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The separation of phenolic compounds from bio-oil produced from pyrolysis of corncobs
Corncob is an agricultural waste which has a potential to be utilized as a raw material for bio-oil. One of many processes to convert the agricultural waste (biomass) into bio-oil is pyrolysis. The pyrolysis process for this study was carried out using fixed bed pyrolysis reactor, performed under te...
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creator | Fardhyanti, D. S. Imani, N. A. C. Damayanti, A. Mardhotillah, S. N. Afifudin, M. Mulyaningtyas, A. Akhir, A. E. Nuramalia, W. Maulana, P. |
description | Corncob is an agricultural waste which has a potential to be utilized as a raw material for bio-oil. One of many processes to convert the agricultural waste (biomass) into bio-oil is pyrolysis. The pyrolysis process for this study was carried out using fixed bed pyrolysis reactor, performed under temperature of 500°C and 600°C with residence time of 4 seconds. The bio-oil was analyzed for its components content using Gas Chromatography-Mass Spectrometry (GCMS). The separation of phenolic compounds from bio-oil was done by a liquid-liquid extraction which carried out for 60 minutes using methanol 80% and chloroform as solvent at various extraction temperatures of 30°C, 40°C, 50°C, and stirring speeds of 200 rpm, 250 rpm, 300 rpm. Then, the extract phase and the raffinate phase were analyzed using Folin-Ciocalteu method. The aim of this study was to determine the effect of temperatures and stirring speeds of the liquid-liquid extraction to the distribution coefficient and the yield of phenolic compound. The result showed that the main component of bio-oil obtained is phenolic compounds. The highest distribution coefficient and the highest yield of phenolic compound were obtained at 50°C and 300 rpm. The highest yield was 66.31% and 58.9% obtained from pyrolysis process at 500°C and 600°C, respectively. Meanwhile, the highest distribution coefficient was 11.08 and 8.92 for pyrolysis at 500°C and 600°C. |
doi_str_mv | 10.1063/5.0001078 |
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S. ; Imani, N. A. C. ; Damayanti, A. ; Mardhotillah, S. N. ; Afifudin, M. ; Mulyaningtyas, A. ; Akhir, A. E. ; Nuramalia, W. ; Maulana, P.</creator><contributor>Rafi, Mohamad ; Wahyuni, Wulan Tri ; Heryanto, Rudi</contributor><creatorcontrib>Fardhyanti, D. S. ; Imani, N. A. C. ; Damayanti, A. ; Mardhotillah, S. N. ; Afifudin, M. ; Mulyaningtyas, A. ; Akhir, A. E. ; Nuramalia, W. ; Maulana, P. ; Rafi, Mohamad ; Wahyuni, Wulan Tri ; Heryanto, Rudi</creatorcontrib><description>Corncob is an agricultural waste which has a potential to be utilized as a raw material for bio-oil. One of many processes to convert the agricultural waste (biomass) into bio-oil is pyrolysis. The pyrolysis process for this study was carried out using fixed bed pyrolysis reactor, performed under temperature of 500°C and 600°C with residence time of 4 seconds. The bio-oil was analyzed for its components content using Gas Chromatography-Mass Spectrometry (GCMS). The separation of phenolic compounds from bio-oil was done by a liquid-liquid extraction which carried out for 60 minutes using methanol 80% and chloroform as solvent at various extraction temperatures of 30°C, 40°C, 50°C, and stirring speeds of 200 rpm, 250 rpm, 300 rpm. Then, the extract phase and the raffinate phase were analyzed using Folin-Ciocalteu method. The aim of this study was to determine the effect of temperatures and stirring speeds of the liquid-liquid extraction to the distribution coefficient and the yield of phenolic compound. The result showed that the main component of bio-oil obtained is phenolic compounds. The highest distribution coefficient and the highest yield of phenolic compound were obtained at 50°C and 300 rpm. The highest yield was 66.31% and 58.9% obtained from pyrolysis process at 500°C and 600°C, respectively. 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E.</creatorcontrib><creatorcontrib>Nuramalia, W.</creatorcontrib><creatorcontrib>Maulana, P.</creatorcontrib><title>The separation of phenolic compounds from bio-oil produced from pyrolysis of corncobs</title><title>AIP conference proceedings</title><description>Corncob is an agricultural waste which has a potential to be utilized as a raw material for bio-oil. One of many processes to convert the agricultural waste (biomass) into bio-oil is pyrolysis. The pyrolysis process for this study was carried out using fixed bed pyrolysis reactor, performed under temperature of 500°C and 600°C with residence time of 4 seconds. The bio-oil was analyzed for its components content using Gas Chromatography-Mass Spectrometry (GCMS). The separation of phenolic compounds from bio-oil was done by a liquid-liquid extraction which carried out for 60 minutes using methanol 80% and chloroform as solvent at various extraction temperatures of 30°C, 40°C, 50°C, and stirring speeds of 200 rpm, 250 rpm, 300 rpm. Then, the extract phase and the raffinate phase were analyzed using Folin-Ciocalteu method. The aim of this study was to determine the effect of temperatures and stirring speeds of the liquid-liquid extraction to the distribution coefficient and the yield of phenolic compound. The result showed that the main component of bio-oil obtained is phenolic compounds. The highest distribution coefficient and the highest yield of phenolic compound were obtained at 50°C and 300 rpm. The highest yield was 66.31% and 58.9% obtained from pyrolysis process at 500°C and 600°C, respectively. Meanwhile, the highest distribution coefficient was 11.08 and 8.92 for pyrolysis at 500°C and 600°C.</description><subject>Agricultural production</subject><subject>Agricultural wastes</subject><subject>Chloroform</subject><subject>Coefficients</subject><subject>Fixed beds</subject><subject>Gas chromatography</subject><subject>Liquid-liquid extraction</subject><subject>Mass spectrometry</subject><subject>Phenols</subject><subject>Pyrolysis</subject><subject>Separation</subject><subject>Stirring</subject><subject>Temperature effects</subject><issn>0094-243X</issn><issn>1551-7616</issn><fulltext>true</fulltext><rsrctype>conference_proceeding</rsrctype><creationdate>2020</creationdate><recordtype>conference_proceeding</recordtype><recordid>eNp9kEtLAzEUhYMoWKsL_0HAnTA1j0kyWUrxBQU3LbgLmTxoynQSkxmh_97RFty5unD5zrn3HABuMVpgxOkDWyCEMBLNGZhhxnAlOObnYIaQrCtS049LcFXKDiEihWhmYLPeOlhc0lkPIfYwepi2ro9dMNDEfYpjbwv0Oe5hG2IVQwdTjnY0zh636ZBjdyih_EhNzL2JbbkGF153xd2c5hxsnp_Wy9dq9f7ytnxcVYaSZqg4pawVrOXMUsa9J61rTYN1zYj2FJuay8ZbaZ1rhEVYOEaorq1wnhspiaVzcHf0nX76HF0Z1C6OuZ9OKlJPiRGmkk7U_ZEqJgy_MVXKYa_zQX3FrJg6VaaS9f_BGKmfjv8E9Bt-TG66</recordid><startdate>20200604</startdate><enddate>20200604</enddate><creator>Fardhyanti, D. 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N.</creatorcontrib><creatorcontrib>Afifudin, M.</creatorcontrib><creatorcontrib>Mulyaningtyas, A.</creatorcontrib><creatorcontrib>Akhir, A. E.</creatorcontrib><creatorcontrib>Nuramalia, W.</creatorcontrib><creatorcontrib>Maulana, P.</creatorcontrib><collection>Technology Research Database</collection><collection>Aerospace Database</collection><collection>Advanced Technologies Database with Aerospace</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Fardhyanti, D. S.</au><au>Imani, N. A. C.</au><au>Damayanti, A.</au><au>Mardhotillah, S. N.</au><au>Afifudin, M.</au><au>Mulyaningtyas, A.</au><au>Akhir, A. E.</au><au>Nuramalia, W.</au><au>Maulana, P.</au><au>Rafi, Mohamad</au><au>Wahyuni, Wulan Tri</au><au>Heryanto, Rudi</au><format>book</format><genre>proceeding</genre><ristype>CONF</ristype><atitle>The separation of phenolic compounds from bio-oil produced from pyrolysis of corncobs</atitle><btitle>AIP conference proceedings</btitle><date>2020-06-04</date><risdate>2020</risdate><volume>2243</volume><issue>1</issue><issn>0094-243X</issn><eissn>1551-7616</eissn><coden>APCPCS</coden><abstract>Corncob is an agricultural waste which has a potential to be utilized as a raw material for bio-oil. One of many processes to convert the agricultural waste (biomass) into bio-oil is pyrolysis. The pyrolysis process for this study was carried out using fixed bed pyrolysis reactor, performed under temperature of 500°C and 600°C with residence time of 4 seconds. The bio-oil was analyzed for its components content using Gas Chromatography-Mass Spectrometry (GCMS). The separation of phenolic compounds from bio-oil was done by a liquid-liquid extraction which carried out for 60 minutes using methanol 80% and chloroform as solvent at various extraction temperatures of 30°C, 40°C, 50°C, and stirring speeds of 200 rpm, 250 rpm, 300 rpm. Then, the extract phase and the raffinate phase were analyzed using Folin-Ciocalteu method. The aim of this study was to determine the effect of temperatures and stirring speeds of the liquid-liquid extraction to the distribution coefficient and the yield of phenolic compound. The result showed that the main component of bio-oil obtained is phenolic compounds. The highest distribution coefficient and the highest yield of phenolic compound were obtained at 50°C and 300 rpm. The highest yield was 66.31% and 58.9% obtained from pyrolysis process at 500°C and 600°C, respectively. Meanwhile, the highest distribution coefficient was 11.08 and 8.92 for pyrolysis at 500°C and 600°C.</abstract><cop>Melville</cop><pub>American Institute of Physics</pub><doi>10.1063/5.0001078</doi><tpages>8</tpages><oa>free_for_read</oa></addata></record> |
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source | American Institute of Physics:Jisc Collections:Transitional Journals Agreement 2021-23 (Reading list) |
subjects | Agricultural production Agricultural wastes Chloroform Coefficients Fixed beds Gas chromatography Liquid-liquid extraction Mass spectrometry Phenols Pyrolysis Separation Stirring Temperature effects |
title | The separation of phenolic compounds from bio-oil produced from pyrolysis of corncobs |
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