SIMULATION OF 1D-PSEUDOHOMOGENEOUS MODEL OF FIXED BED FISCHER-TROPSCH REACTOR USING BIOSYNGAS

Fossil fuels, especially petroleum, are the main source of energy in Indonesia. Based on BP Global Company data, in 2019 oil consumption reached 1.8 million bpd. Since petroleum is a non-renewable energy source, it is important to switch to environmentally friendly energy sources. One method of fuel...

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Main Author: Alwi Ash Shiddiq, Rasyid
Format: Final Project
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/67287
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:67287
spelling id-itb.:672872022-08-19T10:34:25ZSIMULATION OF 1D-PSEUDOHOMOGENEOUS MODEL OF FIXED BED FISCHER-TROPSCH REACTOR USING BIOSYNGAS Alwi Ash Shiddiq, Rasyid Indonesia Final Project 1D-pseudohomogeneous, Fischer-Tropsch, MATLAB, model, fixed bed reactor INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/67287 Fossil fuels, especially petroleum, are the main source of energy in Indonesia. Based on BP Global Company data, in 2019 oil consumption reached 1.8 million bpd. Since petroleum is a non-renewable energy source, it is important to switch to environmentally friendly energy sources. One method of fuel oil production is Fischer-Tropsch (FT) synthesis. In order to produce an environmentally friendly product, a feed in the form of biomass gasification synthesis gas called biosyngas is used. This study aims to build a FT reaction model and determine the effect of operating conditions on FT simulation results. The Fischer-Tropsch reactor built in this study is a fixed bed reactor in a 1D pseudo-homogeneous model with biosyngas feedstock (33% H2, 17% CO, and 50% N2). The simulation process of the Fischer-Tropsch reactor model was performed using MATLAB software at operating conditions of 20 bar and 473 K. The first operating condition varied was the Gas Hourly Space Velocity (GHSV) at values of 50, 100, 150, and 200 Nml.gcat-1h-1. The highest CO conversion was 66.36% at GHSV 37 Nml.gcat-1h-1 and the highest H2 conversion was 66.82% at GHSV 37 Nml.gcat-1h-1. C1-C4 selectivity values tended to increase, while C5+ selectivity decreased. The second operating condition varied was the H2/CO ratio in the feed at values of 1.0, 1.5, 2.0, and 2.5. The highest CO conversion was 70.35% at a ratio of 2.5 and the highest H2 conversion was 58.45% at a ratio of 1.5. The high ratio caused the selectivity of short-chain hydrocarbon products to increase. The third operating condition varied was the wall temperature (Tw) at 473K, 483K, and 493K. The highest CO and H2 conversions were obtained at the highest Tw with values of 88.54% and 86.30% respectively. High Tw causes the selectivity of short-chain hydrocarbons to increase. 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 Fossil fuels, especially petroleum, are the main source of energy in Indonesia. Based on BP Global Company data, in 2019 oil consumption reached 1.8 million bpd. Since petroleum is a non-renewable energy source, it is important to switch to environmentally friendly energy sources. One method of fuel oil production is Fischer-Tropsch (FT) synthesis. In order to produce an environmentally friendly product, a feed in the form of biomass gasification synthesis gas called biosyngas is used. This study aims to build a FT reaction model and determine the effect of operating conditions on FT simulation results. The Fischer-Tropsch reactor built in this study is a fixed bed reactor in a 1D pseudo-homogeneous model with biosyngas feedstock (33% H2, 17% CO, and 50% N2). The simulation process of the Fischer-Tropsch reactor model was performed using MATLAB software at operating conditions of 20 bar and 473 K. The first operating condition varied was the Gas Hourly Space Velocity (GHSV) at values of 50, 100, 150, and 200 Nml.gcat-1h-1. The highest CO conversion was 66.36% at GHSV 37 Nml.gcat-1h-1 and the highest H2 conversion was 66.82% at GHSV 37 Nml.gcat-1h-1. C1-C4 selectivity values tended to increase, while C5+ selectivity decreased. The second operating condition varied was the H2/CO ratio in the feed at values of 1.0, 1.5, 2.0, and 2.5. The highest CO conversion was 70.35% at a ratio of 2.5 and the highest H2 conversion was 58.45% at a ratio of 1.5. The high ratio caused the selectivity of short-chain hydrocarbon products to increase. The third operating condition varied was the wall temperature (Tw) at 473K, 483K, and 493K. The highest CO and H2 conversions were obtained at the highest Tw with values of 88.54% and 86.30% respectively. High Tw causes the selectivity of short-chain hydrocarbons to increase.
format Final Project
author Alwi Ash Shiddiq, Rasyid
spellingShingle Alwi Ash Shiddiq, Rasyid
SIMULATION OF 1D-PSEUDOHOMOGENEOUS MODEL OF FIXED BED FISCHER-TROPSCH REACTOR USING BIOSYNGAS
author_facet Alwi Ash Shiddiq, Rasyid
author_sort Alwi Ash Shiddiq, Rasyid
title SIMULATION OF 1D-PSEUDOHOMOGENEOUS MODEL OF FIXED BED FISCHER-TROPSCH REACTOR USING BIOSYNGAS
title_short SIMULATION OF 1D-PSEUDOHOMOGENEOUS MODEL OF FIXED BED FISCHER-TROPSCH REACTOR USING BIOSYNGAS
title_full SIMULATION OF 1D-PSEUDOHOMOGENEOUS MODEL OF FIXED BED FISCHER-TROPSCH REACTOR USING BIOSYNGAS
title_fullStr SIMULATION OF 1D-PSEUDOHOMOGENEOUS MODEL OF FIXED BED FISCHER-TROPSCH REACTOR USING BIOSYNGAS
title_full_unstemmed SIMULATION OF 1D-PSEUDOHOMOGENEOUS MODEL OF FIXED BED FISCHER-TROPSCH REACTOR USING BIOSYNGAS
title_sort simulation of 1d-pseudohomogeneous model of fixed bed fischer-tropsch reactor using biosyngas
url https://digilib.itb.ac.id/gdl/view/67287
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