O ·2SiO ). This research for the first time shows the possibility of mullite leaching under atmospheric pressure after preliminary desilication using high liquid to solid ratios (L:S ratio) and Na O concentration. The analysis of the desilicated CFA (DCFA) chemical and phase composition before and after leaching has been carried out by inductively coupled plasma optical emission spectrometry (ICP-OES) and X-ray diffraction (XRD). The morphology and elemental composition of solid product particles has been carried out by scanning electron microscopy with energy-dispersive X-ray spectroscopy (SEM-EDX). An automated neural network and a shrinking core model (SCM) were used to evaluate experimental data. The Al extraction efficiency from DCFA has been more than 84% at T = 120 °C, leaching time 60 min, the L/S ratio &gt; 20, and concentration of Na O-400 g L . The kinetics analysis by SCM has shown that the surface chemical reaction controls the leaching process rate at T &lt; 110 °C, and, at T &gt; 110 °C after 15 min of leaching, the process is limited by diffusion through the product layer, which can be represented by titanium compounds. According to the SEM-EDX analysis of the solid residue, the magnetite spheres and mullite acicular particles were the main phases that remained after NaOH leaching. The spheric agglomerates of mullite particles with non-porous surface have also been found.</description><identifier>ISSN: 1996-1944</identifier><identifier>EISSN: 1996-1944</identifier><identifier>DOI: 10.3390/ma14247700</identifier><identifier>PMID: 34947303</identifier><language>eng</language><publisher>Switzerland: MDPI AG</publisher><subject>Acid leaching ; Acids ; Additives ; Alumina ; Aluminum oxide ; Atmospheric pressure ; Boilers ; Chemical composition ; Chemical reactions ; Coal ; Coal-fired power plants ; Diffusion layers ; Energy dispersive X ray spectroscopy ; Fly ash ; Inductively coupled plasma ; Kinetics ; Methods ; Minerals ; Mullite ; Nanoparticles ; Neural networks ; Optical emission spectroscopy ; Particle size ; Phase composition ; Pressure leaching ; Reagents ; Scanning electron microscopy ; Shrinking core model ; Titanium compounds</subject><ispartof>Materials, 2021-12, Vol.14 (24), p.7700</ispartof><rights>2021 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/). Notwithstanding the ProQuest Terms and Conditions, you may use this content in accordance with the terms of the License.</rights><rights>2021 by the authors. 2021</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c406t-4cbab859ed77531e4db6d8f3561722c766ffc14b999a22600af5133bf82d2c13</citedby><cites>FETCH-LOGICAL-c406t-4cbab859ed77531e4db6d8f3561722c766ffc14b999a22600af5133bf82d2c13</cites><orcidid>0000-0002-8820-7502 ; 0000-0002-9684-9628</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://www.ncbi.nlm.nih.gov/pmc/articles/PMC8707349/pdf/$$EPDF$$P50$$Gpubmedcentral$$Hfree_for_read</linktopdf><linktohtml>$$Uhttps://www.ncbi.nlm.nih.gov/pmc/articles/PMC8707349/$$EHTML$$P50$$Gpubmedcentral$$Hfree_for_read</linktohtml><link.rule.ids>230,314,727,780,784,885,27924,27925,53791,53793</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/34947303$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Shoppert, Andrei</creatorcontrib><creatorcontrib>Loginova, Irina</creatorcontrib><creatorcontrib>Valeev, Dmitry</creatorcontrib><title>Kinetics Study of Al Extraction from Desilicated Coal Fly Ash by NaOH at Atmospheric Pressure</title><title>Materials</title><addtitle>Materials (Basel)</addtitle><description>The most promising source of alumina in the 21st century is the coal fly ash (CFA) waste of coal-fired thermal plants. The methods of alumina extraction from CFA are often based on the pressure alkaline or acid leaching or preliminary roasting with different additives followed by water leaching. The efficiency of the alumina extraction from CFA under atmospheric pressure leaching is low due to the high content of acid-insoluble alumina phase mullite (3Al O ·2SiO ). This research for the first time shows the possibility of mullite leaching under atmospheric pressure after preliminary desilication using high liquid to solid ratios (L:S ratio) and Na O concentration. The analysis of the desilicated CFA (DCFA) chemical and phase composition before and after leaching has been carried out by inductively coupled plasma optical emission spectrometry (ICP-OES) and X-ray diffraction (XRD). The morphology and elemental composition of solid product particles has been carried out by scanning electron microscopy with energy-dispersive X-ray spectroscopy (SEM-EDX). An automated neural network and a shrinking core model (SCM) were used to evaluate experimental data. The Al extraction efficiency from DCFA has been more than 84% at T = 120 °C, leaching time 60 min, the L/S ratio &gt; 20, and concentration of Na O-400 g L . The kinetics analysis by SCM has shown that the surface chemical reaction controls the leaching process rate at T &lt; 110 °C, and, at T &gt; 110 °C after 15 min of leaching, the process is limited by diffusion through the product layer, which can be represented by titanium compounds. According to the SEM-EDX analysis of the solid residue, the magnetite spheres and mullite acicular particles were the main phases that remained after NaOH leaching. The spheric agglomerates of mullite particles with non-porous surface have also been found.</description><subject>Acid leaching</subject><subject>Acids</subject><subject>Additives</subject><subject>Alumina</subject><subject>Aluminum oxide</subject><subject>Atmospheric pressure</subject><subject>Boilers</subject><subject>Chemical composition</subject><subject>Chemical reactions</subject><subject>Coal</subject><subject>Coal-fired power plants</subject><subject>Diffusion layers</subject><subject>Energy dispersive X ray spectroscopy</subject><subject>Fly ash</subject><subject>Inductively coupled plasma</subject><subject>Kinetics</subject><subject>Methods</subject><subject>Minerals</subject><subject>Mullite</subject><subject>Nanoparticles</subject><subject>Neural networks</subject><subject>Optical emission spectroscopy</subject><subject>Particle size</subject><subject>Phase composition</subject><subject>Pressure leaching</subject><subject>Reagents</subject><subject>Scanning electron microscopy</subject><subject>Shrinking core model</subject><subject>Titanium compounds</subject><issn>1996-1944</issn><issn>1996-1944</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><sourceid>ABUWG</sourceid><sourceid>AFKRA</sourceid><sourceid>AZQEC</sourceid><sourceid>BENPR</sourceid><sourceid>CCPQU</sourceid><sourceid>DWQXO</sourceid><recordid>eNpdkVtLAzEQhYMoKtoXf4AEfBGhmls3mxeh1HpBsYK-SshmExvZ3dQkK_bfm-LdeZmB-TicmQPAHkbHlAp00irMCOMcoTWwjYUohlgwtv5r3gKDGJ9RLkpxScQm2KJMME4R3QaP164zyekI71NfL6G3cNzA6VsKSifnO2iDb-GZia5xWiVTw4lXDTxvlnAc57Bawls1u4QqwXFqfVzMTXAa3gUTYx_MLtiwqolm8Nl3wMP59GFyObyZXVxNxjdDzVCRhkxXqipHwtScjyg2rK6KurR0VGBOiOZFYa3GrBJCKEIKhJQdYUorW5KaaEx3wOmH7KKvWlNr02X7jVwE16qwlF45-XfTubl88q-y5IjnX2SBw0-B4F96E5NsXdSmaVRnfB8lKfKTaSZJRg_-oc--D12-bkWREtGSr6ijD0oHH2Mw9tsMRnKVm_zJLcP7v-1_o18p0XfQ_ZH0</recordid><startdate>20211213</startdate><enddate>20211213</enddate><creator>Shoppert, Andrei</creator><creator>Loginova, Irina</creator><creator>Valeev, Dmitry</creator><general>MDPI AG</general><general>MDPI</general><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>8FD</scope><scope>8FE</scope><scope>8FG</scope><scope>ABJCF</scope><scope>ABUWG</scope><scope>AFKRA</scope><scope>AZQEC</scope><scope>BENPR</scope><scope>BGLVJ</scope><scope>CCPQU</scope><scope>D1I</scope><scope>DWQXO</scope><scope>HCIFZ</scope><scope>JG9</scope><scope>KB.</scope><scope>PDBOC</scope><scope>PIMPY</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PRINS</scope><scope>7X8</scope><scope>5PM</scope><orcidid>https://orcid.org/0000-0002-8820-7502</orcidid><orcidid>https://orcid.org/0000-0002-9684-9628</orcidid></search><sort><creationdate>20211213</creationdate><title>Kinetics Study of Al Extraction from Desilicated Coal Fly Ash by NaOH at Atmospheric Pressure</title><author>Shoppert, Andrei ; Loginova, Irina ; Valeev, Dmitry</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c406t-4cbab859ed77531e4db6d8f3561722c766ffc14b999a22600af5133bf82d2c13</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2021</creationdate><topic>Acid leaching</topic><topic>Acids</topic><topic>Additives</topic><topic>Alumina</topic><topic>Aluminum oxide</topic><topic>Atmospheric pressure</topic><topic>Boilers</topic><topic>Chemical composition</topic><topic>Chemical reactions</topic><topic>Coal</topic><topic>Coal-fired power plants</topic><topic>Diffusion layers</topic><topic>Energy dispersive X ray spectroscopy</topic><topic>Fly ash</topic><topic>Inductively coupled plasma</topic><topic>Kinetics</topic><topic>Methods</topic><topic>Minerals</topic><topic>Mullite</topic><topic>Nanoparticles</topic><topic>Neural networks</topic><topic>Optical emission spectroscopy</topic><topic>Particle size</topic><topic>Phase composition</topic><topic>Pressure leaching</topic><topic>Reagents</topic><topic>Scanning electron microscopy</topic><topic>Shrinking core model</topic><topic>Titanium compounds</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Shoppert, Andrei</creatorcontrib><creatorcontrib>Loginova, Irina</creatorcontrib><creatorcontrib>Valeev, Dmitry</creatorcontrib><collection>PubMed</collection><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Technology Research Database</collection><collection>ProQuest SciTech Collection</collection><collection>ProQuest Technology Collection</collection><collection>Materials Science &amp; Engineering Collection</collection><collection>ProQuest Central (Alumni)</collection><collection>ProQuest Central</collection><collection>ProQuest Central Essentials</collection><collection>ProQuest Central</collection><collection>Technology Collection</collection><collection>ProQuest One Community College</collection><collection>ProQuest Materials Science Collection</collection><collection>ProQuest Central</collection><collection>SciTech Premium Collection (Proquest) (PQ_SDU_P3)</collection><collection>Materials Research Database</collection><collection>Materials Science Database</collection><collection>Materials science collection</collection><collection>Publicly Available Content Database (Proquest) (PQ_SDU_P3)</collection><collection>ProQuest One Academic Eastern Edition (DO NOT USE)</collection><collection>ProQuest One Academic</collection><collection>ProQuest One Academic UKI Edition</collection><collection>ProQuest Central China</collection><collection>MEDLINE - Academic</collection><collection>PubMed Central (Full Participant titles)</collection><jtitle>Materials</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Shoppert, Andrei</au><au>Loginova, Irina</au><au>Valeev, Dmitry</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Kinetics Study of Al Extraction from Desilicated Coal Fly Ash by NaOH at Atmospheric Pressure</atitle><jtitle>Materials</jtitle><addtitle>Materials (Basel)</addtitle><date>2021-12-13</date><risdate>2021</risdate><volume>14</volume><issue>24</issue><spage>7700</spage><pages>7700-</pages><issn>1996-1944</issn><eissn>1996-1944</eissn><abstract>The most promising source of alumina in the 21st century is the coal fly ash (CFA) waste of coal-fired thermal plants. The methods of alumina extraction from CFA are often based on the pressure alkaline or acid leaching or preliminary roasting with different additives followed by water leaching. The efficiency of the alumina extraction from CFA under atmospheric pressure leaching is low due to the high content of acid-insoluble alumina phase mullite (3Al O ·2SiO ). This research for the first time shows the possibility of mullite leaching under atmospheric pressure after preliminary desilication using high liquid to solid ratios (L:S ratio) and Na O concentration. The analysis of the desilicated CFA (DCFA) chemical and phase composition before and after leaching has been carried out by inductively coupled plasma optical emission spectrometry (ICP-OES) and X-ray diffraction (XRD). The morphology and elemental composition of solid product particles has been carried out by scanning electron microscopy with energy-dispersive X-ray spectroscopy (SEM-EDX). An automated neural network and a shrinking core model (SCM) were used to evaluate experimental data. The Al extraction efficiency from DCFA has been more than 84% at T = 120 °C, leaching time 60 min, the L/S ratio &gt; 20, and concentration of Na O-400 g L . The kinetics analysis by SCM has shown that the surface chemical reaction controls the leaching process rate at T &lt; 110 °C, and, at T &gt; 110 °C after 15 min of leaching, the process is limited by diffusion through the product layer, which can be represented by titanium compounds. According to the SEM-EDX analysis of the solid residue, the magnetite spheres and mullite acicular particles were the main phases that remained after NaOH leaching. The spheric agglomerates of mullite particles with non-porous surface have also been found.</abstract><cop>Switzerland</cop><pub>MDPI AG</pub><pmid>34947303</pmid><doi>10.3390/ma14247700</doi><orcidid>https://orcid.org/0000-0002-8820-7502</orcidid><orcidid>https://orcid.org/0000-0002-9684-9628</orcidid><oa>free_for_read</oa></addata></record>
fulltext fulltext
identifier ISSN: 1996-1944
ispartof Materials, 2021-12, Vol.14 (24), p.7700
issn 1996-1944
1996-1944
language eng
recordid cdi_pubmedcentral_primary_oai_pubmedcentral_nih_gov_8707349
source MDPI - Multidisciplinary Digital Publishing Institute; PubMed Central; Free Full-Text Journals in Chemistry; EZB Electronic Journals Library; PubMed Central Open Access
subjects Acid leaching
Acids
Additives
Alumina
Aluminum oxide
Atmospheric pressure
Boilers
Chemical composition
Chemical reactions
Coal
Coal-fired power plants
Diffusion layers
Energy dispersive X ray spectroscopy
Fly ash
Inductively coupled plasma
Kinetics
Methods
Minerals
Mullite
Nanoparticles
Neural networks
Optical emission spectroscopy
Particle size
Phase composition
Pressure leaching
Reagents
Scanning electron microscopy
Shrinking core model
Titanium compounds
title Kinetics Study of Al Extraction from Desilicated Coal Fly Ash by NaOH at Atmospheric Pressure
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-25T09%3A24%3A07IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_pubme&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Kinetics%20Study%20of%20Al%20Extraction%20from%20Desilicated%20Coal%20Fly%20Ash%20by%20NaOH%20at%20Atmospheric%20Pressure&rft.jtitle=Materials&rft.au=Shoppert,%20Andrei&rft.date=2021-12-13&rft.volume=14&rft.issue=24&rft.spage=7700&rft.pages=7700-&rft.issn=1996-1944&rft.eissn=1996-1944&rft_id=info:doi/10.3390/ma14247700&rft_dat=%3Cproquest_pubme%3E2612803872%3C/proquest_pubme%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=2612803872&rft_id=info:pmid/34947303&rfr_iscdi=true