High Solids Hydroxy‐TEMPO Mediated Radical Semibatch Emulsion Polymerization of Styrene
Stable polystyrene latexes having controlled molecular weight distribution (MWD) with solids contents up to 40 wt% are obtained using potassium persulfate as initiator with the nitroxides 4‐hydroxy‐2,2,6,6‐tetramethylpiperidine‐N‐oxyl (hydroxy‐TEMPO) and 4‐amino‐2,2,6,6‐tetramethylpiperidine‐N‐oxyl...
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Veröffentlicht in: | Macromolecular reaction engineering 2021-04, Vol.15 (2), p.n/a |
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description | Stable polystyrene latexes having controlled molecular weight distribution (MWD) with solids contents up to 40 wt% are obtained using potassium persulfate as initiator with the nitroxides 4‐hydroxy‐2,2,6,6‐tetramethylpiperidine‐N‐oxyl (hydroxy‐TEMPO) and 4‐amino‐2,2,6,6‐tetramethylpiperidine‐N‐oxyl (amino‐TEMPO). Using different concentrations of styrene (St) in the nucleation step, it is possible to create colloidal dispersions with particle size ranging from ≈57 to ≈390 nm, conversions up to ≈96%, nitroxide efficiencies (NEff) up to ≈0.76, and number average molecular weight (Mn) ranging from ≈10 000 to ≈85 000 g mol−1. The effect of the monomer feed rate in the semibatch step is also studied. These polymerizations do not require a separate macroinitiator synthesis, since this is formed in situ during the heating ramp. A mathematical model is used to compare the mechanistic understanding of the system with the experimental results.
A process for producing stable polystyrene latexes via a high‐solids (40 wt%) ab initio semicontinuous emulsion polymerization controlled with 4‐hydroxy‐2,2,6,6‐tetramethylpiperidine‐N‐oxyl, suited for industrial scale‐up, is reported. Monomer conversions up to 96% (5–12 h) and average molecular weights of 10 000–85 000 g mol−1 are achievable. A mathematical model of the process is used to analyze the experimental results. |
doi_str_mv | 10.1002/mren.202000054 |
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A process for producing stable polystyrene latexes via a high‐solids (40 wt%) ab initio semicontinuous emulsion polymerization controlled with 4‐hydroxy‐2,2,6,6‐tetramethylpiperidine‐N‐oxyl, suited for industrial scale‐up, is reported. Monomer conversions up to 96% (5–12 h) and average molecular weights of 10 000–85 000 g mol−1 are achievable. A mathematical model of the process is used to analyze the experimental results.</description><identifier>ISSN: 1862-832X</identifier><identifier>EISSN: 1862-8338</identifier><identifier>DOI: 10.1002/mren.202000054</identifier><language>eng</language><publisher>Weinheim: Wiley Subscription Services, Inc</publisher><subject>alkoxyamines ; controlled radical polymerization ; Dispersions ; Emulsion polymerization ; emulsions ; Feed rate ; Molecular weight ; Molecular weight distribution ; nitroxide ; Nucleation ; Polystyrene resins ; Potassium persulfate ; Styrenes</subject><ispartof>Macromolecular reaction engineering, 2021-04, Vol.15 (2), p.n/a</ispartof><rights>2020 Wiley‐VCH GmbH</rights><rights>2021 Wiley‐VCH GmbH</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c3544-b9366fde1a670f4e99d28136b6060f5bf8574f1959dc722778b2d04cdbb7b74a3</citedby><cites>FETCH-LOGICAL-c3544-b9366fde1a670f4e99d28136b6060f5bf8574f1959dc722778b2d04cdbb7b74a3</cites><orcidid>0000-0001-9623-575X</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Fmren.202000054$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Fmren.202000054$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,776,780,1411,27901,27902,45550,45551</link.rule.ids></links><search><creatorcontrib>González‐Blanco, Roberto</creatorcontrib><creatorcontrib>Jiménez‐Reyes, Nelson</creatorcontrib><creatorcontrib>Cunningham, Michael F.</creatorcontrib><creatorcontrib>Saldívar‐Guerra, Enrique</creatorcontrib><title>High Solids Hydroxy‐TEMPO Mediated Radical Semibatch Emulsion Polymerization of Styrene</title><title>Macromolecular reaction engineering</title><description>Stable polystyrene latexes having controlled molecular weight distribution (MWD) with solids contents up to 40 wt% are obtained using potassium persulfate as initiator with the nitroxides 4‐hydroxy‐2,2,6,6‐tetramethylpiperidine‐N‐oxyl (hydroxy‐TEMPO) and 4‐amino‐2,2,6,6‐tetramethylpiperidine‐N‐oxyl (amino‐TEMPO). Using different concentrations of styrene (St) in the nucleation step, it is possible to create colloidal dispersions with particle size ranging from ≈57 to ≈390 nm, conversions up to ≈96%, nitroxide efficiencies (NEff) up to ≈0.76, and number average molecular weight (Mn) ranging from ≈10 000 to ≈85 000 g mol−1. The effect of the monomer feed rate in the semibatch step is also studied. These polymerizations do not require a separate macroinitiator synthesis, since this is formed in situ during the heating ramp. A mathematical model is used to compare the mechanistic understanding of the system with the experimental results.
A process for producing stable polystyrene latexes via a high‐solids (40 wt%) ab initio semicontinuous emulsion polymerization controlled with 4‐hydroxy‐2,2,6,6‐tetramethylpiperidine‐N‐oxyl, suited for industrial scale‐up, is reported. Monomer conversions up to 96% (5–12 h) and average molecular weights of 10 000–85 000 g mol−1 are achievable. A mathematical model of the process is used to analyze the experimental results.</description><subject>alkoxyamines</subject><subject>controlled radical polymerization</subject><subject>Dispersions</subject><subject>Emulsion polymerization</subject><subject>emulsions</subject><subject>Feed rate</subject><subject>Molecular weight</subject><subject>Molecular weight distribution</subject><subject>nitroxide</subject><subject>Nucleation</subject><subject>Polystyrene resins</subject><subject>Potassium persulfate</subject><subject>Styrenes</subject><issn>1862-832X</issn><issn>1862-8338</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><recordid>eNqFkM9KAzEQxoMoWKtXzwHPW5Ns9k-OUqoVWlvaCnoKySaxKbtNTbboevIRfEafxC2VevS7zAz8vpnhA-ASox5GiFxXXq97BBHUKqFHoIPzlER5HOfHh548nYKzEFYt0Yp1wPPQvizh3JVWBThslHfvzffn12Iwnk7gWCsraq3gTChbiBLOdWWlqIslHFTbMli3hlNXNpX29kPUu9EZOK-b9hN9Dk6MKIO--K1d8Hg7WPSH0Whyd9-_GUVFnFAaSRanqVEaizRDhmrGFMlxnMoUpcgk0uRJRg1mCVNFRkiW5ZIoRAslZSYzKuIuuNrv3Xj3utWh5iu39ev2JCcJpiyniMQt1dtThXcheG34xttK-IZjxHfx8V18_BBfa2B7w5stdfMPzcezwcOf9wcW9XTn</recordid><startdate>202104</startdate><enddate>202104</enddate><creator>González‐Blanco, Roberto</creator><creator>Jiménez‐Reyes, Nelson</creator><creator>Cunningham, Michael F.</creator><creator>Saldívar‐Guerra, Enrique</creator><general>Wiley Subscription Services, Inc</general><scope>AAYXX</scope><scope>CITATION</scope><orcidid>https://orcid.org/0000-0001-9623-575X</orcidid></search><sort><creationdate>202104</creationdate><title>High Solids Hydroxy‐TEMPO Mediated Radical Semibatch Emulsion Polymerization of Styrene</title><author>González‐Blanco, Roberto ; Jiménez‐Reyes, Nelson ; Cunningham, Michael F. ; Saldívar‐Guerra, Enrique</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c3544-b9366fde1a670f4e99d28136b6060f5bf8574f1959dc722778b2d04cdbb7b74a3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2021</creationdate><topic>alkoxyamines</topic><topic>controlled radical polymerization</topic><topic>Dispersions</topic><topic>Emulsion polymerization</topic><topic>emulsions</topic><topic>Feed rate</topic><topic>Molecular weight</topic><topic>Molecular weight distribution</topic><topic>nitroxide</topic><topic>Nucleation</topic><topic>Polystyrene resins</topic><topic>Potassium persulfate</topic><topic>Styrenes</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>González‐Blanco, Roberto</creatorcontrib><creatorcontrib>Jiménez‐Reyes, Nelson</creatorcontrib><creatorcontrib>Cunningham, Michael F.</creatorcontrib><creatorcontrib>Saldívar‐Guerra, Enrique</creatorcontrib><collection>CrossRef</collection><jtitle>Macromolecular reaction engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>González‐Blanco, Roberto</au><au>Jiménez‐Reyes, Nelson</au><au>Cunningham, Michael F.</au><au>Saldívar‐Guerra, Enrique</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>High Solids Hydroxy‐TEMPO Mediated Radical Semibatch Emulsion Polymerization of Styrene</atitle><jtitle>Macromolecular reaction engineering</jtitle><date>2021-04</date><risdate>2021</risdate><volume>15</volume><issue>2</issue><epage>n/a</epage><issn>1862-832X</issn><eissn>1862-8338</eissn><abstract>Stable polystyrene latexes having controlled molecular weight distribution (MWD) with solids contents up to 40 wt% are obtained using potassium persulfate as initiator with the nitroxides 4‐hydroxy‐2,2,6,6‐tetramethylpiperidine‐N‐oxyl (hydroxy‐TEMPO) and 4‐amino‐2,2,6,6‐tetramethylpiperidine‐N‐oxyl (amino‐TEMPO). Using different concentrations of styrene (St) in the nucleation step, it is possible to create colloidal dispersions with particle size ranging from ≈57 to ≈390 nm, conversions up to ≈96%, nitroxide efficiencies (NEff) up to ≈0.76, and number average molecular weight (Mn) ranging from ≈10 000 to ≈85 000 g mol−1. The effect of the monomer feed rate in the semibatch step is also studied. These polymerizations do not require a separate macroinitiator synthesis, since this is formed in situ during the heating ramp. A mathematical model is used to compare the mechanistic understanding of the system with the experimental results.
A process for producing stable polystyrene latexes via a high‐solids (40 wt%) ab initio semicontinuous emulsion polymerization controlled with 4‐hydroxy‐2,2,6,6‐tetramethylpiperidine‐N‐oxyl, suited for industrial scale‐up, is reported. Monomer conversions up to 96% (5–12 h) and average molecular weights of 10 000–85 000 g mol−1 are achievable. A mathematical model of the process is used to analyze the experimental results.</abstract><cop>Weinheim</cop><pub>Wiley Subscription Services, Inc</pub><doi>10.1002/mren.202000054</doi><tpages>9</tpages><orcidid>https://orcid.org/0000-0001-9623-575X</orcidid></addata></record> |
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subjects | alkoxyamines controlled radical polymerization Dispersions Emulsion polymerization emulsions Feed rate Molecular weight Molecular weight distribution nitroxide Nucleation Polystyrene resins Potassium persulfate Styrenes |
title | High Solids Hydroxy‐TEMPO Mediated Radical Semibatch Emulsion Polymerization of Styrene |
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