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用于光合沼气升级的实验室规模鼓泡塔反应器的设计、调试及性能评估

Design, Commissioning, and Performance Assessment of a Lab-Scale Bubble Column Reactor for Photosynthetic Biogas Upgrading with .

作者信息

Bose Archishman, O'Shea Richard, Lin Richen, Murphy Jerry D

机构信息

Environmental Research Institute, MaREI Centre, University College Cork, Cork T23 XE10, Ireland.

School of Engineering, University College Cork, Cork T23 XE10, Ireland.

出版信息

Ind Eng Chem Res. 2021 Apr 21;60(15):5688-5704. doi: 10.1021/acs.iecr.0c05974. Epub 2021 Apr 8.

Abstract

The two-step bubble column-photobioreactor photosynthetic biogas upgrading system can enable simultaneous production of biomethane and value-added products from microalgae. However, due to the influence of a large number of variables, including downstream processes and the presence of microalgae, no unanimity has been reached regarding the performance of bubble column reactors in photosynthetic biogas upgrading. To investigate this further, the present work documents in detail, the design and commissioning of a lab-scale bubble column reactor capable of treating up to 16.3 L/h of biogas while being scalable. The performance of the bubble column was assessed at a pH of 9.35 with different algal densities of at 20 °C in the presence of light (3-5 klux or 40.5-67.5 μmol m s). A liquid/gas flow (L/G) ratio of 0.5 allowed consistent CO removal of over 98% irrespective of the algal density or its photosynthetic activity. For lower concentrations of algae, the volumetric O concentration in the upgraded biomethane varied between 0.05 and 0.52%, thus providing grid quality biomethane. However, for higher algal concentrations, increased oxygen content in the upgraded biomethane due to both enhanced O stripping and the photosynthetic activity of the microalgae as well as clogging and foaming posed severe operational challenges.

摘要

两步鼓泡塔-光生物反应器光合沼气升级系统能够同时从微藻中生产生物甲烷和增值产品。然而,由于包括下游工艺和微藻存在在内的大量变量的影响,关于鼓泡塔反应器在光合沼气升级中的性能尚未达成一致意见。为了进一步研究这一问题,本工作详细记录了一个实验室规模的鼓泡塔反应器的设计和调试情况,该反应器能够处理高达16.3升/小时的沼气,并且具有可扩展性。在20°C、光照(3-5千勒克斯或40.5-67.5微摩尔·米²·秒⁻¹)条件下,在pH值为9.35、不同藻类密度的情况下对鼓泡塔的性能进行了评估。液/气流量(L/G)比为0.5时,无论藻类密度或其光合活性如何,均可实现超过98%的一致CO去除率。对于较低浓度的藻类,升级后生物甲烷中的体积O浓度在0.05%至0.52%之间变化,从而提供电网质量的生物甲烷。然而,对于较高的藻类浓度,由于O汽提增强、微藻的光合活性以及堵塞和起泡,升级后生物甲烷中的氧气含量增加,带来了严峻的操作挑战。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/8a2d/8277169/bd1b13ffd16b/ie0c05974_0002.jpg

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