Synthesis and Characterization Fe/SiO2 as Catalyst Fischer-Tropsch Using Impregnation and Sol-Gel Method

The Fischer-Tropsch (FT) reaction is a reaction that utilized CO and H2 (syngas) to produce hydrocarbon mixture that can be used as clean liquid fuel. Catalyst is the most important factor in FT reaction therefore it needs to be developed to increase productivity and selectivity of the FT reaction....

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Main Author: Ratna Sari, Dewi
Format: Final Project
Language:Indonesia
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Online Access:https://digilib.itb.ac.id/gdl/view/32271
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Institution: Institut Teknologi Bandung
Language: Indonesia
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spelling id-itb.:322712018-12-10T15:20:00ZSynthesis and Characterization Fe/SiO2 as Catalyst Fischer-Tropsch Using Impregnation and Sol-Gel Method Ratna Sari, Dewi Kimia Indonesia Final Project Catalyst, Fischer-Tropsch, Iron, Silica, Sol-Gel INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/32271 The Fischer-Tropsch (FT) reaction is a reaction that utilized CO and H2 (syngas) to produce hydrocarbon mixture that can be used as clean liquid fuel. Catalyst is the most important factor in FT reaction therefore it needs to be developed to increase productivity and selectivity of the FT reaction. In this research was compared characteristic of Fe/SiO2 as catalyst that synthesized using impregnation and sol-gel method. Silica used as supported material was synthesized using sol-gel method using tetraethyl orthosilicate (TEOS) as a precursor. TEOS was dissolved in methanol then hydrolyzed by adding NH3 solution. Dispersion of iron from Fe(NO3)3 solution on the supported material was done by wetness incipient impregnation (catalyst 1) and sol-gel (catalyst 2) methods. Both catalyst 1 and 2 was characterized using X-Ray Difraction (XRD), Nitrogen Fisisorption and Scanning Electron Microscopic (SEM). XRD difractogram showed that silica structure of both catalysts is amorphous. Nitrogen fisisorption revealed that surface area of silica used in catalyst 1 is 585.200 m2/g and after impregnation (catalyst 1) is 530.641 m2/g, while surface area of catalyst 2 is 471.502 m2/g. Catalitycal activity test was conducted using fixed bed reactor at 1.05 atm, 473 K, with CO : H2 ratio 1: 2 and approximately 15 mL/min flow rate. Catalytical activity expressed in % conversion of CO is 14.20% for catalyst 1 and 15.33% for catalyst 2, therefore it can be concluded that sol-gel method produce better FT catalyst. Later on iron precursor in sol–gel method was varied using Fe(NO3)3.9H2O, FeCl3.6H2O and Na[Fe(EDTA)] which respectively has catalitycal activity of 14.38, 17.72 and 8.60%. Based on CO conversion, it can be known that catalyst that was synthesized using FeCl3.H2O as iron precursor has the highest catalityc activity. 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
topic Kimia
spellingShingle Kimia
Ratna Sari, Dewi
Synthesis and Characterization Fe/SiO2 as Catalyst Fischer-Tropsch Using Impregnation and Sol-Gel Method
description The Fischer-Tropsch (FT) reaction is a reaction that utilized CO and H2 (syngas) to produce hydrocarbon mixture that can be used as clean liquid fuel. Catalyst is the most important factor in FT reaction therefore it needs to be developed to increase productivity and selectivity of the FT reaction. In this research was compared characteristic of Fe/SiO2 as catalyst that synthesized using impregnation and sol-gel method. Silica used as supported material was synthesized using sol-gel method using tetraethyl orthosilicate (TEOS) as a precursor. TEOS was dissolved in methanol then hydrolyzed by adding NH3 solution. Dispersion of iron from Fe(NO3)3 solution on the supported material was done by wetness incipient impregnation (catalyst 1) and sol-gel (catalyst 2) methods. Both catalyst 1 and 2 was characterized using X-Ray Difraction (XRD), Nitrogen Fisisorption and Scanning Electron Microscopic (SEM). XRD difractogram showed that silica structure of both catalysts is amorphous. Nitrogen fisisorption revealed that surface area of silica used in catalyst 1 is 585.200 m2/g and after impregnation (catalyst 1) is 530.641 m2/g, while surface area of catalyst 2 is 471.502 m2/g. Catalitycal activity test was conducted using fixed bed reactor at 1.05 atm, 473 K, with CO : H2 ratio 1: 2 and approximately 15 mL/min flow rate. Catalytical activity expressed in % conversion of CO is 14.20% for catalyst 1 and 15.33% for catalyst 2, therefore it can be concluded that sol-gel method produce better FT catalyst. Later on iron precursor in sol–gel method was varied using Fe(NO3)3.9H2O, FeCl3.6H2O and Na[Fe(EDTA)] which respectively has catalitycal activity of 14.38, 17.72 and 8.60%. Based on CO conversion, it can be known that catalyst that was synthesized using FeCl3.H2O as iron precursor has the highest catalityc activity.
format Final Project
author Ratna Sari, Dewi
author_facet Ratna Sari, Dewi
author_sort Ratna Sari, Dewi
title Synthesis and Characterization Fe/SiO2 as Catalyst Fischer-Tropsch Using Impregnation and Sol-Gel Method
title_short Synthesis and Characterization Fe/SiO2 as Catalyst Fischer-Tropsch Using Impregnation and Sol-Gel Method
title_full Synthesis and Characterization Fe/SiO2 as Catalyst Fischer-Tropsch Using Impregnation and Sol-Gel Method
title_fullStr Synthesis and Characterization Fe/SiO2 as Catalyst Fischer-Tropsch Using Impregnation and Sol-Gel Method
title_full_unstemmed Synthesis and Characterization Fe/SiO2 as Catalyst Fischer-Tropsch Using Impregnation and Sol-Gel Method
title_sort synthesis and characterization fe/sio2 as catalyst fischer-tropsch using impregnation and sol-gel method
url https://digilib.itb.ac.id/gdl/view/32271
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