文章摘要
王 星,刘惠萍,周 俊,罗伟中.鸭粪厌氧消化过程的质能平衡研究[J].农业环境科学学报,2013,32(9):1886-1892.
鸭粪厌氧消化过程的质能平衡研究
The Mass and Energy Balance Research on the Anaerobic Digestion of Duck Droppings
  
DOI:10.11654/jaes.2013.09.026
中文关键词: 鸭粪  厌氧消化  质能平衡
英文关键词: duck droppings  anaerobic digestion  mass and energy balance
基金项目:
作者单位
王 星 上海齐耀动力技术有限公司 
刘惠萍 上海市发展改革研究院 
周 俊 上海齐耀动力技术有限公司 
罗伟中 上海齐耀动力技术有限公司 
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中文摘要:
      以鸭粪为原料,利用小型厌氧装置开展了厌氧消化工艺的实验研究。实验建立了3个进料浓度梯度,通过逐步提高进料料浆的浓度,研究了在不同进料负荷率情况下,厌氧消化系统的变化趋势,分析了进料负荷率与挥发性脂肪酸、总碱度、氨氮浓度的变化关系。通过建立质量平衡模型发现,当进料负荷率在4.17、8.33、12.5 kg TS·m-3·d-1时,单位TS产气率分别为0.34、0.26、0.19 m3·kg-1 TS,对应的一级反应动力学常数k值分别为0.29、0.17、0.06 d-1,鸭粪理论TS产气率为0.44 m3·kg-1 TS。经过对进料、出料热值的分析,当有机负荷率为8.33 kg TS·m-3·d-1,进入厌氧系统的鸭粪有45.36%转变为甲烷、47.05%转变为残余物、7.6%转化为热量散失(或被微生物自身利用)。研究认为当单位TS产气率达到理论TS产气率的60%~70%时,此时的停留时间、进料负荷是最为经济的,这一原则适合普通厌氧消化工程的设计及运行。
英文摘要:
      To investigate the fermentation features of duck droppings at different loading rates, a lab scale fermentation process for the anaerobic treatment of duck droppings was carried out with an integrated bio-reacor. The experiment set up three step-wisely increased loading rates. The effects of volatile fatty acid ,total alkalinity, ammonia nitrogen, retention time and loading rates on fermentation process were studied. With the mass balance equations, a theoretical yield of biogas(0.44 m3·kg-1 TS) was achieved. At steady state, the yields of biogas were found to be 0.29 d-1, 0.17 d-1, 0.06 d-1, values for first order kinetics were obtained as 0.29 d-1、0.17 d-1、0.06 d-1 when loading rates were set at 4.17 kg TS·m-3·d-1(TS=5%), 8.33 kg TS·m-3·d-1(TS=10%), 12.5 kg TS·m-3·d-1(TS=15%), respectively. According to the energy value analysis, 45.36% heat value from duck droppings were converted to methane, 47.05% to residues and 7.6% were lost as waste heat when loading rate was set at 8.33 kg TS·m-3·d-1. The research shows that the optimal loading rate and retention time can be obtained when biogas yield is equivalent to 60%~70% of the theoretical biogas yield. The present research achievements can apply for dimensioning completely stirred tank reactors digestion organic wastes from food processing industries, animal waste slurries or biogas crops.
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