POLYGLYCEROL SYNTHESIS USING KOH-DMSO & K2CO3-ZNO CATALYSTS: INVESTIGATION OF REACTION TIME, KOH-DMSO CONCENTRATION, AND K2CO3-ZNO COMPOSITION

Malikul Mulki Anas SuyadiOne of the efforts to utilize crude glycerol is by purifying it first and converting it into polyglycerol. Based on industrial-scale production, the synthesis of polyglycerol is often carried out at high temperatures and long reaction times. Therefore, this research aims to...

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Main Author: Mulki Anas Suyadi, Malikul
Format: Final Project
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/73237
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:73237
spelling id-itb.:732372023-06-16T15:48:38ZPOLYGLYCEROL SYNTHESIS USING KOH-DMSO & K2CO3-ZNO CATALYSTS: INVESTIGATION OF REACTION TIME, KOH-DMSO CONCENTRATION, AND K2CO3-ZNO COMPOSITION Mulki Anas Suyadi, Malikul Indonesia Final Project Polyglycerol, Glycerol, Catalyst, KOH, K2CO3 INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/73237 Malikul Mulki Anas SuyadiOne of the efforts to utilize crude glycerol is by purifying it first and converting it into polyglycerol. Based on industrial-scale production, the synthesis of polyglycerol is often carried out at high temperatures and long reaction times. Therefore, this research aims to synthesize polyglycerol under low-temperature operating conditions, short reaction times, and high selectivity to make the process more efficient and sustainable. To achieve this, glycerol is reacted with KOH & DMSO and K2CO3& ZnO catalysts. The yield of oligomers ranging from diglycerol to hexaglycerol obtained from using KOH and 5 mL of DMSO for reaction times of 2 hours, 4 hours, 6 hours, and 8 hours, respectively, is 9.33%, 32.46%, 36.40%, and 51.10%. For the yield obtained from using 10 mL of DMSO with a 2-hour reaction time, it is 25.23% for diglycerol to hexaglycerol and 58.98% for long-chain polyglycerol. For the yield obtained from using 1 mL of DMSO, no glycerol is converted, resulting in a yield of 0%. The fast reaction time and relatively high yield are due to the KOH-DMSO mixture forming a superbase medium. The yield of polyglycerol using the K2CO3+ ZnO catalyst is 0% because no glycerol is successfully converted. This is because the solubility property of ZnO in glycerol hinders the polymerization process. From the use of KOH & DMSO, it is shown that the production of polyglycerol does not require high temperatures as currently used in the polyglycerol industry. Ultimately, this efficient and sustainable synthesis of polyglycerol is expected to be commercialized so that the by-product from biodiesel production can be utilized with high added value. text
institution Institut Teknologi Bandung
building Institut Teknologi Bandung Library
continent Asia
country Indonesia
Indonesia
content_provider Institut Teknologi Bandung
collection Digital ITB
language Indonesia
description Malikul Mulki Anas SuyadiOne of the efforts to utilize crude glycerol is by purifying it first and converting it into polyglycerol. Based on industrial-scale production, the synthesis of polyglycerol is often carried out at high temperatures and long reaction times. Therefore, this research aims to synthesize polyglycerol under low-temperature operating conditions, short reaction times, and high selectivity to make the process more efficient and sustainable. To achieve this, glycerol is reacted with KOH & DMSO and K2CO3& ZnO catalysts. The yield of oligomers ranging from diglycerol to hexaglycerol obtained from using KOH and 5 mL of DMSO for reaction times of 2 hours, 4 hours, 6 hours, and 8 hours, respectively, is 9.33%, 32.46%, 36.40%, and 51.10%. For the yield obtained from using 10 mL of DMSO with a 2-hour reaction time, it is 25.23% for diglycerol to hexaglycerol and 58.98% for long-chain polyglycerol. For the yield obtained from using 1 mL of DMSO, no glycerol is converted, resulting in a yield of 0%. The fast reaction time and relatively high yield are due to the KOH-DMSO mixture forming a superbase medium. The yield of polyglycerol using the K2CO3+ ZnO catalyst is 0% because no glycerol is successfully converted. This is because the solubility property of ZnO in glycerol hinders the polymerization process. From the use of KOH & DMSO, it is shown that the production of polyglycerol does not require high temperatures as currently used in the polyglycerol industry. Ultimately, this efficient and sustainable synthesis of polyglycerol is expected to be commercialized so that the by-product from biodiesel production can be utilized with high added value.
format Final Project
author Mulki Anas Suyadi, Malikul
spellingShingle Mulki Anas Suyadi, Malikul
POLYGLYCEROL SYNTHESIS USING KOH-DMSO & K2CO3-ZNO CATALYSTS: INVESTIGATION OF REACTION TIME, KOH-DMSO CONCENTRATION, AND K2CO3-ZNO COMPOSITION
author_facet Mulki Anas Suyadi, Malikul
author_sort Mulki Anas Suyadi, Malikul
title POLYGLYCEROL SYNTHESIS USING KOH-DMSO & K2CO3-ZNO CATALYSTS: INVESTIGATION OF REACTION TIME, KOH-DMSO CONCENTRATION, AND K2CO3-ZNO COMPOSITION
title_short POLYGLYCEROL SYNTHESIS USING KOH-DMSO & K2CO3-ZNO CATALYSTS: INVESTIGATION OF REACTION TIME, KOH-DMSO CONCENTRATION, AND K2CO3-ZNO COMPOSITION
title_full POLYGLYCEROL SYNTHESIS USING KOH-DMSO & K2CO3-ZNO CATALYSTS: INVESTIGATION OF REACTION TIME, KOH-DMSO CONCENTRATION, AND K2CO3-ZNO COMPOSITION
title_fullStr POLYGLYCEROL SYNTHESIS USING KOH-DMSO & K2CO3-ZNO CATALYSTS: INVESTIGATION OF REACTION TIME, KOH-DMSO CONCENTRATION, AND K2CO3-ZNO COMPOSITION
title_full_unstemmed POLYGLYCEROL SYNTHESIS USING KOH-DMSO & K2CO3-ZNO CATALYSTS: INVESTIGATION OF REACTION TIME, KOH-DMSO CONCENTRATION, AND K2CO3-ZNO COMPOSITION
title_sort polyglycerol synthesis using koh-dmso & k2co3-zno catalysts: investigation of reaction time, koh-dmso concentration, and k2co3-zno composition
url https://digilib.itb.ac.id/gdl/view/73237
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