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首页> 外文期刊>Journal of Cleaner Production >Effect of reactor operating conditions on carboxylate production and chain elongation from co-fermented sludge and food waste
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Effect of reactor operating conditions on carboxylate production and chain elongation from co-fermented sludge and food waste

机译:反应器运行条件对共发酵污泥和食物垃圾羧酸盐生产和链伸长的影响

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Nowadays, fermentation of organic wastes for the production of carboxylic acids as precursors of higher value products has attracted significant attention. In this paper, sewage sludge and food waste were co fermented to produce carboxylic acids and study the subsequent chain elongation process. The Copenhagen waste stream scenario was taken as a case study. Firstly, design of experiments was used to investigate the overall carboxylic acids and hexanoic acid production in batch, as a function of the co fermentation ratio, substrate to co-culture ratio and initial pH. Optimal operating conditions for hexanoic acid were obtained with SS/FW 6.61, S/Xo 6.73 and initial pH 6.83. Statistical optimization increased the overall carboxylic acid titer by 41%, while co-fermentation allowed to increase hexanoate annual production up to 77%. Furthermore, a continuous fermentation experiment was performed to study the effect of reactor operating conditions. The overall carboxylates titer was 2 times higher, which also favored chain elongation compared to batch mode. An increasing loading rate did not affect the overall carboxylate titer, however the hexanoic acid titer increased by 44%. A maximum titer of 4.9 g/l of hexanoic acid was produced, achieving a productivity of 2.46 g/l/d of hexanoic acid with a retention time of 2 d and no external electron donor addition. This would correspond to 610 t/y of hexanoic acid and 350 t/y of other carboxylic acids that could be produced, based on the waste availability in Copenhagen. (c) 2021 Elsevier Ltd. All rights reserved.
机译:如今,作为羧酸生产的有机废物作为更高价值产品的前体的发酵引起了显着的关注。在本文中,污水污泥和食物废物是发酵,以生产羧酸并研究随后的链伸长率。哥本哈根废物流程是作为案例研究。首先,使用实验的设计来研究总羧酸和批次的己二酸产生,作为CO发酵比,基质与共培养比和初始pH的函数。用SS / FW 6.61,S / XO 6.73和初始pH6.83获得六丙酸的最佳操作条件。统计优化将整个羧酸滴度增加41%,而共发酵允许将己酸酯的年产量增加高达77%。此外,进行连续发酵实验以研究反应器操作条件的作用。总羧酸酯滴度比批量模式相比,也有利于链伸长率。增加的负载率不影响整体羧酸滴度,但六丙酸滴度增加了44%。产生4.9g / L的六烷基酸的最大滴度,达到2.46g / L / d的己酸的生产率,保留时间为2 d,没有外部电子给体添加。这将对应于610℃/次的己酸和其他羧酸的350吨/次,其可以根据哥本哈根的废物可用性生产。 (c)2021 elestvier有限公司保留所有权利。

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