MARC details
| 000 -LEADER |
| fixed length control field |
03796ntm a2200349 i 4500 |
| 003 - CONTROL NUMBER IDENTIFIER |
| control field |
MY-KuUP |
| 005 - DATE AND TIME OF LATEST TRANSACTION |
| control field |
20260707181203.0 |
| 006 - FIXED-LENGTH DATA ELEMENTS--ADDITIONAL MATERIAL CHARACTERISTICS |
| fixed length control field |
t|||||r|||| 000 0 |
| 007 - PHYSICAL DESCRIPTION FIXED FIELD--GENERAL INFORMATION |
| fixed length control field |
ta |
| 008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION |
| fixed length control field |
260707t20252025my a|||fr|||| 000 0 eng d |
| 020 ## - INTERNATIONAL STANDARD BOOK NUMBER |
| International Standard Book Number |
THE0010674 (Local) |
| Qualifying information |
Hardback |
| 040 ## - CATALOGING SOURCE |
| Original cataloging agency |
UMPSA |
| Language of cataloging |
eng |
| Transcribing agency |
UMPSA |
| Description conventions |
rda |
| 090 ## - LOCALLY ASSIGNED LC-TYPE CALL NUMBER (OCLC); LOCAL CALL NUMBER (RLIN) |
| Classification number (OCLC) (R) ; Classification number, CALL (RLIN) (NR) |
FTKKP .F38 2025 r Bc. |
| 100 0# - MAIN ENTRY--PERSONAL NAME |
| Personal name |
Fatin Laila Lissa Binti Mohamad Safri, |
| Relator term |
author. |
| 245 10 - TITLE STATEMENT |
| Title |
Performance of monometallic catalyst supported on calcium oxide derived fom lime carbide in toluene steam reforming for hydrogen-rich syngas production / |
| Statement of responsibility, etc. |
Fatin Laila Lissa Binti Mohamad Safri |
| 264 #1 - PRODUCTION, PUBLICATION, DISTRIBUTION, MANUFACTURE, AND COPYRIGHT NOTICE |
| Place of production, publication, distribution, manufacture |
Kuantan, Pahang : |
| Name of producer, publisher, distributor, manufacturer |
UMPSA, |
| Date of production, publication, distribution, manufacture, or copyright notice |
2025 |
| 264 #4 - PRODUCTION, PUBLICATION, DISTRIBUTION, MANUFACTURE, AND COPYRIGHT NOTICE |
| Date of production, publication, distribution, manufacture, or copyright notice |
© 2025 |
| 300 ## - PHYSICAL DESCRIPTION |
| Extent |
50 pages : |
| Other physical details |
illustrations ; |
| 336 ## - CONTENT TYPE |
| Source |
rdacontent |
| Content type term |
text |
| 337 ## - MEDIA TYPE |
| Source |
rdamedia |
| Media type term |
unmediated |
| 338 ## - CARRIER TYPE |
| Source |
rdacarrier |
| Carrier type term |
volume |
| 347 ## - DIGITAL FILE CHARACTERISTICS |
| Source |
rda |
| File type |
text file |
| Encoding format |
PDF |
| 500 ## - GENERAL NOTE |
| General note |
Faculty of Chemical and Process Engineering Technology |
| 502 ## - DISSERTATION NOTE |
| Dissertation note |
Final Year Report (Bachelor of Chemical Engineering ) -- Universiti Malaysia Pahang Al-Sultan Abdullah - 2025 |
| 504 ## - BIBLIOGRAPHY, ETC. NOTE |
| Bibliography, etc. note |
Include bibliographical reference |
| 520 3# - SUMMARY, ETC. |
| Summary, etc. |
Toluene steam reforming (TSR) presents notable environmental and economic benefits; however, it faces challenges, including catalyst deactivation due to coke formation. Nichol and cobalt are commonly used in TSR; however, their high carbon precipitation rate can lead to deactivation. The enhancement of catalytic activity and resistance to carbon deposition can be attained by investigating innovative catalysts that utilise waste-derived supports, such as calcium oxide (CaO). This study aims to examine the efficacy of a monometallic catalyst supported by lime carbide in Toluene Steam Reforming for syngas production. The catalysts employed in this research are Nickel (Ni) and Cobalt (Co), supported by Calcium oxide. The catalyst was synthesised using an ultrasonic-assisted technique, and its characterisation was conducted by XRD and FESEM investigations. The catalyst's efficacy in mitigating deactivation from coke formation in TSR is being adjusted based on two parameters: temperature and steam to carbon (SC) ratio. The employed temperature ranges from 700°C to 900°C, with steam-to-carbon ratios (S/C) of 1, 1.5, and 2. The syngas produced from this process is analysed using Gas Chromatography-Thermal Conductivity Detection (GC-TCD). This study shows that Ni/CaO is a better catalyst for toluene steam reforming (TSR) than Co/CaO, producing more syngas and higher hydrogen yields. Both catalysts performed best at 900°C, and the optimal steam-to-carbon (S/C) ratio was found to be 1.5. At this ratio, both toluene conversion and hydrogen yield were highest. The XRD results revealed that Ni/CaO maintained more active nickel at higher temperatures, making it more effective than Co/CaO, which formed less active cobalt oxide species. In summary, Ni/CaO is an effective catalyst for TSR, especially at 900°C with an S/C ratio of 1.5, which balances hydrogen production and toluene conversion. However, more research is needed to test its long-term stability and improve its resistance to coke formation. Future studies could also explore bi-metallic or hybrid catalysts, as well as using CaO or waste-derived supports, to further enhance performance and sustainability. As the need for clean energy grows, improving TSR for hydrogen-rich syngas production will be a key focus for both researchers and industries. Keywords:Toluene steam reforming;Catalyst support;Calcium oxide;Syngas production |
| 610 20 - SUBJECT ADDED ENTRY--CORPORATE NAME |
| Corporate name or jurisdiction name as entry element |
Faculty of Chemical and Process Engineering Technology |
| General subdivision |
Dissertations |
| 650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM |
| Topical term or geographic name entry element |
Universities and colleges |
| General subdivision |
Dissertations |
| 650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM |
| Topical term or geographic name entry element |
Theses |
| General subdivision |
Dissertations |
| 856 ## - ELECTRONIC LOCATION AND ACCESS |
| Uniform Resource Identifier |
https://umpir.ump.edu.my/id/eprint/47482 |
| 942 ## - ADDED ENTRY ELEMENTS (KOHA) |
| Source of classification or shelving scheme |
Library of Congress Classification |
| Koha item type |
Final Year Report |