Welcome To UTPedia

We would like to introduce you, the new knowledge repository product called UTPedia. The UTP Electronic and Digital Intellectual Asset. It stores digitized version of thesis, dissertation, final year project reports and past year examination questions.

Browse content of UTPedia using Year, Subject, Department and Author and Search for required document using Searching facilities included in UTPedia. UTPedia with full text are accessible for all registered users, whereas only the physical information and metadata can be retrieved by public users. UTPedia collaborating and connecting peoples with university’s intellectual works from anywhere.

Disclaimer - Universiti Teknologi PETRONAS shall not be liable for any loss or damage caused by the usage of any information obtained from this web site.Best viewed using Mozilla Firefox 3 or IE 7 with resolution 1024 x 768.

Simulation of Syngas Production via Carbon Dioxide Reforming of Methane in a Fluidized Bed Reactor

Husain, Mohd. Farhan Hatta (2002) Simulation of Syngas Production via Carbon Dioxide Reforming of Methane in a Fluidized Bed Reactor. Universiti Teknologi Petronas. (Unpublished)

[img] PDF
Download (1247Kb)

Abstract

The paper produced is to present the simulation results of an experiment. The experiment is about the reaction engineering of carbon dioxide reforming of methane in a fluidized bed reactor. The model to be constructed will be used to analysed mechanism and activity of the reaction. Carbon dioxide reforming is the latest method of obtaining syngas a valuable feedstock for many petrochemical industries. The product varies from naphtha to diesel and fuel additives in automotive industry. The project involves a study on surface engineering that is catalytic mechanism and activity of the process. Generally the study is based on a journal, which has been selected as the case study. Upon understanding of the basic mechanism, a simple simulation will be carried out for the selected process. Extensive literature review will give sufficient information towards the development of the model. Some calculations were made in order to obtain some parameters and variables, which will be used in the computer simulation. From the model created, it is found that the concentration profile along the catalyst bed drops at a very high rate before slowing down. Factors affecting the behavior of the reactant concentration will be discussed further.

Item Type: Final Year Project
Academic Subject : Academic Department - Chemical Engineering - Process Safety
Subject: T Technology > TP Chemical technology
Divisions: Engineering > Chemical
Depositing User: Users 2053 not found.
Date Deposited: 09 Oct 2013 11:08
Last Modified: 25 Jan 2017 09:47
URI: http://utpedia.utp.edu.my/id/eprint/8339

Actions (login required)

View Item View Item

Document Downloads

More statistics for this item...