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Kinetic Modeling of Dry Anaerobic Co-Digestion of Lignocellulosic Biomass

机译:木质纤维素生物质干厌氧消化的动力学模型

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Anaerobic digestion is a widely used conversion process for recovering energy from bio degradable waste materials. Dry anaerobic co-digestion of lignocellulosic biomass such as rice straw (RS) with cow dung (CD) offers various benefits other than mono digestion or liquid state anaerobic digestion. However dry anaerobic co-digestion of lignocellulosic biomass has restrictions due to low moisture content and retarded mass transfer within the mixture of substrates which contains in the reactor. Three consecutive batch experiments (E1, E-2, and E-3) were conducted by reusing solid digestate of E1 as an inoculum to E-2 and solid digestate of E-2 as an inoculum for E-3 in lab scale reactors using RS and CD as substrates. In E-1, CD was the only inoculum and it acted as a substrate as well. Total solids (TS) content of the substrate mixtures of E-1, E-2 and E-3 were 15%, 16%, and 20% respectively. Then mathematical modeling was applied to estimate kinetic parameters related to dry anaerobic co-digestion process using the modified Gompertz model for the three experiments. Modified Gompertz model very closely predicted the ultimate methane yield (Mmax) with R2 almost 0.99 in each scenario. Degradation kinetics improved drastically with the strategy of reusing of digestate, as for the E-2 the lag phase period (λ) reduced from 14 days to almost zero. Ultimate methane yield increased by 104% through this approach. Degradation kinetics were negatively affected with the increase of TS% within the substrate mixture even though digestate was reused as an inoculum. In E-3 ultimate methane yield was 138 ml/g volatile solids (VS) which was a 38% reduction compared to E-2, even though digestate was used as the main inoculum source for the both experiments. But it was a 27% increase compared to E-1 which CD was used as the only inoculum.
机译:厌氧消化是一种广泛使用的转化过程,用于从可生物降解的废料中回收能量。木质纤维素生物质(如稻草(RS)和牛粪(CD))的干式厌氧共消化除了单消化或液态厌氧消化外,还具有多种优势。然而,木质纤维素生物质的干厌氧共消化由于水分含量低和反应器中包含的底物混合物内的传质受阻而受到限制。在实验室规模的反应器中,通过将E1的固体消化物作为接种物重用到E-2以及E-2的固体消化物作为E-3的接种物,在实验室规模的反应器中进行了三个连续的批处理实验(E1,E-2和E-3) RS和CD作为底物。在E-1中,CD是唯一的接种物,它也可以作为底物。 E-1,E-2和E-3的底物混合物的总固体(TS)含量分别为15%,16%和20%。然后,使用改进的Gompertz模型对这三个实验进行数学建模,以估算与干式厌氧消化过程有关的动力学参数。修正的Gompertz模型非常紧密地预测了最终甲烷产量(M max )与R 2 在每种情况下几乎为0.99。降解动力学随着酶消化物的再利用而得到了极大的改善,因为E-2的滞后期(λ)从14天减少到几乎为零。通过这种方法,最终甲烷产量提高了104%。即使将消化物重新用作接种物,降解动力学也会因底物混合物中TS%的增加而受到负面影响。在E-3中,最终的甲烷产量为138 ml / g挥发性固体(VS),与E-2相比降低了38%,尽管在两个实验中消化液均被用作主要接种物。但是与CD被用作唯一接种物的E-1相比,它增加了27%。

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