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
Hauptverfasser: Wang, Ziyi, Gong, Zhiqiang, Wang, Zhenbo, Li, Xiaoyu, Liu, Jixiang, Tang, Chen, Chu, Zhiwei
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container_issue 7
container_start_page 4621
container_title Journal of thermal analysis and calorimetry
container_volume 147
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
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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. 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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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