MARC details
| 000 -LEADER |
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| fixed length control field |
02896ntm a2200349 i 4500 |
| 003 - CONTROL NUMBER IDENTIFIER |
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| control field |
MY-KuUP |
| 005 - DATE AND TIME OF LATEST TRANSACTION |
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| control field |
20260709120014.0 |
| 006 - FIXED-LENGTH DATA ELEMENTS--ADDITIONAL MATERIAL CHARACTERISTICS |
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| fixed length control field |
t|||||r|||| 000 0 |
| 007 - PHYSICAL DESCRIPTION FIXED FIELD--GENERAL INFORMATION |
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| fixed length control field |
ta |
| 008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION |
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| fixed length control field |
260709t20252025my a|||fr|||| 000 0 eng d |
| 020 ## - INTERNATIONAL STANDARD BOOK NUMBER |
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| International Standard Book Number |
THE0010688 (Local) |
| Qualifying information |
Hardback |
| 040 ## - CATALOGING SOURCE |
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| 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) |
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| Classification number (OCLC) (R) ; Classification number, CALL (RLIN) (NR) |
FTKKP .I74 2025 r Bc. |
| 100 0# - MAIN ENTRY--PERSONAL NAME |
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| Personal name |
Mohamad Irfan Bin Nordin, , , |
| Relator term |
author. |
| 245 10 - TITLE STATEMENT |
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| Title |
Conversion of ethanol to hydrogen over co/pofa catalyst / |
| Statement of responsibility, etc. |
Mohamad Irfan Bin Nordin |
| 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 |
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| Extent |
xv, 66 pages : |
| Other physical details |
illustrations ; |
| 336 ## - CONTENT TYPE |
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| Source |
rdacontent |
| Content type term |
text |
| 337 ## - MEDIA TYPE |
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| Source |
rdamedia |
| Media type term |
unmediated |
| 338 ## - CARRIER TYPE |
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| Source |
rdacarrier |
| Carrier type term |
volume |
| 347 ## - DIGITAL FILE CHARACTERISTICS |
|---|
| Source |
rda |
| File type |
text file |
| Encoding format |
PDF |
| 500 ## - GENERAL NOTE |
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| General note |
Faculty of Chemical and Process Engineering Technology |
| 502 ## - DISSERTATION NOTE |
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| Dissertation note |
Final Year Report (Bachelor of Chemical Engineering ) -- Universiti Malaysia Pahang Al-Sultan Abdullah - 2025 |
| 504 ## - BIBLIOGRAPHY, ETC. NOTE |
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| Bibliography, etc. note |
Include bibliographical reference |
| 520 3# - SUMMARY, ETC. |
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| Summary, etc. |
Syngas, a combination of hydrogen (H2) and carbon monoxide (CO), is produced by the thermochemical process of ethanol dry reforming, which takes ethanol (C2H5OH) and carbon dioxide (CO2). The physicochemical characteristics of the catalyst at different Cobalt (Co) loadings supported by palm oil fuel ash (POFA) and the effectiveness of the Co/POFA catalysts for ethanol dry reforming to produce syngas were the primary objectives of this study. The mass change in Thermal-Gravimetric Analysis (TGA) will be used to characterize the synthesized catalyst, and Fourier Transform Infrared Spectroscopy (FTIR) will be used to determines the chemical bonds that exist within the catalyst. Brunaeur-Emmett-Teller (BET) will be used to determine the catalyst's surface area. In a fixed-bed reactor with regulated temperature and pressure, the prepared catalysts' dry reforming performance is assessed. Systematically, the impact of the cobalt precursor on the catalyst's resistance to deactivation, selectivity towards desired products (H2 and CO), and activity for producing hydrogen is examined. As the weight percentage of cobalt in POFA increases, the conversion and yield of syngas produced also increase. This happens as a result of the carbon attaching to the catalyst surface and creating syngas. The fixed-bed reactor containing the cobalt with the weight percentages (5wt%, 10wt%, 15wt%, and 20wt%), supported by POFA, will be used, and the temperature at which the ethanol dry reforming reaction occurs will be fixed (750oC). For this study, the ultrasonic method will be utilized to produce the Co/POFA catalyst. |
| 610 20 - SUBJECT ADDED ENTRY--CORPORATE NAME |
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| 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 |
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| 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 |
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| Uniform Resource Identifier |
https://umpir.ump.edu.my/id/eprint/47501 |
| 942 ## - ADDED ENTRY ELEMENTS (KOHA) |
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| Source of classification or shelving scheme |
Library of Congress Classification |
| Koha item type |
Final Year Report |