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      KCI등재 SCIE SCOPUS

      Effect of temperature and feed rate on pyrolysis oil produced via helical screw fluidized bed reactor

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      https://www.riss.kr/link?id=A107829663

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      다국어 초록 (Multilingual Abstract)

      A series of experiments was conducted to study the effect of temperature and feed rate on physicochemical properties and yield of bio-oil. The experiments were performed in a helical screw fluidized bed reactor and about 150-gram palm shell (PS) was pyrolyzed in each run at 275 oC/min heating rate. The first set of experiments was conducted at temperature ranging from 400 to 650 oC without using any inert gas for fluidization. While the second set of experiments were performed at feed rates ranging from 3 to 25 g/min in order to investigate the effects of feed rate on pyrolytic products. Results showed that the bio-oil yield was increased with the increase in temperature and feed rate due to the enhanced biomass volatilization. In a similar vein to this, a greater extent in oxygenates cracking was also noted in the bio-oil. A maximum liquid yield of about 72.84 wt% was obtained at 500 oC, while 72.92 wt% liquid yield was obtained with 25 g/min feed rate. The HHV of bio-oil was also increased from 38.52 to 43.13 MJ/kg when pyrolysis temperature was increased from 400 to 650 oC.
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      A series of experiments was conducted to study the effect of temperature and feed rate on physicochemical properties and yield of bio-oil. The experiments were performed in a helical screw fluidized bed reactor and about 150-gram palm shell (PS) was p...

      A series of experiments was conducted to study the effect of temperature and feed rate on physicochemical properties and yield of bio-oil. The experiments were performed in a helical screw fluidized bed reactor and about 150-gram palm shell (PS) was pyrolyzed in each run at 275 oC/min heating rate. The first set of experiments was conducted at temperature ranging from 400 to 650 oC without using any inert gas for fluidization. While the second set of experiments were performed at feed rates ranging from 3 to 25 g/min in order to investigate the effects of feed rate on pyrolytic products. Results showed that the bio-oil yield was increased with the increase in temperature and feed rate due to the enhanced biomass volatilization. In a similar vein to this, a greater extent in oxygenates cracking was also noted in the bio-oil. A maximum liquid yield of about 72.84 wt% was obtained at 500 oC, while 72.92 wt% liquid yield was obtained with 25 g/min feed rate. The HHV of bio-oil was also increased from 38.52 to 43.13 MJ/kg when pyrolysis temperature was increased from 400 to 650 oC.

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      참고문헌 (Reference)

      1 A. Ayala-Cortés, 140 : 290-, 2019

      2 S. -J. Kim, 101 : 9294-, 2010

      3 F. Abnisa, 76 : 1073-, 2013

      4 K. M. Qureshi, 142 : 104605-, 2019

      5 J. Akhtar, 16 : 5101-, 2012

      6 K. M. Qureshi, 131 : 52-, 2018

      7 Z. Xiong, 233 : 461-, 2018

      8 M. N. Uddin, 11 : 3115-, 2018

      9 M. I. Jahirul, 5 : 4952-, 2012

      10 K. M. Qureshi, 4 : 100174-, 2021

      1 A. Ayala-Cortés, 140 : 290-, 2019

      2 S. -J. Kim, 101 : 9294-, 2010

      3 F. Abnisa, 76 : 1073-, 2013

      4 K. M. Qureshi, 142 : 104605-, 2019

      5 J. Akhtar, 16 : 5101-, 2012

      6 K. M. Qureshi, 131 : 52-, 2018

      7 Z. Xiong, 233 : 461-, 2018

      8 M. N. Uddin, 11 : 3115-, 2018

      9 M. I. Jahirul, 5 : 4952-, 2012

      10 K. M. Qureshi, 4 : 100174-, 2021

      11 J. I. Montoya, 82 : 239-, 2015

      12 C. Quan, 2016 : 6197867-, 2016

      13 Y. Wang, 9 : 5535-, 2019

      14 T. Miranda, 8 : 1413-, 2015

      15 Y. Lu, 2017 : 1-, 2017

      16 H. Yang, 86 : 1781-, 2007

      17 U. D. Hamza, 57 : 7999-, 2016

      18 M. K. Rafiq, 11 : e0156894-, 2016

      19 T. Miranda, 8 : 1413-, 2015

      20 L. Fan, 241 : 1118-, 2017

      21 A. N. Kay Lup, 27 : 349-, 2019

      22 A. V. Bridgwater, 38 : 68-, 2012

      23 T. Kan, 57 : 1126-, 2016

      24 N. Bhattacharjee, 91 : 605-, 2018

      25 S. Mutsengerere, 104 : 328-, 2019

      26 R. Zhou, 6 : 53-, 2013

      27 R. E. Guedes, 129 : 134-, 2018

      28 Q. Xiong, 27 : 5948-, 2013

      29 K. M. Qureshi, 142 : 104605-, 2019

      30 F. Abnisa, 35 : 1863-, 2011

      31 Y. Lu, 2017 : 9298523-, 2017

      32 J. I. Montoya, 82 : 239-, 2015

      33 E. Ranzi, 22 : 4292-, 2008

      34 C. Branca, 45 : 5891-, 2006

      35 A. V. Bridgwater, 38 : 68-, 2012

      36 R. V. Powar, 3 : 519-, 2013

      37 S. W. Kim, 108 : 118-, 2013

      38 P. T. Williams, 51 : 107-, 1999

      39 S. Zhou, 27 : 1428-, 2013

      40 S. Jalalifar, 234 : 616-, 2018

      41 W. Treedet, 179 : 17-, 2018

      42 M. Bardalai, 5 : 277-, 2015

      43 M. Bertero, 116 : 409-, 2014

      44 Q. Lu, 50 : 1376-, 2009

      45 C. L. Yiin, 33 : 223-, 2014

      46 F. M. Hossain, 10 : 467-, 2017

      47 A. N. Kay Lup, 14 : e2293-, 2019

      48 S. Khan, 140 : 1-, 2019

      49 A. N. Kay Lup, 541 : 87-, 2017

      50 G. Lyu, 3 : 28-, 2015

      51 P. Fu, 88 : 117-, 2010

      52 C. Hu, 177 : 765-, 2018

      53 S. H. Chang, 119 : 263-, 2018

      54 J. O. Ogunkanmi, 12 : 711-, 2018

      55 C. Z. Zaman, "Pyrolysis" IntechOpen 2017

      56 K. Kundu, "Prospects of alternative transportation fuels" Springer 2018

      57 M. Ringer, "Large-scale pyrolysis oil production:A technology assessment and economic analysis" National Renewable Energy Lab. (NREL) 2006

      58 M. S. A. Moraes, "Frontiers in bioenergy and biofuels" IntechOpen Limited 2017

      59 Aghdas Heidari, "Effect of process conditions on product yield and composition of fast pyrolysis of Eucalyptus grandis in fluidized bed reactor" 한국공업화학회 20 (20): 2594-2602, 2014

      60 P. S. Tanvidkar, "Catalytic up-gradation of bio-oil by pyrolysis of biomass" National Institute of Technology Rourkela Odisha 2015

      61 A. N. Kay Lup, "Acidity, oxophilicity and hydrogen sticking probability of supported metal catalysts for hydrodeoxygenation process" 2017

      62 Andrew Ng Kay Lup, "A review on reactivity and stability of heterogeneous metal catalysts for deoxygenation of bio-oil model compounds" 한국공업화학회 56 : 1-34, 2017

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      학술지 이력

      학술지 이력
      연월일 이력구분 이력상세 등재구분
      2023 평가예정 해외DB학술지평가 신청대상 (해외등재 학술지 평가)
      2020-01-01 평가 등재학술지 유지 (해외등재 학술지 평가) KCI등재
      2016-06-21 학술지명변경 한글명 : The Korean Journal of Chemical Engineering -> Korean Journal of Chemical Engineering
      외국어명 : The Korean Journal of Chemical Engineering -> Korean Journal of Chemical Engineering
      KCI등재
      2011-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2009-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2007-09-27 학회명변경 영문명 : The Korean Institute Of Chemical Engineers -> The Korean Institute of Chemical Engineers KCI등재
      2007-09-03 학술지명변경 한글명 : The Korean Journal of Chemical Engineeri -> The Korean Journal of Chemical Engineering
      외국어명 : The Korean Journal of Chemical Engineeri -> The Korean Journal of Chemical Engineering
      KCI등재
      2007-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2005-01-01 평가 등재학술지 유지 (등재유지) KCI등재
      2002-01-01 평가 등재학술지 선정 (등재후보2차) KCI등재
      1999-07-01 평가 등재후보학술지 선정 (신규평가) KCI등재후보
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      학술지 인용정보

      학술지 인용정보
      기준연도 WOS-KCI 통합IF(2년) KCIF(2년) KCIF(3년)
      2016 1.92 0.72 1.4
      KCIF(4년) KCIF(5년) 중심성지수(3년) 즉시성지수
      1.15 0.94 0.403 0.14
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