CNT production through the catalytic thermal decomposition of methane over Ni-Cu/A12O3 catalyst in a fluidized bed

A study on the optimization of the process and catalyst parameters for the production of CNTs over Ni-Cu/Al2O3 in a fluidized bed reactor was done. The process parameters were the inlet CH4 concentration and the reaction temperature, and the catalyst parameter was the catalyst metal loading. Optimiz...

Full description

Saved in:
Bibliographic Details
Main Author: Bernardo, Gian Paolo Obligacion
Format: text
Language:English
Published: Animo Repository 2012
Online Access:https://animorepository.dlsu.edu.ph/etd_masteral/4341
Tags: Add Tag
No Tags, Be the first to tag this record!
Institution: De La Salle University
Language: English
id oai:animorepository.dlsu.edu.ph:etd_masteral-11179
record_format eprints
spelling oai:animorepository.dlsu.edu.ph:etd_masteral-111792021-01-16T00:26:19Z CNT production through the catalytic thermal decomposition of methane over Ni-Cu/A12O3 catalyst in a fluidized bed Bernardo, Gian Paolo Obligacion A study on the optimization of the process and catalyst parameters for the production of CNTs over Ni-Cu/Al2O3 in a fluidized bed reactor was done. The process parameters were the inlet CH4 concentration and the reaction temperature, and the catalyst parameter was the catalyst metal loading. Optimization was done in terms of the diameter of the CNTs formed through the latest Solver function of Excel with integer and binary constraints on respective variables. The determination of the significance of the process and catalyst parameters was determined through ANOVA. Catalyst pre-characterization confirmed the presence of g-Al2O3, NiO and NiCu catalyst components. AAS results showed that the catalyst preparation method achieved the target metal loading, with the greatest deviation being 13.6%. BET data showed that the catalyst surface area and pore volume are directly proportional to the catalyst metal loading. The catalyst pore size, on the other hand, is inversely proportional to the catalyst metal loading. Catalyst post-characterization involved the measurement of the CNT diameters. Post-CTDM BET results showed that the initial surface area of the catalyst had no significant effect on the diameter of the CNTs.The smallest average CNT diameter was 48.5 nm produced with 5% CH4, 30% Ni loading with 12:5 mol:mol Ni:Cu, and 950°C reaction temperature. From the results, a non-linear model was developed which illustrated that the CNT diameter was generally inversely proportional with and a strong function of reaction temperature.Optimizing the model yielded 5% CH4, 10% Ni loading with 12:5 mol:mol Ni:Cu, and 950°C reaction temperature as the process parameters necessary to yield a minimum diameter of 47.75 nm for the CNTs. 2012-01-01T08:00:00Z text https://animorepository.dlsu.edu.ph/etd_masteral/4341 Master's Theses English Animo Repository
institution De La Salle University
building De La Salle University Library
continent Asia
country Philippines
Philippines
content_provider De La Salle University Library
collection DLSU Institutional Repository
language English
description A study on the optimization of the process and catalyst parameters for the production of CNTs over Ni-Cu/Al2O3 in a fluidized bed reactor was done. The process parameters were the inlet CH4 concentration and the reaction temperature, and the catalyst parameter was the catalyst metal loading. Optimization was done in terms of the diameter of the CNTs formed through the latest Solver function of Excel with integer and binary constraints on respective variables. The determination of the significance of the process and catalyst parameters was determined through ANOVA. Catalyst pre-characterization confirmed the presence of g-Al2O3, NiO and NiCu catalyst components. AAS results showed that the catalyst preparation method achieved the target metal loading, with the greatest deviation being 13.6%. BET data showed that the catalyst surface area and pore volume are directly proportional to the catalyst metal loading. The catalyst pore size, on the other hand, is inversely proportional to the catalyst metal loading. Catalyst post-characterization involved the measurement of the CNT diameters. Post-CTDM BET results showed that the initial surface area of the catalyst had no significant effect on the diameter of the CNTs.The smallest average CNT diameter was 48.5 nm produced with 5% CH4, 30% Ni loading with 12:5 mol:mol Ni:Cu, and 950°C reaction temperature. From the results, a non-linear model was developed which illustrated that the CNT diameter was generally inversely proportional with and a strong function of reaction temperature.Optimizing the model yielded 5% CH4, 10% Ni loading with 12:5 mol:mol Ni:Cu, and 950°C reaction temperature as the process parameters necessary to yield a minimum diameter of 47.75 nm for the CNTs.
format text
author Bernardo, Gian Paolo Obligacion
spellingShingle Bernardo, Gian Paolo Obligacion
CNT production through the catalytic thermal decomposition of methane over Ni-Cu/A12O3 catalyst in a fluidized bed
author_facet Bernardo, Gian Paolo Obligacion
author_sort Bernardo, Gian Paolo Obligacion
title CNT production through the catalytic thermal decomposition of methane over Ni-Cu/A12O3 catalyst in a fluidized bed
title_short CNT production through the catalytic thermal decomposition of methane over Ni-Cu/A12O3 catalyst in a fluidized bed
title_full CNT production through the catalytic thermal decomposition of methane over Ni-Cu/A12O3 catalyst in a fluidized bed
title_fullStr CNT production through the catalytic thermal decomposition of methane over Ni-Cu/A12O3 catalyst in a fluidized bed
title_full_unstemmed CNT production through the catalytic thermal decomposition of methane over Ni-Cu/A12O3 catalyst in a fluidized bed
title_sort cnt production through the catalytic thermal decomposition of methane over ni-cu/a12o3 catalyst in a fluidized bed
publisher Animo Repository
publishDate 2012
url https://animorepository.dlsu.edu.ph/etd_masteral/4341
_version_ 1769841898893082624