000			03191ntm a2200349 i 4500
003			MY-KuUP
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008			260624t20242024my a|||fr|||| 000 0 eng d
020			_aTHE0010629 (Local) _qHardback
040			_aUMPSA _beng _cUMPSA _erda
090			_aFTKKP .Y56 2024 r Bc.
100	0		_aNur Yasmin Suraya Binti Yusri, _eauthor.
245	1	0	_aPalm oil mill biogas to syngas production: a simulation study _cNur Yasmin Suraya Binti Yusri
264		1	_aKuantan, Pahang : _bUMPSA, _c2024
264		4	_c© 2024
300			_a39 pages : _billustrations ;
336			_2rdacontent _atext
337			_2rdamedia _aunmediated
338			_2rdacarrier _avolume
347			_2rda _atext file _bPDF
500			_aFaculty of Chemical and Process Engineering Technology
502			_aFinal Year Report (Bachelor of Chemical Engineering ) -- Universiti Malaysia Pahang Al-Sultan Abdullah - 2024
504			_aInclude bibliographical reference
520	3		_aPalm oil mill effluent, also known as POME, is a wastewater produced by the milling of palm oil that needs to be effectively treated before being released into waterways. This is due to its extremely polluting characteristics. POME has a high COD and BOD, making it a highly polluting wastewater. Only 10% of the biomass used in palm oil mills in Malaysia is recycled to generates electricity, while the remaining 90% is disposed of as waste. However, biogas production coming from POME through anaerobic digestion contributes to GHG’s emission that could cause harm to the environment if it is not treated properly. POME undergoes anaerobic digestor to form biogas and with a further continuity with dry reforming process, biogas from POME can be converted into syngas, a mixture of H2 and CO. This research aims in using simulation of Aspen Plus to study the overall process of POME biogas to syngas production. The objective of this research aims to study the effect of POME compositions fed into anaerobic digestor towards syngas production and to study the effect of reaction temperature towards syngas production. Aspen Plus was used to simulate the process at range 500℃-850℃ in methane dry reforming. From the simulation, an analysis of CH4 and CO2 conversion and syngas production yield has been observed. From the simulation works, it was found that POME compositions with the highest amount of carbohydrate produced the highest conversions of CH4 and CO2 at 86.8% and 100.0% respectively and highest yields of H2 and CO at 91.4% and 92.5% respectively. Higher temperatures at 750 ℃ also led to higher conversions of CH4 and CO2 at 86.8% and 99.9% respectively and higher yield of H2 and CO at 91.3% and 92.5% respectively. Hence, the POME feed compositions and reaction temperature in methane dry reforming did affect the conversion and yield of syngas production from biogas generated from POME.
610	2	0	_aFaculty of Chemical and Process Engineering Technology _xDissertations
650		0	_aUniversities and colleges _xDissertations
650		0	_aTheses _xDissertations
856			_uhttps://umpir.ump.edu.my/id/eprint/47090
942			_2lcc _cPSM
999			_c105030 _d105036