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首页> 外文期刊>Bioresource Technology: Biomass, Bioenergy, Biowastes, Conversion Technologies, Biotransformations, Production Technologies >Effects of solid-liquid separation on recovering residual methane and nitrogen from digested dairy cow manure
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Effects of solid-liquid separation on recovering residual methane and nitrogen from digested dairy cow manure

机译:固液分离对消化的奶牛粪便中残留甲烷和氮的回收作用

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The feasibility of optimizing methane and nitrogen recovery of samples obtained from farm biogas digester (35 degrees C) and post-storage tank (where digested material is stored for 9-12 months) was studied by separating the materials into different fractions using 2, 1, 0.5 and 0.25 mm sieves. Mass-balances revealed that digested material mainly consists of <0.25 mm (60-69%) and >2 mm (18-27%) fractions, while fractions between 2 and 0.25 mm made the rest. Incubation of solid fractions >0.25 mm of digester material at 35 degrees C resulted in specific methane yields of 0.060-0.085 m(3) kg(-1) volatile solids (VS) during initial 30-50 d and 0.16-0.18 m(3) kg(-1) VS at the end of 340 d incubation. Similarly, fractions >0.25 mm. of post-storage tank material produced 0.055-0.092 m(3) kg(-1) VS and 0.13-0.16 m(3) kg(-1) VS of methane after 30-50 d and after 250 d, respectively. Methane yields for fractions <0.25 mm of post-storage tank was 0.03 m(3) kg(-1) VS after 30-50 d and 0.05 m(3) kg(-1) VS after 250 d compared to 0.20 m(3) kg(-1) VS and 0.41 m(3) kg(-1) VS, respectively for the same fraction of digester material. Separation of digested cow manure into solids and liquid fractions to recover methane may be feasible only for post-storage tank material and not for digester material. Nitrogen management would not be feasible with neither material as total nitrogen and ammonium-nitrogen concentrations were equally distributed among the segregated fractions. (C) 2006 Elsevier Ltd. All rights reserved.
机译:通过使用2、1将物料分离成不同的馏分,研究了优化从农场沼气池(35摄氏度)和后储罐(消化后的物料存储9-12个月)中获得的样品的甲烷和氮气回收率的可行性。 ,0.5和0.25毫米的筛子。质量平衡表明,消化后的物质主要由<0.25 mm(60-69%)和> 2 mm(18-27%)的馏分组成,而介于2和0.25 mm之间的馏分则构成了其余部分。在35摄氏度下将大于0.25 mm的蒸煮器物料的固体馏分温育,在最初的30-50 d和0.16-0.18 m(3)期间的比甲烷产量为0.060-0.085 m(3)kg(-1)挥发性固体(VS) 340 d孵化结束时)kg(-1)VS。同样,分数> 0.25 mm。 30-50 d和250 d后,分别储存的储罐材料分别产生0.055-0.092 m(3)kg(-1)VS和0.13-0.16 m(3)kg(-1)VS的甲烷。储存后储罐<0.25 mm的馏分的甲烷产率为30-50 d后为0.03 m(3)kg(-1)VS和250 d后为0.05 m(3)kg(-1)VS,而0.20 m(3 )kg(-1)VS和0.41 m(3)kg(-1)VS,分别用于相同比例的消化器材料。将消化后的牛粪分离成固体和液体部分以回收甲烷可能仅对储罐后的物料可行,对消化器的物料则不可行。使用这两种材料进行氮管理都是不可行的,因为总氮和铵氮浓度在分离的馏分之间平均分配。 (C)2006 Elsevier Ltd.保留所有权利。

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