The Study Of Conversion Cpo To Polyol (Polyalcohol)

Indonesia is the second big CPO producer after Malaysia. The CPO production of Indonesia gradually increases and reaches 8.2 million tones. About two third of it is used to meet the domestic will receive little income. Therefore, it must be converted into the other product, which has the high value....
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Autor*in:	F. S. Budi [verfasserIn] z. Abidin [verfasserIn]

Format:	E-Artikel
Sprache:	Englisch ; Indonesisch

Erschienen:	2017

Schlagwörter:	CPO, hydroxylation, polyol

Übergeordnetes Werk:	In: Reaktor - Diponegoro University, 2015, 11(2017), 1, Seite 8-13
Übergeordnetes Werk:	volume:11 ; year:2017 ; number:1 ; pages:8-13

Links:	Link aufrufen Link aufrufen Link aufrufen Journal toc Journal toc

DOI / URN:	10.14710/reaktor.11.1.8-13

Katalog-ID:	DOAJ019110596

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520			\|a Indonesia is the second big CPO producer after Malaysia. The CPO production of Indonesia gradually increases and reaches 8.2 million tones. About two third of it is used to meet the domestic will receive little income. Therefore, it must be converted into the other product, which has the high value. The main component of it is glyceride composed of glycerol and fatty acid. The glyceride can be converted into polyol (polyalcohol) which is the material in manufacturing polyurethane, cosmetic, lubricant etc. the process of converting of CPO into polyol is called the hydroxylation. This research aim to study the hydroxylation process of CPO into polyol and to optimize the variable which really affect the hydroxyl number of product. Based on the experiment, the optimum condition of hydroxylation of CPO with the hydrogen peroxide (H2O2) and the formic acid (HCOOH) into polyol is got as follows: temperature 50 0C, composition of reactan 40% and time 2 hours. The polyol produced has the hydroxyl number 148. Keywords : CPO, hydroxylation, polyol
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allfields	10.14710/reaktor.11.1.8-13 doi (DE-627)DOAJ019110596 (DE-599)DOAJc2d90b06860447bc9835557cd567644b DE-627 ger DE-627 rakwb eng ind TP155-156 F. S. Budi verfasserin aut The Study Of Conversion Cpo To Polyol (Polyalcohol) 2017 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Indonesia is the second big CPO producer after Malaysia. The CPO production of Indonesia gradually increases and reaches 8.2 million tones. About two third of it is used to meet the domestic will receive little income. Therefore, it must be converted into the other product, which has the high value. The main component of it is glyceride composed of glycerol and fatty acid. The glyceride can be converted into polyol (polyalcohol) which is the material in manufacturing polyurethane, cosmetic, lubricant etc. the process of converting of CPO into polyol is called the hydroxylation. This research aim to study the hydroxylation process of CPO into polyol and to optimize the variable which really affect the hydroxyl number of product. Based on the experiment, the optimum condition of hydroxylation of CPO with the hydrogen peroxide (H2O2) and the formic acid (HCOOH) into polyol is got as follows: temperature 50 0C, composition of reactan 40% and time 2 hours. The polyol produced has the hydroxyl number 148. Keywords : CPO, hydroxylation, polyol CPO, hydroxylation, polyol Chemical engineering z. Abidin verfasserin aut In Reaktor Diponegoro University, 2015 11(2017), 1, Seite 8-13 (DE-627)818489049 (DE-600)2810102-9 24075973 nnns volume:11 year:2017 number:1 pages:8-13 https://doi.org/10.14710/reaktor.11.1.8-13 kostenfrei https://doaj.org/article/c2d90b06860447bc9835557cd567644b kostenfrei https://ejournal.undip.ac.id/index.php/reaktor/article/view/14906 kostenfrei https://doaj.org/toc/0852-0798 Journal toc kostenfrei https://doaj.org/toc/2407-5973 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_138 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_187 GBV_ILN_213 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_647 GBV_ILN_702 GBV_ILN_2014 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 11 2017 1 8-13
spelling	10.14710/reaktor.11.1.8-13 doi (DE-627)DOAJ019110596 (DE-599)DOAJc2d90b06860447bc9835557cd567644b DE-627 ger DE-627 rakwb eng ind TP155-156 F. S. Budi verfasserin aut The Study Of Conversion Cpo To Polyol (Polyalcohol) 2017 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Indonesia is the second big CPO producer after Malaysia. The CPO production of Indonesia gradually increases and reaches 8.2 million tones. About two third of it is used to meet the domestic will receive little income. Therefore, it must be converted into the other product, which has the high value. The main component of it is glyceride composed of glycerol and fatty acid. The glyceride can be converted into polyol (polyalcohol) which is the material in manufacturing polyurethane, cosmetic, lubricant etc. the process of converting of CPO into polyol is called the hydroxylation. This research aim to study the hydroxylation process of CPO into polyol and to optimize the variable which really affect the hydroxyl number of product. Based on the experiment, the optimum condition of hydroxylation of CPO with the hydrogen peroxide (H2O2) and the formic acid (HCOOH) into polyol is got as follows: temperature 50 0C, composition of reactan 40% and time 2 hours. The polyol produced has the hydroxyl number 148. Keywords : CPO, hydroxylation, polyol CPO, hydroxylation, polyol Chemical engineering z. Abidin verfasserin aut In Reaktor Diponegoro University, 2015 11(2017), 1, Seite 8-13 (DE-627)818489049 (DE-600)2810102-9 24075973 nnns volume:11 year:2017 number:1 pages:8-13 https://doi.org/10.14710/reaktor.11.1.8-13 kostenfrei https://doaj.org/article/c2d90b06860447bc9835557cd567644b kostenfrei https://ejournal.undip.ac.id/index.php/reaktor/article/view/14906 kostenfrei https://doaj.org/toc/0852-0798 Journal toc kostenfrei https://doaj.org/toc/2407-5973 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_138 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_187 GBV_ILN_213 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_647 GBV_ILN_702 GBV_ILN_2014 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 11 2017 1 8-13
allfields_unstemmed	10.14710/reaktor.11.1.8-13 doi (DE-627)DOAJ019110596 (DE-599)DOAJc2d90b06860447bc9835557cd567644b DE-627 ger DE-627 rakwb eng ind TP155-156 F. S. Budi verfasserin aut The Study Of Conversion Cpo To Polyol (Polyalcohol) 2017 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Indonesia is the second big CPO producer after Malaysia. The CPO production of Indonesia gradually increases and reaches 8.2 million tones. About two third of it is used to meet the domestic will receive little income. Therefore, it must be converted into the other product, which has the high value. The main component of it is glyceride composed of glycerol and fatty acid. The glyceride can be converted into polyol (polyalcohol) which is the material in manufacturing polyurethane, cosmetic, lubricant etc. the process of converting of CPO into polyol is called the hydroxylation. This research aim to study the hydroxylation process of CPO into polyol and to optimize the variable which really affect the hydroxyl number of product. Based on the experiment, the optimum condition of hydroxylation of CPO with the hydrogen peroxide (H2O2) and the formic acid (HCOOH) into polyol is got as follows: temperature 50 0C, composition of reactan 40% and time 2 hours. The polyol produced has the hydroxyl number 148. Keywords : CPO, hydroxylation, polyol CPO, hydroxylation, polyol Chemical engineering z. Abidin verfasserin aut In Reaktor Diponegoro University, 2015 11(2017), 1, Seite 8-13 (DE-627)818489049 (DE-600)2810102-9 24075973 nnns volume:11 year:2017 number:1 pages:8-13 https://doi.org/10.14710/reaktor.11.1.8-13 kostenfrei https://doaj.org/article/c2d90b06860447bc9835557cd567644b kostenfrei https://ejournal.undip.ac.id/index.php/reaktor/article/view/14906 kostenfrei https://doaj.org/toc/0852-0798 Journal toc kostenfrei https://doaj.org/toc/2407-5973 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_138 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_187 GBV_ILN_213 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_647 GBV_ILN_702 GBV_ILN_2014 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 11 2017 1 8-13
allfieldsGer	10.14710/reaktor.11.1.8-13 doi (DE-627)DOAJ019110596 (DE-599)DOAJc2d90b06860447bc9835557cd567644b DE-627 ger DE-627 rakwb eng ind TP155-156 F. S. Budi verfasserin aut The Study Of Conversion Cpo To Polyol (Polyalcohol) 2017 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Indonesia is the second big CPO producer after Malaysia. The CPO production of Indonesia gradually increases and reaches 8.2 million tones. About two third of it is used to meet the domestic will receive little income. Therefore, it must be converted into the other product, which has the high value. The main component of it is glyceride composed of glycerol and fatty acid. The glyceride can be converted into polyol (polyalcohol) which is the material in manufacturing polyurethane, cosmetic, lubricant etc. the process of converting of CPO into polyol is called the hydroxylation. This research aim to study the hydroxylation process of CPO into polyol and to optimize the variable which really affect the hydroxyl number of product. Based on the experiment, the optimum condition of hydroxylation of CPO with the hydrogen peroxide (H2O2) and the formic acid (HCOOH) into polyol is got as follows: temperature 50 0C, composition of reactan 40% and time 2 hours. The polyol produced has the hydroxyl number 148. Keywords : CPO, hydroxylation, polyol CPO, hydroxylation, polyol Chemical engineering z. Abidin verfasserin aut In Reaktor Diponegoro University, 2015 11(2017), 1, Seite 8-13 (DE-627)818489049 (DE-600)2810102-9 24075973 nnns volume:11 year:2017 number:1 pages:8-13 https://doi.org/10.14710/reaktor.11.1.8-13 kostenfrei https://doaj.org/article/c2d90b06860447bc9835557cd567644b kostenfrei https://ejournal.undip.ac.id/index.php/reaktor/article/view/14906 kostenfrei https://doaj.org/toc/0852-0798 Journal toc kostenfrei https://doaj.org/toc/2407-5973 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_138 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_187 GBV_ILN_213 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_647 GBV_ILN_702 GBV_ILN_2014 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 11 2017 1 8-13
allfieldsSound	10.14710/reaktor.11.1.8-13 doi (DE-627)DOAJ019110596 (DE-599)DOAJc2d90b06860447bc9835557cd567644b DE-627 ger DE-627 rakwb eng ind TP155-156 F. S. Budi verfasserin aut The Study Of Conversion Cpo To Polyol (Polyalcohol) 2017 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Indonesia is the second big CPO producer after Malaysia. The CPO production of Indonesia gradually increases and reaches 8.2 million tones. About two third of it is used to meet the domestic will receive little income. Therefore, it must be converted into the other product, which has the high value. The main component of it is glyceride composed of glycerol and fatty acid. The glyceride can be converted into polyol (polyalcohol) which is the material in manufacturing polyurethane, cosmetic, lubricant etc. the process of converting of CPO into polyol is called the hydroxylation. This research aim to study the hydroxylation process of CPO into polyol and to optimize the variable which really affect the hydroxyl number of product. Based on the experiment, the optimum condition of hydroxylation of CPO with the hydrogen peroxide (H2O2) and the formic acid (HCOOH) into polyol is got as follows: temperature 50 0C, composition of reactan 40% and time 2 hours. The polyol produced has the hydroxyl number 148. Keywords : CPO, hydroxylation, polyol CPO, hydroxylation, polyol Chemical engineering z. Abidin verfasserin aut In Reaktor Diponegoro University, 2015 11(2017), 1, Seite 8-13 (DE-627)818489049 (DE-600)2810102-9 24075973 nnns volume:11 year:2017 number:1 pages:8-13 https://doi.org/10.14710/reaktor.11.1.8-13 kostenfrei https://doaj.org/article/c2d90b06860447bc9835557cd567644b kostenfrei https://ejournal.undip.ac.id/index.php/reaktor/article/view/14906 kostenfrei https://doaj.org/toc/0852-0798 Journal toc kostenfrei https://doaj.org/toc/2407-5973 Journal toc kostenfrei GBV_USEFLAG_A SYSFLAG_A GBV_DOAJ GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_65 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_138 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_187 GBV_ILN_213 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_647 GBV_ILN_702 GBV_ILN_2014 GBV_ILN_4012 GBV_ILN_4037 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4249 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4338 GBV_ILN_4367 GBV_ILN_4700 AR 11 2017 1 8-13
language	English Indonesian
source	In Reaktor 11(2017), 1, Seite 8-13 volume:11 year:2017 number:1 pages:8-13
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S. Budi</subfield><subfield code="e">verfasserin</subfield><subfield code="4">aut</subfield></datafield><datafield tag="245" ind1="1" ind2="4"><subfield code="a">The Study Of Conversion Cpo To Polyol (Polyalcohol)</subfield></datafield><datafield tag="264" ind1=" " ind2="1"><subfield code="c">2017</subfield></datafield><datafield tag="336" ind1=" " ind2=" "><subfield code="a">Text</subfield><subfield code="b">txt</subfield><subfield code="2">rdacontent</subfield></datafield><datafield tag="337" ind1=" " ind2=" "><subfield code="a">Computermedien</subfield><subfield code="b">c</subfield><subfield code="2">rdamedia</subfield></datafield><datafield tag="338" ind1=" " ind2=" "><subfield code="a">Online-Ressource</subfield><subfield code="b">cr</subfield><subfield code="2">rdacarrier</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Indonesia is the second big CPO producer after Malaysia. The CPO production of Indonesia gradually increases and reaches 8.2 million tones. About two third of it is used to meet the domestic will receive little income. Therefore, it must be converted into the other product, which has the high value. The main component of it is glyceride composed of glycerol and fatty acid. The glyceride can be converted into polyol (polyalcohol) which is the material in manufacturing polyurethane, cosmetic, lubricant etc. the process of converting of CPO into polyol is called the hydroxylation. This research aim to study the hydroxylation process of CPO into polyol and to optimize the variable which really affect the hydroxyl number of product. Based on the experiment, the optimum condition of hydroxylation of CPO with the hydrogen peroxide (H2O2) and the formic acid (HCOOH) into polyol is got as follows: temperature 50 0C, composition of reactan 40% and time 2 hours. The polyol produced has the hydroxyl number 148. 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callnumber-first	T - Technology
author	F. S. Budi
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topic_title	TP155-156 The Study Of Conversion Cpo To Polyol (Polyalcohol) CPO, hydroxylation, polyol
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title	The Study Of Conversion Cpo To Polyol (Polyalcohol)
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title_sort	study of conversion cpo to polyol (polyalcohol)
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title_auth	The Study Of Conversion Cpo To Polyol (Polyalcohol)
abstract	Indonesia is the second big CPO producer after Malaysia. The CPO production of Indonesia gradually increases and reaches 8.2 million tones. About two third of it is used to meet the domestic will receive little income. Therefore, it must be converted into the other product, which has the high value. The main component of it is glyceride composed of glycerol and fatty acid. The glyceride can be converted into polyol (polyalcohol) which is the material in manufacturing polyurethane, cosmetic, lubricant etc. the process of converting of CPO into polyol is called the hydroxylation. This research aim to study the hydroxylation process of CPO into polyol and to optimize the variable which really affect the hydroxyl number of product. Based on the experiment, the optimum condition of hydroxylation of CPO with the hydrogen peroxide (H2O2) and the formic acid (HCOOH) into polyol is got as follows: temperature 50 0C, composition of reactan 40% and time 2 hours. The polyol produced has the hydroxyl number 148. Keywords : CPO, hydroxylation, polyol
abstractGer	Indonesia is the second big CPO producer after Malaysia. The CPO production of Indonesia gradually increases and reaches 8.2 million tones. About two third of it is used to meet the domestic will receive little income. Therefore, it must be converted into the other product, which has the high value. The main component of it is glyceride composed of glycerol and fatty acid. The glyceride can be converted into polyol (polyalcohol) which is the material in manufacturing polyurethane, cosmetic, lubricant etc. the process of converting of CPO into polyol is called the hydroxylation. This research aim to study the hydroxylation process of CPO into polyol and to optimize the variable which really affect the hydroxyl number of product. Based on the experiment, the optimum condition of hydroxylation of CPO with the hydrogen peroxide (H2O2) and the formic acid (HCOOH) into polyol is got as follows: temperature 50 0C, composition of reactan 40% and time 2 hours. The polyol produced has the hydroxyl number 148. Keywords : CPO, hydroxylation, polyol
abstract_unstemmed	Indonesia is the second big CPO producer after Malaysia. The CPO production of Indonesia gradually increases and reaches 8.2 million tones. About two third of it is used to meet the domestic will receive little income. Therefore, it must be converted into the other product, which has the high value. The main component of it is glyceride composed of glycerol and fatty acid. The glyceride can be converted into polyol (polyalcohol) which is the material in manufacturing polyurethane, cosmetic, lubricant etc. the process of converting of CPO into polyol is called the hydroxylation. This research aim to study the hydroxylation process of CPO into polyol and to optimize the variable which really affect the hydroxyl number of product. Based on the experiment, the optimum condition of hydroxylation of CPO with the hydrogen peroxide (H2O2) and the formic acid (HCOOH) into polyol is got as follows: temperature 50 0C, composition of reactan 40% and time 2 hours. The polyol produced has the hydroxyl number 148. Keywords : CPO, hydroxylation, polyol
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title_short	The Study Of Conversion Cpo To Polyol (Polyalcohol)
url	https://doi.org/10.14710/reaktor.11.1.8-13 https://doaj.org/article/c2d90b06860447bc9835557cd567644b https://ejournal.undip.ac.id/index.php/reaktor/article/view/14906 https://doaj.org/toc/0852-0798 https://doaj.org/toc/2407-5973
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