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在中试规模气升式环流反应器中培养微藻的可行性。

Feasibility of microalgal cultivation in a pilot-scale airlift-driven raceway reactor.

机构信息

Civil Engineering Department, New Mexico State University, Las Cruces, NM 88002, USA.

出版信息

Bioresour Technol. 2012 Mar;108:196-202. doi: 10.1016/j.biortech.2011.12.146. Epub 2012 Jan 8.

Abstract

A Scenedesmus sp. was cultivated in a 23-L airlift-driven raceway reactor under artificial lighting and laboratory conditions, in batch and continuous modes. In batch mode, a maximum volumetric biomass productivity of 0.085 dry g L(-1) day(-1) was achieved under sparging at a CO(2)-to-air ratio of 1%, and a maximum CO(2) utilization efficiency of 33% was achieved at a CO(2)-to-air ratio of 0.25%. In continuous mode, the maximum volumetric biomass productivity was 0.19 dry g L(-1) day(-1). Biomass productivities per unit power input achieved in this reactor configuration (0.60-0.69 dry g W(-1) day(-1)) were comparable to or better than those reported in the literature for different photobioreactor designs (0.10-0.51 dry g W(-1) day(-1)). Based on the energy-efficient productivity and the high CO(2) utilization efficiency demonstrated in this study, the proposed airlift-driven raceway design holds promise for cost-effective algal cultivation.

摘要

在人工照明和实验室条件下,以间歇式和连续式培养方式,在 23 升气升式环流反应器中培养了一株栅藻。在间歇式培养条件下,以 CO2 与空气的比例为 1%进行鼓泡时,最大比体积生物质生产率达到 0.085 干克每升每天,而当 CO2 与空气的比例为 0.25%时,最大 CO2 利用率达到 33%。在连续式培养条件下,最大比体积生物质生产率达到 0.19 干克每升每天。与不同光生物反应器设计(0.10-0.51 干克每瓦每天)的文献报道相比,该反应器构型下单位功率输入的生物质生产率(0.60-0.69 干克每瓦每天)可与之媲美或优于其水平。基于本研究中展示的高效节能生产力和高 CO2 利用率,所提出的气升式环流跑道设计有望实现具有成本效益的藻类培养。

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