两段式和一段式厌氧协同消化蔗渣和酿酒酵母废渣以生产生物氢和甲烷。

IF 2.5 4区 生物学 Q3 BIOCHEMISTRY & MOLECULAR BIOLOGY
Molecular Biotechnology Pub Date : 2025-09-01 Epub Date: 2024-01-17 DOI:10.1007/s12033-023-01015-3
Chatchawin Nualsri, Peer Mohamed Abdul, Tsuyoshi Imai, Alissara Reungsang, Sureewan Sittijunda
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引用次数: 0

摘要

本研究旨在评估两阶段和一阶段厌氧协同消化沼渣和废酿酒酵母细胞(SBY)以生产生物氢和甲烷的情况。研究了两阶段和一阶段生产过程中沼渣与酵母细胞的比例和粉煤灰浓度的优化。在两阶段工艺中,对蔗渣与 SBY 的比例和粉煤灰浓度进行了优化,并将剩余废水用于生产甲烷。生物制氢的最佳条件是蔗渣与 SBY 的比例为 7:3% v/w,粉煤灰浓度为 0.4% w/v,最大氢气产量为 43.7 ml-H2/g-VSadded。相比之下,蔗渣与 SBY 的比例为 10:0% v/w,粉煤灰浓度为 0.2% w/v,被认为是生产甲烷的最佳比例,最大甲烷产量为 214.6 ml-CH4/g-VSadded。在单阶段工艺中,蔗渣与 SBY 的比例为 10:0% v/w,粉煤灰浓度为 0.1% w/v,被认为是最理想的甲烷产生量,其最大甲烷产生量为 243.6 ml-CH4/g-VSadded。在两阶段工艺中,氢气(0.05-0.47 kJ/g-VSadded)的能量产率为 0.62%-11.78%,主要部分甲烷(3.19-7.73 kJ/g-VSadded)的收益约为 88.22%-99.38%。在单级工艺中,总能量产率分布范围为 4.20 至 8.77 kJ/g-VSadded。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Two-Stage and One-Stage Anaerobic Co-digestion of Vinasse and Spent Brewer Yeast Cells for Biohydrogen and Methane Production.

Two-Stage and One-Stage Anaerobic Co-digestion of Vinasse and Spent Brewer Yeast Cells for Biohydrogen and Methane Production.

This study aimed to evaluate the two-stage and one-stage anaerobic co-digestion of vinasse and spent brewer yeast cells (SBY) for biohydrogen and methane production. Optimization of the vinasse-to-SBY ratio and fly ash concentration of the two-stage and one-stage production processes was investigated. In the two-stage process, the vinasse-to-SBY ratio and fly ash concentration were optimized, and the leftover effluent was used for methane production. The optimum conditions for biohydrogen production were a vinasse-to-SBY ratio of 7:3% v/w and fly ash concentration of 0.4% w/v, in which the maximum hydrogen yield was 43.7 ml-H2/g-VSadded. In contrast, a vinasse-to-SBY ratio of 10:0% v/w and fly ash concentration of 0.2% w/v were considered optimal for methane production, and resulted in a maximum methane yield of 214.6 ml-CH4/g-VSadded. For the one-stage process, a vinasse-to-SBY ratio of 10:0% v/w and fly ash concentration of 0.1% w/v were considered optimal, and resulted in a maximum methane yield of 243.6 ml-CH4/g-VSadded. In the two-stage process, the energy yield from hydrogen (0.05-0.47 kJ/g-VSadded) was 0.62%-11.78%, and the major fraction was approximately 88.22%-99.38% gain from methane (3.19-7.73 kJ/g-VSadded). For the one-stage process, the total energy yield distribution ranged from 4.20 to 8.77 kJ/g-VSadded.

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来源期刊
Molecular Biotechnology
Molecular Biotechnology 医学-生化与分子生物学
CiteScore
4.10
自引率
3.80%
发文量
165
审稿时长
6 months
期刊介绍: Molecular Biotechnology publishes original research papers on the application of molecular biology to both basic and applied research in the field of biotechnology. Particular areas of interest include the following: stability and expression of cloned gene products, cell transformation, gene cloning systems and the production of recombinant proteins, protein purification and analysis, transgenic species, developmental biology, mutation analysis, the applications of DNA fingerprinting, RNA interference, and PCR technology, microarray technology, proteomics, mass spectrometry, bioinformatics, plant molecular biology, microbial genetics, gene probes and the diagnosis of disease, pharmaceutical and health care products, therapeutic agents, vaccines, gene targeting, gene therapy, stem cell technology and tissue engineering, antisense technology, protein engineering and enzyme technology, monoclonal antibodies, glycobiology and glycomics, and agricultural biotechnology.
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