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Biogas production from marine macroalgae: Macronutrient demand in experimental seawater anaerobic bioreactors.

机译:海洋大型藻类产生的沼气:海水厌氧生物反应器中对大量营养素的需求。

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摘要

During the last few decades, the anaerobic digestion (AD) process has become a worldwide topic of interest since it is considered as one of the most suitable and cost-effective technologies to address the problem of wastewater treatment while generating bioenergy. Until today, the use of seawater in the operations of anaerobic digestion processes for biogas production was unfamiliar to the scientific community. In this research, we proposed to investigate the dynamics and performance of two multi-stage bench-scale anaerobic bioreactors (MSBSABs), operated under high salinity conditions (an intermediate salinity of 1.0% w/w as a control system, and a high salinity of 3.5% w/w as an experimental system). Both bioreactors were fed with the marine macroalgae, Sargassum spp., as energy biomass during an 18-week period of operations. The elemental composition of this energy biomass (dry sargassum) was lower than other fresh marine biomasses used in AD process. This was expected since the sargassum feedstock used in our study was harvested onshore and was already dried by the sun (beach wrack blend). The reduction of the volatile solids (VS) content within the control system was greater in the third chamber S3 (6.30+/- 1.79 g/100ml) than the VS content of the first chamber S1 (9.03+/- 2.83 g/100ml). A similar pattern was observed in the experimental system, which VS content was 6.90+/- 2.39 g/100ml in S3, compared to 10.25+/- 2.65 g/100ml in S1. A significant reduction of the mass fraction of macronutrients (C, H & N) was observed in both systems from the first chamber S1 to the last chamber S3. Nevertheless, the sulfur fraction of the third chamber S3 was higher in both bioreactors when comparing to that measured in S1. The biogas production was 30% greater in the control system (1.0% w/w) than the experimental system (3.5% w/w). The biogas yield averaged over time was a normalized rate of 91.05 ml of biogas per gram of VS fed per day in the experimental system, compared to a volumetric production of 132.42 ml of biogas per gram of VS fed per day in the control system. The biogas samples of both bioreactors presented a similar chemical composition to that reported for traditional freshwater anaerobic biodigesters. However, the biogas samples of the experimental bioreactor were of better quality in terms of methane concentration than the control bioreactor (with a methane percentage around 61.28+/- 1.70 for the experimental bioreactor, and 53.82+/- 5.10 for the control bioreactor).
机译:在过去的几十年中,厌氧消化(AD)工艺已成为全球关注的话题,因为它被认为是解决废水处理问题同时产生生物能的最合适,最具成本效益的技术之一。直到今天,科学界还不熟悉在厌氧消化过程中用于生产沼气的海水的使用。在这项研究中,我们建议研究在高盐度条件下(作为控制系统的中度盐度为1.0%w / w)和高盐度下运行的两个多级台式厌氧生物反应器(MSBSAB)的动力学和性能。重量为3.5%w / w(作为实验系统)。在18个星期的运行期间,两个生物反应器都被喂食了海洋大型藻类Sargassum spp。作为能源生物质。这种能量生物质(海藻干)的元素组成低于AD过程中使用的其他新鲜海洋生物质。这是预料之中的,因为在我们的研究中使用的马尾藻原料是在陆上收获的,并且已经被太阳晒干了(海滩残骸混合物)。在第三腔室S3(6.30 +/- 1.79 g / 100ml)中,控制系统中挥发性固体(VS)含量的减少大于第一腔室S1中的VS含量(9.03 +/- 2.83 g / 100ml) 。在实验系统中观察到了类似的模式,S3中的VS含量为6.90 +/- 2.39 g / 100ml,而S1中的VS含量为10.25 +/- 2.65 g / 100ml。从第一个腔室S1到最后一个腔室S3,在两个系统中都观察到大量营养素(C,H和N)的质量分数显着降低。然而,与在S1中测得的硫含量相比,两个生物反应器中第三室S3的硫含量都更高。对照系统(1.0%w / w)的沼气产量比实验系统(3.5%w / w)高30%。在实验系统中,随时间推移平均产生的沼气的标准化速率为每天每克VS饲喂91.05 ml沼气,相比之下,对照系统中每天每克VS饲喂132.42 ml沼气。两种生物反应器的沼气样品都具有与传统淡水厌氧生物消化器报告的化学成分相似的化学成分。但是,就甲烷浓度而言,实验生物反应器的沼气样品质量要比对照生物反应器好(实验生物反应器的甲烷百分比约为61.28 +/- 1.70,对照生物反应器的甲烷百分比约为53.82 +/- 5.10)。

著录项

  • 作者

    Forestil, Antonin.;

  • 作者单位

    University of Puerto Rico, Rio Piedras (Puerto Rico).;

  • 授予单位 University of Puerto Rico, Rio Piedras (Puerto Rico).;
  • 学科 Environmental science.;Sustainability.;Energy.
  • 学位 M.S.
  • 年度 2015
  • 页码 104 p.
  • 总页数 104
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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