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通过启动液体再循环提高青贮饲料两相沼气发酵过程中的转化率和细菌活性。

Stimulation of conversion rates and bacterial activity in a silage-fed two-phase biogas process by initiating liquid recirculation.

作者信息

Jarvis A, Nordberg A, Mathisen B, Svensson B H

机构信息

Department of Microbiology, Swedish University of Agricultural Sciences, Uppsala.

出版信息

Antonie Van Leeuwenhoek. 1995 Nov;68(4):317-27. doi: 10.1007/BF00874142.

Abstract

The effects of liquid recirculation on a liquefaction-acidogenic reactor in an anaerobic two-phase digesting system operating with grass-clover silage was studied during 40 days after initiating recirculation of effluent from the methanogenic reactor to the liquefaction-acidogenic reactor. An increase in alkalinity and, thus, an increase in pH from 5.2 to 6.0 occurred in the liquefaction-acidogenic reactor. During the same period, a 10-fold increase (from 0.2 to 1.9 g.l-1.h-1) in the degradation rate of mannitol and an almost 9-fold increase in the activity of hydrogenotrophic methanogens was observed. The estimated number of these bacteria increased by one order of magnitude. The average degradation rate of lactate increased 3-fold, probably as a consequence of the more efficient hydrogen consumption by the hydrogenotrophic methanogens. An observed increase in net mineralization of organic nitrogen compounds was probably the main reason for an enhanced net production of organic acids (from 0.2 to 0.9 g.l-1.d-1). The liquefaction of cellulose and hemicellulose was low from the start of recirculation (3% and 20% reduction, respectively) and did not seem to be affected by the liquid recirculation. This was in accordance with the low number of cellulose degraders (4.0 x 10(2) counts.ml-1) observed. The results from this investigation show that the initiation of liquid recirculation in silage-fed two-phase biogas processes will stimulate the activity of hydrogenotrophic methanogens in the liquefaction-acidogenic reactor. This will lead to more thermodynamically favourable conditions for acidification reactions which are dependent upon interspecies transfer of reducing equivalents.

摘要

在将产甲烷反应器的出水回流至液化-产酸反应器40天期间,研究了液体循环对以三叶草青贮饲料为原料运行的厌氧两相消化系统中液化-产酸反应器的影响。液化-产酸反应器中碱度增加,pH值从5.2升至6.0。同一时期,观察到甘露醇降解率提高了10倍(从0.2克·升⁻¹·小时⁻¹增至1.9克·升⁻¹·小时⁻¹),氢营养型产甲烷菌的活性几乎提高了9倍。这些细菌的估计数量增加了一个数量级。乳酸的平均降解率提高了3倍,这可能是氢营养型产甲烷菌更有效地消耗氢气的结果。观察到的有机氮化合物净矿化增加可能是有机酸净产量提高(从0.2克·升⁻¹·天⁻¹增至0.9克·升⁻¹·天⁻¹)的主要原因。从回流开始,纤维素和半纤维素的液化率就很低(分别降低了3%和20%),似乎不受液体循环的影响。这与观察到的纤维素降解菌数量较少(4.0×10²个·毫升⁻¹)一致。本研究结果表明,在以青贮饲料为原料的两相沼气工艺中启动液体循环将刺激液化-产酸反应器中氢营养型产甲烷菌的活性。这将为依赖还原当量种间转移的酸化反应创造更有利于热力学的条件。

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