MARC details
| 000 -LEADER |
| fixed length control field |
03512ntm a2200373 i 4500 |
| 001 - CONTROL NUMBER |
| control field |
vtls000102802 |
| 003 - CONTROL NUMBER IDENTIFIER |
| control field |
KUKTEM |
| 005 - DATE AND TIME OF LATEST TRANSACTION |
| control field |
20251117113357.0 |
| 008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION |
| fixed length control field |
180118t20172016my da f a m 000 0 eng d |
| 020 ## - INTERNATIONAL STANDARD BOOK NUMBER |
| International Standard Book Number |
THE0000937(Local) |
| 039 #9 - LEVEL OF BIBLIOGRAPHIC CONTROL AND CODING DETAIL [OBSOLETE] |
| Level of rules in bibliographic description |
201905271031 |
| Level of effort used to assign nonsubject heading access points |
nazirah |
| Level of effort used to assign subject headings |
201802081535 |
| Level of effort used to assign classification |
fateeha |
| Level of effort used to assign subject headings |
201801231137 |
| Level of effort used to assign classification |
fateeha |
| -- |
201801181035 |
| -- |
fateeha |
| 040 ## - CATALOGING SOURCE |
| Original cataloging agency |
UMP |
| Language of cataloging |
eng |
| Transcribing agency |
UMP |
| Description conventions |
rda |
| 090 ## - LOCALLY ASSIGNED LC-TYPE CALL NUMBER (OCLC); LOCAL CALL NUMBER (RLIN) |
| Classification number (OCLC) (R) ; Classification number, CALL (RLIN) (NR) |
FKKSA .L44 2017 r Bc. |
| 100 1# - MAIN ENTRY--PERSONAL NAME |
| Personal name |
Lee, Zhan Sheng, |
| Relator term |
author. |
| 245 10 - TITLE STATEMENT |
| Title |
Process simulation of co-gasification system using adaro coal & Empty Fruit Bunches (EFB) in aspen hysys / |
| Statement of responsibility, etc. |
Lee Zhan Sheng |
| 264 #1 - PRODUCTION, PUBLICATION, DISTRIBUTION, MANUFACTURE, AND COPYRIGHT NOTICE |
| Place of production, publication, distribution, manufacture |
Kuantan, Pahang : |
| Name of producer, publisher, distributor, manufacturer |
UMP, |
| Date of production, publication, distribution, manufacture, or copyright notice |
2017 |
| 264 #4 - PRODUCTION, PUBLICATION, DISTRIBUTION, MANUFACTURE, AND COPYRIGHT NOTICE |
| Date of production, publication, distribution, manufacture, or copyright notice |
© 2016 |
| 300 ## - PHYSICAL DESCRIPTION |
| Extent |
xvi, 92 pages : |
| Other physical details |
illustrations (some color), charts ; |
| Dimensions |
30 cm. + |
| Accompanying material |
1 CD-ROM |
| 336 ## - CONTENT TYPE |
| Content type term |
text |
| Source |
rdacontent |
| 336 ## - CONTENT TYPE |
| Content type term |
text |
| Source |
rdacontent |
| 337 ## - MEDIA TYPE |
| Media type term |
unmediated |
| Source |
rdamedia |
| 337 ## - MEDIA TYPE |
| Media type term |
computer |
| Source |
rdamedia |
| 338 ## - CARRIER TYPE |
| Carrier type term |
volume |
| Source |
rdacarrier |
| 338 ## - CARRIER TYPE |
| Carrier type term |
computer disc |
| Source |
rdacarrier |
| 347 ## - DIGITAL FILE CHARACTERISTICS |
| File type |
text file |
| Encoding format |
PDF |
| Source |
rda |
| 500 ## - GENERAL NOTE |
| General note |
Faculty of Chemical & Natural Resources Engineering |
| 502 ## - DISSERTATION NOTE |
| Dissertation note |
Project Paper (Bachelors of Chemical Engineering) -- Universiti Malaysia Pahang – 2017 |
| 504 ## - BIBLIOGRAPHY, ETC. NOTE |
| Bibliography, etc. note |
Includes bibliographical references |
| 520 3# - SUMMARY, ETC. |
| Summary, etc. |
In recent years, alternatives to fossil fuels have been thoroughly discussed and researched. One of the great interests would be co-gasification, which is the process of converting multiple components of carbon-containing feedstock, specifically comprising both biomass and coal in this project, under high temperature with limited air supply in gasifier to produce synthetic gas (syngas). The biggest motivation here is co-gasification is able to utilise coal cleanly while employing biomass as the renewable energy source. Malaysia is one of the biggest producers and exporters of palm oil today, and having Empty Fruit Bunches (EFB) as the palm oil waste. Currently, there is no comprehensive simulation work on co-gasification of using EFB as the main feedstock yet. This has strongly driven the initiation in researching this co-gasification process. ASPEN HYSYS simulator is employed to perform the simulation. Steady state, isothermal model was built in ASPEN HYSYS with the assumptions of all chemical reactions take place at equilibrium state with neglected pressure drop in gasifier. A total of four parameters to be investigated in this simulation consist of temperature, equivalence ratio (ER), feedstock’s ratio of biomass to coal (B/C) and ratio of steam to biomass (S/B). A set of total twelve reactor models simulates various reaction zones of the entrained flow gasifier, comprising of pyrolysis of feedstock, combustion and char gasification. The results of simulation are compared with literature work to determine the error. Syngas composition decreases with the increase of ER. The increase of gasification temperature will increase CO and H2 in the syngas composition, so to increase the heating value of syngas. Increasing S/B will increase the production of CH4 and H2 at the expense of CO. For B/C ratio parameter study, the result shows that plain biomass gasification is not efficient as compared to hybrid feedstock – biomass and coal. |
| 610 20 - SUBJECT ADDED ENTRY--CORPORATE NAME |
| Corporate name or jurisdiction name as entry element |
Faculty of Chemical & Natural Resources Engineering |
| 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 |