STUDI PENGGUNAAN RECYCLE NON-CONDENSABLE PRODUCT SEBAGAI FLUIDIZING GAS PADA PRODUKSI BIO-OIL MENGGUNAKAN PROSES FAST PYROLYSIS

Bio-oil can be produced from biomass with fast pyrolysis process. To facilitate fast heat transfer to quickly heat up the solid phase necessitates the use of inert fluidizing fluid. The cost of inert gas is the main factor that hinders the application of fast pyrolysis commercially. This research is...

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Main Authors: , JOHAN SYAFRI MAHATHIR AHMAD, , Ir. Moh. Fahrurrozi, M.Sc.,Ph.D
Format: Theses and Dissertations NonPeerReviewed
Published: [Yogyakarta] : Universitas Gadjah Mada 2012
Subjects:
ETD
Online Access:https://repository.ugm.ac.id/98766/
http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=54858
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spelling id-ugm-repo.987662016-03-04T08:47:14Z https://repository.ugm.ac.id/98766/ STUDI PENGGUNAAN RECYCLE NON-CONDENSABLE PRODUCT SEBAGAI FLUIDIZING GAS PADA PRODUKSI BIO-OIL MENGGUNAKAN PROSES FAST PYROLYSIS , JOHAN SYAFRI MAHATHIR AHMAD , Ir. Moh. Fahrurrozi, M.Sc.,Ph.D ETD Bio-oil can be produced from biomass with fast pyrolysis process. To facilitate fast heat transfer to quickly heat up the solid phase necessitates the use of inert fluidizing fluid. The cost of inert gas is the main factor that hinders the application of fast pyrolysis commercially. This research is directed to investigate alternative fluidizing gases which are easier and cheaper to be prepared. The objective of this research was to study influence of operating conditions in a fast pyrolysis process with re-circulated non-condensable product for producing bio-oil from various biomasses (corncob, coconut shell, teakwood sawdust and rice husk). The experiment was done in a fluidized bed reactor equipped with controlled electric heater and a non-condensable gas re-circulator. A condenser is installed to separate the bio-oil from non-condensable gas. The non-condensable gas was recirculated back to the reactor. Pyrolysis was done at temperature between 400 °C up to 500 °C and particle diameters from 0.4 mm up to 1.4 mm and fluidizing gas flowrate 2 up to 16 L/min. The experiment results show that coconut shell produce more bio oil compared to other materials (up to 77.99 % yield for coconut shell and 44.89 %, 56.69 % and 62.45 % for corncob, teak wood sawdust and rice husk respectively). The highest biooil yield was obtained at the operating temperature for coconut shel, teak wood sawdust, croncob and risk husk respectively 420, 440,500 and 460°C [Yogyakarta] : Universitas Gadjah Mada 2012 Thesis NonPeerReviewed , JOHAN SYAFRI MAHATHIR AHMAD and , Ir. Moh. Fahrurrozi, M.Sc.,Ph.D (2012) STUDI PENGGUNAAN RECYCLE NON-CONDENSABLE PRODUCT SEBAGAI FLUIDIZING GAS PADA PRODUKSI BIO-OIL MENGGUNAKAN PROSES FAST PYROLYSIS. UNSPECIFIED thesis, UNSPECIFIED. http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=54858
institution Universitas Gadjah Mada
building UGM Library
country Indonesia
collection Repository Civitas UGM
topic ETD
spellingShingle ETD
, JOHAN SYAFRI MAHATHIR AHMAD
, Ir. Moh. Fahrurrozi, M.Sc.,Ph.D
STUDI PENGGUNAAN RECYCLE NON-CONDENSABLE PRODUCT SEBAGAI FLUIDIZING GAS PADA PRODUKSI BIO-OIL MENGGUNAKAN PROSES FAST PYROLYSIS
description Bio-oil can be produced from biomass with fast pyrolysis process. To facilitate fast heat transfer to quickly heat up the solid phase necessitates the use of inert fluidizing fluid. The cost of inert gas is the main factor that hinders the application of fast pyrolysis commercially. This research is directed to investigate alternative fluidizing gases which are easier and cheaper to be prepared. The objective of this research was to study influence of operating conditions in a fast pyrolysis process with re-circulated non-condensable product for producing bio-oil from various biomasses (corncob, coconut shell, teakwood sawdust and rice husk). The experiment was done in a fluidized bed reactor equipped with controlled electric heater and a non-condensable gas re-circulator. A condenser is installed to separate the bio-oil from non-condensable gas. The non-condensable gas was recirculated back to the reactor. Pyrolysis was done at temperature between 400 °C up to 500 °C and particle diameters from 0.4 mm up to 1.4 mm and fluidizing gas flowrate 2 up to 16 L/min. The experiment results show that coconut shell produce more bio oil compared to other materials (up to 77.99 % yield for coconut shell and 44.89 %, 56.69 % and 62.45 % for corncob, teak wood sawdust and rice husk respectively). The highest biooil yield was obtained at the operating temperature for coconut shel, teak wood sawdust, croncob and risk husk respectively 420, 440,500 and 460°C
format Theses and Dissertations
NonPeerReviewed
author , JOHAN SYAFRI MAHATHIR AHMAD
, Ir. Moh. Fahrurrozi, M.Sc.,Ph.D
author_facet , JOHAN SYAFRI MAHATHIR AHMAD
, Ir. Moh. Fahrurrozi, M.Sc.,Ph.D
author_sort , JOHAN SYAFRI MAHATHIR AHMAD
title STUDI PENGGUNAAN RECYCLE NON-CONDENSABLE PRODUCT SEBAGAI FLUIDIZING GAS PADA PRODUKSI BIO-OIL MENGGUNAKAN PROSES FAST PYROLYSIS
title_short STUDI PENGGUNAAN RECYCLE NON-CONDENSABLE PRODUCT SEBAGAI FLUIDIZING GAS PADA PRODUKSI BIO-OIL MENGGUNAKAN PROSES FAST PYROLYSIS
title_full STUDI PENGGUNAAN RECYCLE NON-CONDENSABLE PRODUCT SEBAGAI FLUIDIZING GAS PADA PRODUKSI BIO-OIL MENGGUNAKAN PROSES FAST PYROLYSIS
title_fullStr STUDI PENGGUNAAN RECYCLE NON-CONDENSABLE PRODUCT SEBAGAI FLUIDIZING GAS PADA PRODUKSI BIO-OIL MENGGUNAKAN PROSES FAST PYROLYSIS
title_full_unstemmed STUDI PENGGUNAAN RECYCLE NON-CONDENSABLE PRODUCT SEBAGAI FLUIDIZING GAS PADA PRODUKSI BIO-OIL MENGGUNAKAN PROSES FAST PYROLYSIS
title_sort studi penggunaan recycle non-condensable product sebagai fluidizing gas pada produksi bio-oil menggunakan proses fast pyrolysis
publisher [Yogyakarta] : Universitas Gadjah Mada
publishDate 2012
url https://repository.ugm.ac.id/98766/
http://etd.ugm.ac.id/index.php?mod=penelitian_detail&sub=PenelitianDetail&act=view&typ=html&buku_id=54858
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