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稳定的嗜热厌氧消化法通过与猪粪共消化来处理溶气浮选(DAF)污泥。

Stable thermophilic anaerobic digestion of dissolved air flotation (DAF) sludge by co-digestion with swine manure.

机构信息

Novozymes North America, 77 Perrys Chapel Church Road, Franklinton, NC 27525, USA.

出版信息

Bioresour Technol. 2010 May;101(9):3020-4. doi: 10.1016/j.biortech.2009.12.029. Epub 2010 Jan 8.

Abstract

Environmentally sound treatment of by-products in a value-adding process is an ongoing challenge in animal agriculture. The sludge produced as a result of the dissolved air flotation (DAF) wastewater treatment process in swine processing facilities is one such low-value residue. The objective of this study was to determine the fundamental performance parameters for thermophilic anaerobic digestion of DAF sludge. Testing in a semi-continuous stirred tank reactor and in batch reactors was conducted to determine the kinetics of degradation and biogas yield. Stable operation could not be achieved using pure DAF sludge as a substrate, possibly due to inhibition by long-chain fatty acids or to nutrient deficiencies. However, in a 1:1 ratio (w/w, dry basis) with swine manure, operation was both stable and productive. In the semi-continuous stirred reactor at 54.5 degrees Celsius, a hydraulic residence time of 10 days, and an organic loading rate of 4.68 gVS/day/L, the methane production rate was 2.19 L/L/day and the specific methane production rate was 0.47 L/gVS (fed). Maximum specific methanogenic activity (SMA) in batch testing was 0.15 mmoles CH(4) h(-1) gVS(-1) at a substrate concentration of 6.9 gVS L(-1). Higher substrate concentrations cause an initial lag in methane production, possibly due to long-chain fatty acid or nitrogen inhibition.

摘要

在增值过程中对副产品进行环境无害化处理是动物养殖业面临的持续挑战。在猪加工设施的溶气浮选(DAF)废水处理过程中产生的污泥就是这样一种低价值残留物。本研究的目的是确定高温厌氧消化 DAF 污泥的基本性能参数。通过半连续搅拌槽式反应器和分批式反应器进行测试,以确定降解动力学和沼气产率。由于长链脂肪酸的抑制或营养物质的缺乏,可能无法使用纯 DAF 污泥作为底物来实现稳定运行。然而,在与猪粪以 1:1 的比例(w/w,干基)混合时,运行既稳定又具有生产力。在 54.5°C 的半连续搅拌式反应器中,水力停留时间为 10 天,有机负荷率为 4.68 gVS/天/L,甲烷生成率为 2.19 L/L/天,特定甲烷生成率为 0.47 L/gVS(进料)。在批量测试中,最大比甲烷生成活性(SMA)在底物浓度为 6.9 gVS/L 时达到 0.15 毫摩尔 CH(4) h(-1) gVS(-1)。较高的底物浓度会导致甲烷生成的初始滞后,这可能是由于长链脂肪酸或氮抑制所致。

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