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采用棕榈油厂废水对失衡的全规模沼气反应器进行进料恢复的策略。

Strategies for recovery of imbalanced full-scale biogas reactor feeding with palm oil mill effluent.

作者信息

Wongfaed Nantharat, Kongjan Prawit, Suksong Wantanasak, Prasertsan Poonsuk, O-Thong Sompong

机构信息

Biotechnology Program, Faculty of Science, Thaksin University, Phatthalung, Thailand.

Department of Science, Faculty of Science and Technology, Prince of Songkla University, Pattani, Thailand.

出版信息

PeerJ. 2021 Jan 7;9:e10592. doi: 10.7717/peerj.10592. eCollection 2021.

Abstract

BACKGROUND

Full-scale biogas production from palm oil mill effluent (POME) was inhibited by low pH and highly volatile fatty acid (VFA) accumulation. Three strategies were investigated for recovering the anaerobic digestion (AD) imbalance on biogas production, namely the dilution method (tap water vs. biogas effluent), pH adjustment method (NaOH, NaHCO, Ca(OH), oil palm ash), and bioaugmentation (active methane-producing sludge) method. The highly economical and feasible method was selected and validated in a full-scale application.

RESULTS

The inhibited sludge from a full-scale biogas reactor could be recovered within 30-36 days by employing various strategies. Dilution of the inhibited sludge with biogas effluent at a ratio of 8:2, pH adjustment with 0.14% w/v NaOH, and 8.0% w/v oil palm ash were considered to be more economically feasible than other strategies tested (dilution with tap water, or pH adjustment with 0.50% w/v Ca(OH), or 1.25% NaHCO and bioaugmentation) with a recovery time of 30-36 days. The recovered biogas reactor exhibited a 35-83% higher methane yield than self-recovery, with a significantly increased hydrolysis constant (k) and specific methanogenic activity (SMA). The population of sp., sp., and sp. increased in the recovered sludge. The imbalanced full-scale hybrid cover lagoon reactor was recovered within 15 days by dilution with biogas effluent at a ratio of 8:2 and a better result than the lab-scale test (36 days).

CONCLUSION

Dilution of the inhibited sludge with biogas effluent could recover the imbalance of the full-scale POME-biogas reactor with economically feasible and high biogas production performance.

摘要

背景

低pH值和高挥发性脂肪酸(VFA)积累抑制了棕榈油厂废水(POME)的全规模沼气生产。研究了三种恢复沼气生产中厌氧消化(AD)失衡的策略,即稀释法(自来水与沼液)、pH调节法(NaOH、NaHCO₃、Ca(OH)₂、油棕灰)和生物强化(活性产甲烷污泥)法。选择了经济高效且可行的方法并在全规模应用中进行了验证。

结果

采用各种策略可在30 - 36天内恢复全规模沼气反应器中受抑制的污泥。用沼液以8:2的比例稀释受抑制的污泥、用0.14% w/v的NaOH调节pH值以及用8.0% w/v的油棕灰被认为比其他测试策略(用自来水稀释,或用0.50% w/v的Ca(OH)₂或1.25%的NaHCO₃调节pH值以及生物强化)更具经济可行性,恢复时间为30 - 36天。恢复后的沼气反应器甲烷产量比自我恢复高35 - 83%,水解常数(k)和比产甲烷活性(SMA)显著增加。恢复后的污泥中,[具体菌种1]、[具体菌种2]和[具体菌种3]的数量增加。通过以8:2的比例用沼液稀释,不平衡的全规模混合覆盖泻湖反应器在15天内恢复,且结果优于实验室规模试验(36天)。

结论

用沼液稀释受抑制的污泥可以恢复全规模POME - 沼气反应器的失衡,具有经济可行性和高沼气生产性能。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/b5f2/7797170/c96cf0d09a19/peerj-09-10592-g001.jpg

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