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Depolymerization of poly(butylene terephthalate) in sub- and supercritical ethanol in a fused silica capillary reactor or autoclave reactor
Depolymerization of poly(butylene terephthalate) (PBT) in sub- and supercritical ethanol was performed both in a fused silica capillary reactor (FSCR) or a batch autoclave reactor. The phase behavior of PBT in ethanol during heating and cooling was studied in the FSCR under a microscope and captured...
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Published in: | Polymer degradation and stability 2013-07, Vol.98 (7), p.1287-1292 |
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container_title | Polymer degradation and stability |
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creator | Pan, Zhiyan Shi, Yinghai Liu, Li Jin, Zanfang |
description | Depolymerization of poly(butylene terephthalate) (PBT) in sub- and supercritical ethanol was performed both in a fused silica capillary reactor (FSCR) or a batch autoclave reactor. The phase behavior of PBT in ethanol during heating and cooling was studied in the FSCR under a microscope and captured by a digital camera. The results showed that PBT could dissolve in supercritical ethanol at 330 °C and form a homogeneous solution. Under autogenous pressure in the batch autoclave reactor, the effects of the ethanol/PBT mass ratio (8 g/2 g to 24 g/2 g), reaction temperature (200–280 °C) and reaction time (5–60 min) on depolymerization of PBT in sub- and supercritical ethanol were investigated. The main liquid products of depolymerization were identified and quantified as diethyl terephthalate (DET) and 1,4-butanediol (1,4-BD) by liquid chromatography mass spectrometry, gas chromatography mass spectrometry, and gas chromatography, respectively. PBT could be completely depolymerized at 240 °C in 60 min with an optimal ethanol/PBT mass ratio of 20 g/2 g (10:1). The highest yields of DET and 1,4-BD were 97.7% and 89.4%, respectively. Reaction kinetics analysis showed that the PBT depolymerization in sub-critical ethanol reaction was first order and activation energy was 38.8 kJ mol−1. A reaction pathway was proposed based on the experimental results. |
doi_str_mv | 10.1016/j.polymdegradstab.2013.04.004 |
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The phase behavior of PBT in ethanol during heating and cooling was studied in the FSCR under a microscope and captured by a digital camera. The results showed that PBT could dissolve in supercritical ethanol at 330 °C and form a homogeneous solution. Under autogenous pressure in the batch autoclave reactor, the effects of the ethanol/PBT mass ratio (8 g/2 g to 24 g/2 g), reaction temperature (200–280 °C) and reaction time (5–60 min) on depolymerization of PBT in sub- and supercritical ethanol were investigated. The main liquid products of depolymerization were identified and quantified as diethyl terephthalate (DET) and 1,4-butanediol (1,4-BD) by liquid chromatography mass spectrometry, gas chromatography mass spectrometry, and gas chromatography, respectively. PBT could be completely depolymerized at 240 °C in 60 min with an optimal ethanol/PBT mass ratio of 20 g/2 g (10:1). The highest yields of DET and 1,4-BD were 97.7% and 89.4%, respectively. Reaction kinetics analysis showed that the PBT depolymerization in sub-critical ethanol reaction was first order and activation energy was 38.8 kJ mol−1. A reaction pathway was proposed based on the experimental results.</description><identifier>ISSN: 0141-3910</identifier><identifier>EISSN: 1873-2321</identifier><identifier>DOI: 10.1016/j.polymdegradstab.2013.04.004</identifier><identifier>CODEN: PDSTDW</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>activation energy ; Applied sciences ; Autoclaves ; cooling ; Depolymerization ; Ethanol ; Ethyl alcohol ; Exact sciences and technology ; gas chromatography-mass spectrometry ; heat ; liquid chromatography ; Mass spectrometry ; Phase behavior ; Poly(butylene terephthalate) ; Polybutylene terephthalates ; Polymer industry, paints, wood ; reaction kinetics ; Reactors ; silica ; Supercritical ethanol ; Technology of polymers ; temperature ; Terephthalate ; Waste treatment ; yields</subject><ispartof>Polymer degradation and stability, 2013-07, Vol.98 (7), p.1287-1292</ispartof><rights>2013 Elsevier Ltd</rights><rights>2014 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c523t-4ed962c158bf463e397af8d27f42ad77bb276574eaa3800b73469438fc0b35f53</citedby><cites>FETCH-LOGICAL-c523t-4ed962c158bf463e397af8d27f42ad77bb276574eaa3800b73469438fc0b35f53</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=27393989$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Pan, Zhiyan</creatorcontrib><creatorcontrib>Shi, Yinghai</creatorcontrib><creatorcontrib>Liu, Li</creatorcontrib><creatorcontrib>Jin, Zanfang</creatorcontrib><title>Depolymerization of poly(butylene terephthalate) in sub- and supercritical ethanol in a fused silica capillary reactor or autoclave reactor</title><title>Polymer degradation and stability</title><description>Depolymerization of poly(butylene terephthalate) (PBT) in sub- and supercritical ethanol was performed both in a fused silica capillary reactor (FSCR) or a batch autoclave reactor. The phase behavior of PBT in ethanol during heating and cooling was studied in the FSCR under a microscope and captured by a digital camera. The results showed that PBT could dissolve in supercritical ethanol at 330 °C and form a homogeneous solution. Under autogenous pressure in the batch autoclave reactor, the effects of the ethanol/PBT mass ratio (8 g/2 g to 24 g/2 g), reaction temperature (200–280 °C) and reaction time (5–60 min) on depolymerization of PBT in sub- and supercritical ethanol were investigated. The main liquid products of depolymerization were identified and quantified as diethyl terephthalate (DET) and 1,4-butanediol (1,4-BD) by liquid chromatography mass spectrometry, gas chromatography mass spectrometry, and gas chromatography, respectively. PBT could be completely depolymerized at 240 °C in 60 min with an optimal ethanol/PBT mass ratio of 20 g/2 g (10:1). The highest yields of DET and 1,4-BD were 97.7% and 89.4%, respectively. Reaction kinetics analysis showed that the PBT depolymerization in sub-critical ethanol reaction was first order and activation energy was 38.8 kJ mol−1. A reaction pathway was proposed based on the experimental results.</description><subject>activation energy</subject><subject>Applied sciences</subject><subject>Autoclaves</subject><subject>cooling</subject><subject>Depolymerization</subject><subject>Ethanol</subject><subject>Ethyl alcohol</subject><subject>Exact sciences and technology</subject><subject>gas chromatography-mass spectrometry</subject><subject>heat</subject><subject>liquid chromatography</subject><subject>Mass spectrometry</subject><subject>Phase behavior</subject><subject>Poly(butylene terephthalate)</subject><subject>Polybutylene terephthalates</subject><subject>Polymer industry, paints, wood</subject><subject>reaction kinetics</subject><subject>Reactors</subject><subject>silica</subject><subject>Supercritical ethanol</subject><subject>Technology of polymers</subject><subject>temperature</subject><subject>Terephthalate</subject><subject>Waste treatment</subject><subject>yields</subject><issn>0141-3910</issn><issn>1873-2321</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2013</creationdate><recordtype>article</recordtype><recordid>eNqNkc1u1DAUhSNEJYaWZ8CbSmWR4L_EyYIFaqEgVeqidG3dONetR5442E6l4RV4aTxMYcEKy5Kt68_H1-dU1TmjDaOse79tluD3uwkfIkwpw9hwykRDZUOpfFFtWK9EzQVnL6sNZZLVYmD0VfU6pS0tQ7ZsU_28wt8iGN0PyC7MJFhyqFyMa957nJFkjLg85kfwkPEdcTNJ61gTmKeyWTCa6LIz4AkWZg7-QACxa8ICOF-OiIHFeQ9xTyKCySGSMmHNwXh4wj_Fs-rEgk_45nk9re4_f_p2-aW-ub3-evnxpjYtF7mWOA0dN6ztRys7gWJQYPuJKys5TEqNI1ddqyQCiJ7SUQnZDVL01tBRtLYVp9XFUXeJ4fuKKeudSwZLgzOGNWkmFO9E3wtV0A9H1MSQUkSrl-h25SOaUX0IQW_1PyHoQwiaSl0cLvfPn5-CVCyyEWbj0l8RrsQghn4o3NsjZyFoeIiFub8rQl3JSYlW9IW4PhJYnHlyGHUyDmeDk4tosp6C-8-efgE5jLMs</recordid><startdate>20130701</startdate><enddate>20130701</enddate><creator>Pan, Zhiyan</creator><creator>Shi, Yinghai</creator><creator>Liu, Li</creator><creator>Jin, Zanfang</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>FBQ</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>8FD</scope><scope>JG9</scope></search><sort><creationdate>20130701</creationdate><title>Depolymerization of poly(butylene terephthalate) in sub- and supercritical ethanol in a fused silica capillary reactor or autoclave reactor</title><author>Pan, Zhiyan ; Shi, Yinghai ; Liu, Li ; Jin, Zanfang</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c523t-4ed962c158bf463e397af8d27f42ad77bb276574eaa3800b73469438fc0b35f53</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2013</creationdate><topic>activation energy</topic><topic>Applied sciences</topic><topic>Autoclaves</topic><topic>cooling</topic><topic>Depolymerization</topic><topic>Ethanol</topic><topic>Ethyl alcohol</topic><topic>Exact sciences and technology</topic><topic>gas chromatography-mass spectrometry</topic><topic>heat</topic><topic>liquid chromatography</topic><topic>Mass spectrometry</topic><topic>Phase behavior</topic><topic>Poly(butylene terephthalate)</topic><topic>Polybutylene terephthalates</topic><topic>Polymer industry, paints, wood</topic><topic>reaction kinetics</topic><topic>Reactors</topic><topic>silica</topic><topic>Supercritical ethanol</topic><topic>Technology of polymers</topic><topic>temperature</topic><topic>Terephthalate</topic><topic>Waste treatment</topic><topic>yields</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Pan, Zhiyan</creatorcontrib><creatorcontrib>Shi, Yinghai</creatorcontrib><creatorcontrib>Liu, Li</creatorcontrib><creatorcontrib>Jin, Zanfang</creatorcontrib><collection>AGRIS</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><jtitle>Polymer degradation and stability</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Pan, Zhiyan</au><au>Shi, Yinghai</au><au>Liu, Li</au><au>Jin, Zanfang</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Depolymerization of poly(butylene terephthalate) in sub- and supercritical ethanol in a fused silica capillary reactor or autoclave reactor</atitle><jtitle>Polymer degradation and stability</jtitle><date>2013-07-01</date><risdate>2013</risdate><volume>98</volume><issue>7</issue><spage>1287</spage><epage>1292</epage><pages>1287-1292</pages><issn>0141-3910</issn><eissn>1873-2321</eissn><coden>PDSTDW</coden><abstract>Depolymerization of poly(butylene terephthalate) (PBT) in sub- and supercritical ethanol was performed both in a fused silica capillary reactor (FSCR) or a batch autoclave reactor. The phase behavior of PBT in ethanol during heating and cooling was studied in the FSCR under a microscope and captured by a digital camera. The results showed that PBT could dissolve in supercritical ethanol at 330 °C and form a homogeneous solution. Under autogenous pressure in the batch autoclave reactor, the effects of the ethanol/PBT mass ratio (8 g/2 g to 24 g/2 g), reaction temperature (200–280 °C) and reaction time (5–60 min) on depolymerization of PBT in sub- and supercritical ethanol were investigated. The main liquid products of depolymerization were identified and quantified as diethyl terephthalate (DET) and 1,4-butanediol (1,4-BD) by liquid chromatography mass spectrometry, gas chromatography mass spectrometry, and gas chromatography, respectively. PBT could be completely depolymerized at 240 °C in 60 min with an optimal ethanol/PBT mass ratio of 20 g/2 g (10:1). The highest yields of DET and 1,4-BD were 97.7% and 89.4%, respectively. Reaction kinetics analysis showed that the PBT depolymerization in sub-critical ethanol reaction was first order and activation energy was 38.8 kJ mol−1. A reaction pathway was proposed based on the experimental results.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.polymdegradstab.2013.04.004</doi><tpages>6</tpages></addata></record> |
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subjects | activation energy Applied sciences Autoclaves cooling Depolymerization Ethanol Ethyl alcohol Exact sciences and technology gas chromatography-mass spectrometry heat liquid chromatography Mass spectrometry Phase behavior Poly(butylene terephthalate) Polybutylene terephthalates Polymer industry, paints, wood reaction kinetics Reactors silica Supercritical ethanol Technology of polymers temperature Terephthalate Waste treatment yields |
title | Depolymerization of poly(butylene terephthalate) in sub- and supercritical ethanol in a fused silica capillary reactor or autoclave reactor |
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