MARC details
| 000 -LEADER |
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| fixed length control field |
03407ntm 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 |
20260710181416.0 |
| 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 |
260710t20252025my a|||fr|||| 000 0 eng d |
| 020 ## - INTERNATIONAL STANDARD BOOK NUMBER |
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| International Standard Book Number |
THE0010707 (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 .A857 2025 r Bc. |
| 100 0# - MAIN ENTRY--PERSONAL NAME |
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| Personal name |
Nurul Atirah Binti Hosi, , , |
| Relator term |
author. |
| 245 10 - TITLE STATEMENT |
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| Title |
Development of new modified thermodynamic equilibrium model for estimating product gas and TAR generation from biomass gasification process / |
| Statement of responsibility, etc. |
Nurul Atirah Binti Hosi |
| 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 |
60 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. |
The work discusses the development of a comprehensive thermodynamic equilibrium model-based framework for biomass gasification processes. This framework includes models for fixed bed, fluidized bed, and entrained flow gasifiers, supported by a biomass database. The study aims to modify the thermodynamic equilibrium model to predict synthesis gas (CO, CO2, CH4, H2), char, and tar in biomass gasification using steam as the gasifying agent. This research focuses on evaluating the original thermodynamic equilibrium model and modifying it to predict synthesis gas, char, and tar. It includes model simulation and validation, along with studying the effects of operating conditions on synthesis gas, char, tar, and gasification performance (cold gas efficiency, lower heating value, carbon conversion, and synthesis gas yield) within a temperature range of 600°C to 1000°C. Biomass gasification is motivated by its ability to use waste materials as feedstock to reduce waste and increase efficiency. However, one key issue is its reliance on simplifying assumptions and idealized conditions. While helpful for modeling, these assumptions may not match real gasifier conditions. The biomass tested using this model by process and product specification to employ one type of gasifiers which are fixed bed gasifiers. Following that, model validation and simulation use to the validation process confirms the applicability of the model for analyzing gas production in fixed bed gasifiers. Since the type of biomass that have been choose are empty fruit bunch raw, empty fruit bunch torrefied, palm kernel shell raw and palm kernel shell torrefied, the peak stability of the gasification process is reached at 900 °C, 800 °C and 900 °C, 900 °C and 700 °C, respectively, making it the optimal gasification temperature as the highest synthesis gas yield appeared at this temperature. The result of the performance analysis shows that the fixed bed gasifier is more efficient than fluidized bed and entrained flow gasifier in terms of gas production. |
| 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/47582 |
| 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 |