Pyrolysis performance and kinetic analysis of oily sludge
In this paper, pyrolysis treatment was carried out with the tank bottom sludge of Liaohe Oilfield (LSOS) as the treatment object. Pyrolysis oil has the highest output of only 6% and the main components are gasoline and light diesel. Syngas which was the main form of energy recovery was mainly compos...
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Veröffentlicht in: | Journal of thermal analysis and calorimetry 2022-04, Vol.147 (7), p.4621-4633 |
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creator | Wang, Ziyi Gong, Zhiqiang Wang, Zhenbo Li, Xiaoyu Liu, Jixiang Tang, Chen Chu, Zhiwei |
description | In this paper, pyrolysis treatment was carried out with the tank bottom sludge of Liaohe Oilfield (LSOS) as the treatment object. Pyrolysis oil has the highest output of only 6% and the main components are gasoline and light diesel. Syngas which was the main form of energy recovery was mainly composed of CO/CO
2
, CH
4
, C
2
H
4
, etc. Temperature is the most important factor affecting energy recovery, and high-temperature environments have a positive impact on the cracking of macromolecular hydrocarbons. Increasing the temperature had a significant effect on improving the efficiency of energy recovery, which is beneficial to the recovery of energy in the form of gaseous and liquid oil. The content of organic matter in char greatly reduced, which was reflected in the significant reduction in C/H content. Part of the S/N compounds migrated and transformed, mixed into gas and liquid oil while heavy metals were enriched in char. The thermogravimetric method was carried out for the study on the pyrolysis behavior of LSOS. Starink method, KAS method and FWO method were used to calculate the kinetic parameters. The activation energy range and the average activation energy calculated by the three methods all showed high similarity, which were 61.75–237.33 kJ·mol
−1
, 52.58–205.63 kJ·mol
−1
and 59.35–207.54 kJ·mol
−1
and the average values were 122.19 kJ·mol
−1
, 106.64 kJ·mol
−1
and 112.13 kJ·mol
−1
, respectively. |
doi_str_mv | 10.1007/s10973-021-10858-4 |
format | Article |
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2
, CH
4
, C
2
H
4
, etc. Temperature is the most important factor affecting energy recovery, and high-temperature environments have a positive impact on the cracking of macromolecular hydrocarbons. Increasing the temperature had a significant effect on improving the efficiency of energy recovery, which is beneficial to the recovery of energy in the form of gaseous and liquid oil. The content of organic matter in char greatly reduced, which was reflected in the significant reduction in C/H content. Part of the S/N compounds migrated and transformed, mixed into gas and liquid oil while heavy metals were enriched in char. The thermogravimetric method was carried out for the study on the pyrolysis behavior of LSOS. Starink method, KAS method and FWO method were used to calculate the kinetic parameters. The activation energy range and the average activation energy calculated by the three methods all showed high similarity, which were 61.75–237.33 kJ·mol
−1
, 52.58–205.63 kJ·mol
−1
and 59.35–207.54 kJ·mol
−1
and the average values were 122.19 kJ·mol
−1
, 106.64 kJ·mol
−1
and 112.13 kJ·mol
−1
, respectively.</description><identifier>ISSN: 1388-6150</identifier><identifier>EISSN: 1588-2926</identifier><identifier>DOI: 10.1007/s10973-021-10858-4</identifier><language>eng</language><publisher>Cham: Springer International Publishing</publisher><subject>Activation energy ; Analysis ; Analytical Chemistry ; Chemistry ; Chemistry and Materials Science ; Energy ; Energy recovery ; Heavy metals ; High temperature environments ; Inorganic Chemistry ; Mathematical analysis ; Measurement Science and Instrumentation ; Oil field equipment ; Oil fields ; Organic matter ; Physical Chemistry ; Polymer Sciences ; Pyrolysis ; Sludge ; Synthesis gas</subject><ispartof>Journal of thermal analysis and calorimetry, 2022-04, Vol.147 (7), p.4621-4633</ispartof><rights>Akadémiai Kiadó, Budapest, Hungary 2021</rights><rights>COPYRIGHT 2022 Springer</rights><rights>Akadémiai Kiadó, Budapest, Hungary 2021.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c358t-8a6f274f2e43cba86308f846790b944f8c7644ffb1e45fbdeee0121ec7521ac33</citedby><cites>FETCH-LOGICAL-c358t-8a6f274f2e43cba86308f846790b944f8c7644ffb1e45fbdeee0121ec7521ac33</cites><orcidid>0000-0001-5795-257X</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1007/s10973-021-10858-4$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1007/s10973-021-10858-4$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>315,781,785,27929,27930,41493,42562,51324</link.rule.ids></links><search><creatorcontrib>Wang, Ziyi</creatorcontrib><creatorcontrib>Gong, Zhiqiang</creatorcontrib><creatorcontrib>Wang, Zhenbo</creatorcontrib><creatorcontrib>Li, Xiaoyu</creatorcontrib><creatorcontrib>Liu, Jixiang</creatorcontrib><creatorcontrib>Tang, Chen</creatorcontrib><creatorcontrib>Chu, Zhiwei</creatorcontrib><title>Pyrolysis performance and kinetic analysis of oily sludge</title><title>Journal of thermal analysis and calorimetry</title><addtitle>J Therm Anal Calorim</addtitle><description>In this paper, pyrolysis treatment was carried out with the tank bottom sludge of Liaohe Oilfield (LSOS) as the treatment object. Pyrolysis oil has the highest output of only 6% and the main components are gasoline and light diesel. Syngas which was the main form of energy recovery was mainly composed of CO/CO
2
, CH
4
, C
2
H
4
, etc. Temperature is the most important factor affecting energy recovery, and high-temperature environments have a positive impact on the cracking of macromolecular hydrocarbons. Increasing the temperature had a significant effect on improving the efficiency of energy recovery, which is beneficial to the recovery of energy in the form of gaseous and liquid oil. The content of organic matter in char greatly reduced, which was reflected in the significant reduction in C/H content. Part of the S/N compounds migrated and transformed, mixed into gas and liquid oil while heavy metals were enriched in char. The thermogravimetric method was carried out for the study on the pyrolysis behavior of LSOS. Starink method, KAS method and FWO method were used to calculate the kinetic parameters. The activation energy range and the average activation energy calculated by the three methods all showed high similarity, which were 61.75–237.33 kJ·mol
−1
, 52.58–205.63 kJ·mol
−1
and 59.35–207.54 kJ·mol
−1
and the average values were 122.19 kJ·mol
−1
, 106.64 kJ·mol
−1
and 112.13 kJ·mol
−1
, respectively.</description><subject>Activation energy</subject><subject>Analysis</subject><subject>Analytical Chemistry</subject><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><subject>Energy</subject><subject>Energy recovery</subject><subject>Heavy metals</subject><subject>High temperature environments</subject><subject>Inorganic Chemistry</subject><subject>Mathematical analysis</subject><subject>Measurement Science and Instrumentation</subject><subject>Oil field equipment</subject><subject>Oil fields</subject><subject>Organic matter</subject><subject>Physical Chemistry</subject><subject>Polymer Sciences</subject><subject>Pyrolysis</subject><subject>Sludge</subject><subject>Synthesis gas</subject><issn>1388-6150</issn><issn>1588-2926</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2022</creationdate><recordtype>article</recordtype><recordid>eNp9UE1LAzEUDKJgrf4BTwuet-Z7k2MpfkFBD3oO2fSlpG43Ndke9t-buoI3eYcZHjPzHoPQLcELgnFznwnWDasxJTXBSqian6EZEUrVVFN5XjgrXBKBL9FVzjuMsdaYzJB-G1PsxhxydYDkY9rb3kFl-031GXoYgivcToLoqxi6scrdcbOFa3ThbZfh5hfn6OPx4X31XK9fn15Wy3XtmFBDraz0tOGeAmeutUoyrLzistG41Zx75RpZwLcEuPDtBgAwoQRcIyixjrE5uptyDyl-HSEPZhePqfyUDZWMi5IleFEtJtXWdmBC7-OQrCuzgX1wsQcfyn4ptWC0kewUSyeDSzHnBN4cUtjbNBqCzalTM3VqSqfmp1NzusImUy7ifgvp75d_XN9ExXjr</recordid><startdate>20220401</startdate><enddate>20220401</enddate><creator>Wang, Ziyi</creator><creator>Gong, Zhiqiang</creator><creator>Wang, Zhenbo</creator><creator>Li, Xiaoyu</creator><creator>Liu, Jixiang</creator><creator>Tang, Chen</creator><creator>Chu, Zhiwei</creator><general>Springer International Publishing</general><general>Springer</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope><orcidid>https://orcid.org/0000-0001-5795-257X</orcidid></search><sort><creationdate>20220401</creationdate><title>Pyrolysis performance and kinetic analysis of oily sludge</title><author>Wang, Ziyi ; Gong, Zhiqiang ; Wang, Zhenbo ; Li, Xiaoyu ; Liu, Jixiang ; Tang, Chen ; Chu, Zhiwei</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c358t-8a6f274f2e43cba86308f846790b944f8c7644ffb1e45fbdeee0121ec7521ac33</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2022</creationdate><topic>Activation energy</topic><topic>Analysis</topic><topic>Analytical Chemistry</topic><topic>Chemistry</topic><topic>Chemistry and Materials Science</topic><topic>Energy</topic><topic>Energy recovery</topic><topic>Heavy metals</topic><topic>High temperature environments</topic><topic>Inorganic Chemistry</topic><topic>Mathematical analysis</topic><topic>Measurement Science and Instrumentation</topic><topic>Oil field equipment</topic><topic>Oil fields</topic><topic>Organic matter</topic><topic>Physical Chemistry</topic><topic>Polymer Sciences</topic><topic>Pyrolysis</topic><topic>Sludge</topic><topic>Synthesis gas</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Wang, Ziyi</creatorcontrib><creatorcontrib>Gong, Zhiqiang</creatorcontrib><creatorcontrib>Wang, Zhenbo</creatorcontrib><creatorcontrib>Li, Xiaoyu</creatorcontrib><creatorcontrib>Liu, Jixiang</creatorcontrib><creatorcontrib>Tang, Chen</creatorcontrib><creatorcontrib>Chu, Zhiwei</creatorcontrib><collection>CrossRef</collection><jtitle>Journal of thermal analysis and calorimetry</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Wang, Ziyi</au><au>Gong, Zhiqiang</au><au>Wang, Zhenbo</au><au>Li, Xiaoyu</au><au>Liu, Jixiang</au><au>Tang, Chen</au><au>Chu, Zhiwei</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Pyrolysis performance and kinetic analysis of oily sludge</atitle><jtitle>Journal of thermal analysis and calorimetry</jtitle><stitle>J Therm Anal Calorim</stitle><date>2022-04-01</date><risdate>2022</risdate><volume>147</volume><issue>7</issue><spage>4621</spage><epage>4633</epage><pages>4621-4633</pages><issn>1388-6150</issn><eissn>1588-2926</eissn><abstract>In this paper, pyrolysis treatment was carried out with the tank bottom sludge of Liaohe Oilfield (LSOS) as the treatment object. Pyrolysis oil has the highest output of only 6% and the main components are gasoline and light diesel. Syngas which was the main form of energy recovery was mainly composed of CO/CO
2
, CH
4
, C
2
H
4
, etc. Temperature is the most important factor affecting energy recovery, and high-temperature environments have a positive impact on the cracking of macromolecular hydrocarbons. Increasing the temperature had a significant effect on improving the efficiency of energy recovery, which is beneficial to the recovery of energy in the form of gaseous and liquid oil. The content of organic matter in char greatly reduced, which was reflected in the significant reduction in C/H content. Part of the S/N compounds migrated and transformed, mixed into gas and liquid oil while heavy metals were enriched in char. The thermogravimetric method was carried out for the study on the pyrolysis behavior of LSOS. Starink method, KAS method and FWO method were used to calculate the kinetic parameters. The activation energy range and the average activation energy calculated by the three methods all showed high similarity, which were 61.75–237.33 kJ·mol
−1
, 52.58–205.63 kJ·mol
−1
and 59.35–207.54 kJ·mol
−1
and the average values were 122.19 kJ·mol
−1
, 106.64 kJ·mol
−1
and 112.13 kJ·mol
−1
, respectively.</abstract><cop>Cham</cop><pub>Springer International Publishing</pub><doi>10.1007/s10973-021-10858-4</doi><tpages>13</tpages><orcidid>https://orcid.org/0000-0001-5795-257X</orcidid></addata></record> |
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source | SpringerNature Journals |
subjects | Activation energy Analysis Analytical Chemistry Chemistry Chemistry and Materials Science Energy Energy recovery Heavy metals High temperature environments Inorganic Chemistry Mathematical analysis Measurement Science and Instrumentation Oil field equipment Oil fields Organic matter Physical Chemistry Polymer Sciences Pyrolysis Sludge Synthesis gas |
title | Pyrolysis performance and kinetic analysis of oily sludge |
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