ISOTHERM AND KINETIC STUDIES OF RESIDUAL OIL ADSORPTION FROM PALM OIL MILL EFFLUENT (POME) USING BOILER FLY ASH

2013 ◽  
Vol 12 (3) ◽  
pp. 417-427 ◽  
Author(s):  
Jude C. Igwe ◽  
Uche Arukwe ◽  
Stella N. Anioke
2018 ◽  
Vol 35 (3) ◽  
pp. 195
Author(s):  
J. Chibuzo Igwe ◽  
C. O. Onyegbado ◽  
Augustine Abia

Palm oil is one of the two most important vegetable oils in the world’s oil and fats market. The extraction and purification processes generate different kinds of waste generally known as palm oil mill effluent (POME). Earlier studies had indicated the possibility of using boiler fly ash to adsorb impurities and colour in POME treatment. The adsorption treatment of POME using boiler fly ash was further investigated in detail in this work with regards to the reduction of BOD, colour and TSS from palm oil mill effluent. The amount of BOD, colour and TSS adsorbed increased as the weight of the boiler fly ash used was increased. Also, the smallerparticle size of 425μm adsorbed more than the 850μm size. Attempts were made to fit the experimental data with the Freundlich, Langmuir and Dubinin-Radushkevich isotherms. The R2values, which ranged from 0.8974–0.9898, 0.8848–0.9824 and 0.6235–0.9101 for Freundlich, Langmuir and Dubinin-Radushkevich isotherms respectively, showed that Freundlich isotherm gave a better fit followed by Langmuir and then Dubinin-Radushkevich isotherm. The sorption trend could be put as BOD > Colour > TSS. The apparent energy of adsorption was found to be 1.25, 0.58 and 0.97 (KJ/mol) for BOD, colour and TSS respectively, showing that sorption process occurs by physiosorption. Therefore, boiler fly ash is capable of reducing BOD, Colour and TSS from POME and hence could be used to develop a good adsorbent for POME treatment.


2012 ◽  
Vol 43 (6) ◽  
pp. 934-941 ◽  
Author(s):  
Mohammad Amin Shavandi ◽  
Zahra Haddadian ◽  
Mohd Halim Shah Ismail ◽  
Norhafizah Abdullah

Fuel ◽  
2017 ◽  
Vol 195 ◽  
pp. 82-87 ◽  
Author(s):  
Saowakon Suwanno ◽  
Thanaphorn Rakkan ◽  
Tewan Yunu ◽  
Nisa Paichid ◽  
Pattarawadee Kimtun ◽  
...  

BioResources ◽  
2015 ◽  
Vol 10 (4) ◽  
Author(s):  
Wan Siti Shazzelyn Aida Wan Sharifudin ◽  
Alawi Sulaiman ◽  
Noriznan Mokhtar ◽  
Azhari Samsu Baharuddin ◽  
Meisam Tabatabaei ◽  
...  

2012 ◽  
Author(s):  
Bassim H. Hameed ◽  
Abdul Latif Ahmad ◽  
Ai Hoon Ng.

Pencemaran akibat dari minyak buangan yang terkandung dalam air sisa merupakan salah satu masalah persekitaran yang amat serius. Disebabkan oleh perkembangan industri kelapa sawit yang amat pesat di Malaysia, suatu isipadu air sisa dari kilang kelapa sawit (POME) yang banyak juga dihasilkan pada masa yang sama. Pengekstrakkan minyak buangan dari POME telah dijalankan menggunakan proses pengektrakan pelarut. Dalam kajian ini, kesan masa pengektrakan, nisbah pelarut/suapan dan kadar pencampuran pengektrakan menggunakan beberapa jenis pelarut telah dijalankan. N–pentana, n–hexana dan n–heptana telah digunakan sebagai pelarut. Peratus minyak yang diekstrakkan pada keadaan–keadaan optimum ujikaji menggunakan n–pentana, n–hexana dan n–heptana diperolehi masing–masing sebanyak 58, 63 dan 65 peratus. Pengekstrakan berbagai peringkat juga telah dijalankan. Lebih dari 97% minyak buangan yang terkandung dalam POME telah berjaya diekstrakkan pada peringkat keempat pengekstrakkan menggunakan pelarut–pelarut tersebut. Kata kunci: Pengekstrakkan; kadar pencampuran; masa pencampuran; pelarut; POME Pollution from residual oil content in the wastewater is one of the serious environmental problems. Due to the rapid development of the palm oil industry in Malaysia, a large volume of palm oil mill effluent (POME) has been produced at the same time. Removal of residual oil from POME was carried out using solvent extraction process. The effect of different solvents, extraction time, solvent/feed ratio and mixing rate on extraction efficiency were investigated throughout this work. N– pentane, n–hexane and n–heptane were used as solvents. The percent of oil extracted at the optimum conditions of 10 min extraction time, 1:1 solvent: feed ratio, 200 rpm using n–pentane, n–hexane and n–heptane were found to be 58, 63 and 65, respectively for a single stage extraction. Multistage extraction has shown that the % of oil extracted increased significantly to more than 97% of the residual oil in the POME. Key words: Extraction; mixing rate; mixing time; solvent; POME


2005 ◽  
Vol 22 (3) ◽  
pp. 371-379 ◽  
Author(s):  
A.L. Ahmad ◽  
S. Bhatia ◽  
N. Ibrahim ◽  
S. Sumathi

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