Anaerobic digestion of cattle manure after ultrasonic pretreatment under different conditions

Abstract

The ultrasonic pretreatment (UP) is one of the common pretreatment technologies applied in biogas production. In this study, UP was applied to cattle manure (CM) with different intensity and different intervals. The UP was applied to the intensity of 0.1, 0.5, 1.0, 3.0, 5.0 and 10.0 W/mL and respectively for each pretreatment intensity 5, 10, 20, 30 for 60 min. Biogas production was carried out in batch reactors under mesophilic conditions (30 ± 2 °C) and 5.0 % total solids (TS). As a result of the UP, soluble chemical oxygen demand removal increased from 41.0 % to maximum 67.0 %. The biogas production in this reactor was 270.6 mL/g TS. Thus, 59.0 % incremental biogas production was realized. In this reactor, cellulose and hemicellulose removal was 20.6 % and 16.9 %, respectively. The UP led to the dissolution of cellulose and hemicellulose molecules in water at the anaerobic digestion stage. The optimum times of 0.1, 0.5, 1.0, 3.0, 5.0 and 10.0 W/mL pretreatments were determined. All reactors successfully fitted to the modified Logistic model and the modified Von Bertalanffy model.

Keywords

• Biogas
• anaerobic digestion
• ultrasonic pretreatment
• modified Logistic Model
• modified Von Bertalanffy model.

Farklı koşullar altında ultrasonik ön işlemden sonra sığır gübresinin anaerobik sindirimi

Abstract

Ultrasonik ön arıtma (UP), biyogaz üretiminde uygulanan yaygın ön arıtma teknolojilerinden biridir. Bu çalışmada sığır gübresine (CM) farklı yoğunluk ve farklı aralıklarla UP uygulanmıştır. UP, 0.1, 0.5, 1.0, 3.0, 5.0 ve 10.0 W/mL'lik yoğunluğa ve sırasıyla her bir ön-muamele yoğunluğu için 5, 10, 20, 30 60 dakika boyunca uygulandı. Biyogaz üretimi, kesikli reaktörlerde mezofilik koşullar (30 ± 2 °C) ve % 5.0 toplam katı madde (TS) altında gerçekleştirilmiştir. UP'nin bir sonucu olarak, çözünür kimyasal oksijen ihtiyacının giderilmesi %41.0'dan maksimum %67.0'a yükseldi. Bu reaktördeki biyogaz üretimi 270.6 mL/g TS idi. Böylece %59,0 artımlı biyogaz üretimi gerçekleştirilmiştir. Bu reaktörde selüloz ve hemiselüloz giderimi sırasıyla %20,6 ve %16,9 olmuştur. UP, anaerobik sindirim aşamasında suda selüloz ve hemiselüloz moleküllerinin çözünmesine yol açtı. 0.1, 0.5, 1.0, 3.0, 5.0 ve 10.0 W/mL ön işlemlerin optimum süreleri belirlendi. Tüm reaktörler, değiştirilmiş Lojistik modeline ve değiştirilmiş Von Bertalanffy modeline başarıyla uydu.

Keywords

• biyogaz
• anaerobik çürütme
• ultrasonik ön arıtma
• modifiye Lojistik Model
• modifiye Von Bertalanffy modeli.

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