Advanced Treatment of Palm Oil Mill Effluent Using Thermally Activated Persulfate Oxidation

被引:7
作者
Bashir, Mohammed J. K. [1 ]
Sheen, Ong Sue [1 ]
Ng, Choon Aun [1 ]
Abujazar, Mohammed Shadi S. [2 ]
Alazaiza, Motasem Y. D. [3 ]
Abu Amr, Salim S. [4 ]
机构
[1] Univ Tunku Abdul Rahman, Fac Engn & Green Technol FEGT, Dept Environm Engn, Kampar 31900, Perak, Malaysia
[2] Al Aqsa Univ, Al Aqsa Community Intermediate Coll, PB 4051, Gaza, Palestine
[3] ASharqiyah Univ ASU, Coll Engn, Dept Civil & Environm Engn, Ibra 400, Oman
[4] Int Coll Engn & Management, Hlth Safety & Environm Management, Seeb 111, Oman
关键词
sulfate radical; advanced oxidation process; thermos-activation; treatment optimization; organic pollutants; OPTIMIZATION; DEGRADATION; REMOVAL; POME;
D O I
10.3390/separations9070171
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
Advanced treatment of biologically processed palm oil mill effluent (BIOTPOME), which possesses a potential danger to the water sources is required to meet the Malaysian discharge standard, as BIOTPOME contains high level of chemical oxygen demand (COD), suspended solids and oil and grease even after going through conventional treatment process. The significant but insufficient treatment efficiency of ponding system in Malaysia urged an alternative method to treat the recalcitrant organic compounds. Thus, post-treatment of BIOTPOME using oxidation by thermally activated persulfate process was proposed to solve this issue. In order to maximize the removal of COD and color, the central composite design (CCD) module of the response surface approach was used to optimize the interactions of the process variables temperature, S2O82-/COD ratio, and reaction time. In order to identify the significant terms of interacting process factors, CCD performed a batch study from which statistical models of responses were created. All models were confirmed by analysis of variance (ANOVA) showing significances with Prob > F less than 0.1. The optimal performance was obtained at the temperature of 67.4 degrees C, S2O82-/COD ratio of 9.8 and reaction time of 120 min, rendering COD removal of 85.65% and color removal of 85.74%. The total cost for the treatment process was RM0.94 per liter.
引用
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页数:12
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