SAPO-34 Zeolite Membrane for CO2/N2 Separation

method that is used for purification of CO2 from high content CO2 gas with high pressure. However, this method is not applicable for lower CO2 content gases with atmospheric pressure such as flue gas. Membrane technology is potential to separate CO2 from gases, since membrane process requires les...

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Main Author: Steven Kencana, Kevin
Format: Final Project
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/38327
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:38327
spelling id-itb.:383272019-05-22T10:25:23ZSAPO-34 Zeolite Membrane for CO2/N2 Separation Steven Kencana, Kevin Indonesia Final Project CO2/N2 selectivity; SAPO-34 membrane; Optimized secondary growth; Permeability; Silica support INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/38327 method that is used for purification of CO2 from high content CO2 gas with high pressure. However, this method is not applicable for lower CO2 content gases with atmospheric pressure such as flue gas. Membrane technology is potential to separate CO2 from gases, since membrane process requires less energy. This study used a silica supported SAPO-34 zeolite membrane that has a pore size of 0.38 nm to effectively separate CO2 and N2 due to the molecular sieving and adsorption. This study aims to synthesize SAPO-34 on silica as support with optimized secondary growth which use combination of ageing, rubbing, and enhanced gel as synthesis method. The feed used in this research is pure gas CO2 and N2. The feed gas pressure varied from 150 kPa to 1500 kPa with flow rate of 2 SCFH. SAPO-34 membrane layer was successfully synthesized in the inside of tubular silica support with TEAOH as the structure directing agent. XRD result of SAPO-34 seeds showed the characteristics of SAPO-34 crystal with rhombohedral shape and high crystallinity. SEM analysis showed that the size of SAPO-34 seeds was about 200-400 nm and membrane thickness was about 1.7 ?m. The CO2 permeance of synthesized SAPO-34 membrane was about 5.48 x 10-6 mol/m2.s.Pa and the CO2/N2 selectivity was about 53. The highest permeance and selectivity was observed at 27°C and 98 kPa trans-membrane pressure. High selectivity of SAPO-34 membrane was the result of molecular sieving and selective adsorption separation mechanism. Silica support and optimized secondary growth create uniform SAPO-34 layer due to stronger hydrogen bonding and controlled growth of SAPO-34 crystals on membrane. 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 method that is used for purification of CO2 from high content CO2 gas with high pressure. However, this method is not applicable for lower CO2 content gases with atmospheric pressure such as flue gas. Membrane technology is potential to separate CO2 from gases, since membrane process requires less energy. This study used a silica supported SAPO-34 zeolite membrane that has a pore size of 0.38 nm to effectively separate CO2 and N2 due to the molecular sieving and adsorption. This study aims to synthesize SAPO-34 on silica as support with optimized secondary growth which use combination of ageing, rubbing, and enhanced gel as synthesis method. The feed used in this research is pure gas CO2 and N2. The feed gas pressure varied from 150 kPa to 1500 kPa with flow rate of 2 SCFH. SAPO-34 membrane layer was successfully synthesized in the inside of tubular silica support with TEAOH as the structure directing agent. XRD result of SAPO-34 seeds showed the characteristics of SAPO-34 crystal with rhombohedral shape and high crystallinity. SEM analysis showed that the size of SAPO-34 seeds was about 200-400 nm and membrane thickness was about 1.7 ?m. The CO2 permeance of synthesized SAPO-34 membrane was about 5.48 x 10-6 mol/m2.s.Pa and the CO2/N2 selectivity was about 53. The highest permeance and selectivity was observed at 27°C and 98 kPa trans-membrane pressure. High selectivity of SAPO-34 membrane was the result of molecular sieving and selective adsorption separation mechanism. Silica support and optimized secondary growth create uniform SAPO-34 layer due to stronger hydrogen bonding and controlled growth of SAPO-34 crystals on membrane.
format Final Project
author Steven Kencana, Kevin
spellingShingle Steven Kencana, Kevin
SAPO-34 Zeolite Membrane for CO2/N2 Separation
author_facet Steven Kencana, Kevin
author_sort Steven Kencana, Kevin
title SAPO-34 Zeolite Membrane for CO2/N2 Separation
title_short SAPO-34 Zeolite Membrane for CO2/N2 Separation
title_full SAPO-34 Zeolite Membrane for CO2/N2 Separation
title_fullStr SAPO-34 Zeolite Membrane for CO2/N2 Separation
title_full_unstemmed SAPO-34 Zeolite Membrane for CO2/N2 Separation
title_sort sapo-34 zeolite membrane for co2/n2 separation
url https://digilib.itb.ac.id/gdl/view/38327
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