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首页> 外文期刊>Indian Journal of Chemical Technology >Application of cement kiln dust enhancing methane production using upflow anaerobic sludge blanket reactor for the treatment of palm oil mill effluent
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Application of cement kiln dust enhancing methane production using upflow anaerobic sludge blanket reactor for the treatment of palm oil mill effluent

机译:上流式厌氧污泥床反应器在水泥窑除尘增产甲烷中的应用

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摘要

Anaerobic digestion of palm oil mill effluent (POME) for continuous biogas production has been carried out in an upflow anaerobic sludge blanket reactor (UASBR) using cement kiln dust (CKD). POME is used as the substrate carbon source and CKD as a neutralizing agent. The effects of the hydrualic retention time (HRT) 20 h and organic loading rate (OLR) 4.5 kg COD/m(3)h(-1) over 95% COD removal and 0.89 mL CH4/L/h with a methane yield of 0.65 L CH4/g CODremoved at 1600 mg/L CKD in UASBR have been studied. Without CKD (control) the reactor for the removal of COD only 10.5% and methane production up to 0.13 L CH4/g COD. However, increasing the OLR to 4.5 kgCOD/m(3)h(-1) by reducing the hydraulic retention time (HRT 6 h) reduced the COD removal efficiency to 58% and methane production up to 0.43 L CH4/g CODremoved. Considering this, the use of CKD containing UASBR might be practically and economically attractive for industrial scale biogas production and sludge reduction from industrial wastes and wastewater.
机译:已在上流式厌氧污泥床反应器(UASBR)中使用水泥窑粉尘(CKD)对棕榈油厂废水(POME)进行厌氧消化以连续生产沼气。 POME用作底物碳源,CKD用作中和剂。水合保留时间(HRT)20小时和有机物负载率(OLR)4.5 kg COD / m(3)h(-1)超过95%COD去除和0.89 mL CH4 / L / h的影响,甲烷产率为研究了在UASBR中以1600 mg / L CKD去除的0.65 L CH4 / g COD。如果没有CKD(对照),反应器的COD去除率仅为10.5%,甲烷生成量高达0.13 L CH4 / g COD。但是,通过减少水力停留时间(HRT 6小时)将OLR增加到4.5 kgCOD / m(3)h(-1),可将COD去除效率降至58%,并将甲烷生成量提高至0.43 L CH4 / g COD。考虑到这一点,对于工业规模的沼气生产以及减少工业废物和废水产生的污泥,使用含CKD的UASBR可能在经济上具有吸引力。

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