The excessive mineralization of organic molecules during anaerobic fermentation increases the availability of nitrogen and carbon. For this reason, the development of downstream processing technologies is required to better manage ammonia and carbon dioxide emissions during the storage and land application of the resulting soil organic amendment. The present work investigated classical distillation as a technology for valorizing ammoniacal nitrogen (NH-N) in anaerobic digestate. The results implied that the direct isolation of ammonium bicarbonate (NHHCO) was possible when applying the reactive distillation to the food waste digestate (FWD) with a high content of NH-N, while the addition of antifoam to the agrowaste digestate (AWD) was necessary to be able to produce an aqueous solution of NHHCO as the distillate. The reason was that the extraction of NHHCO from the AWD required a higher temperature (>95 °C) and duration (i.e., steady state in batch operation) than the recovery of the inorganic fertilizer from the FWD. The titration method, when applied to the depleted digestate, offered the quickest way of monitoring the reactive distillation because the buffer capacity of the distillate was much higher. The isolation of NHHCO from the FWD was attained in a transient mode at a temperature below 90 °C (i.e., while heating up to reach the desired distillation temperature or cooling down once the batch distillation was finished). For the operating conditions to be regarded as techno-economically feasible, they should be attained in the anaerobic digestion plant by integrating the heat harvested from the engines, which convert the biogas into electricity.
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http://dx.doi.org/10.3390/bioengineering11111152 | DOI Listing |
BioTech (Basel)
December 2024
Department of Environmental Science and Engineering, Feng Chia University, Taichung City 40724, Taiwan.
Sorghum distillers grains (SDGs) produced from a sorghum liquor company were used for generating biohydrogen via dark fermentation at pH 4.5-6.5 and 55 °C with a batch test, and the biohydrogen electricity generation potential was evaluated.
View Article and Find Full Text PDFJ Chromatogr A
January 2025
Department of Process and Life Science Engineering, Lund University, Box 124, 221 00 Lund, Sweden.
The production of biopharmaceuticals is a chemical- and water-intensive process. The consumption of water and chemicals is partly due to the need for many different buffers in large volumes during the downstream process, typically consisting of several chromatography steps. Given the global commitment to the goals for sustainable development and the anticipated growth of the biopharmaceutical market, the consumption of large buffer volumes is expected to become problematic.
View Article and Find Full Text PDFBioengineering (Basel)
November 2024
Department of Chemical and Biomolecular Engineering, Lehigh University, B336 Iacocca Hall, 111 Research Drive, Bethlehem, PA 18015, USA.
The excessive mineralization of organic molecules during anaerobic fermentation increases the availability of nitrogen and carbon. For this reason, the development of downstream processing technologies is required to better manage ammonia and carbon dioxide emissions during the storage and land application of the resulting soil organic amendment. The present work investigated classical distillation as a technology for valorizing ammoniacal nitrogen (NH-N) in anaerobic digestate.
View Article and Find Full Text PDFSci Adv
November 2024
Department of Medicine, University of Chicago, Chicago, IL, USA.
Artificial intelligence models have been increasingly used in the analysis of tumor histology to perform tasks ranging from routine classification to identification of molecular features. These approaches distill cancer histologic images into high-level features, which are used in predictions, but understanding the biologic meaning of such features remains challenging. We present and validate a custom generative adversarial network-HistoXGAN-capable of reconstructing representative histology using feature vectors produced by common feature extractors.
View Article and Find Full Text PDFBioprocess Biosyst Eng
November 2024
School of Biological Sciences, Universiti Sains Malaysia, 11800 USM, Pulau Pinang, Malaysia.
The study focused on rhamnolipid production by batch fermentation of Pseudomonas aeruginosa USM-AR2 in a 3-L stirred-tank reactor (STR) using palm sludge oil (PSO) as the sole carbon source. The impact of various agitation rates towards the dispersion of PSO in the medium was evaluated to improve biomass growth and rhamnolipid production. A mechanical foam collection and recycling system was designed and retrofitted to the STR to overcome severe foam formation during fermentation.
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