11 research outputs found

    Comparison of different machine learning algorithms to estimate liquid level for bioreactor management

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    Estimating the liquid level in an anaerobic digester can be disturbed by its closedness, bubbles and scum formation, and the inhomogeneity of the digestate. In our previous study, a soft-sensor approach using seven pressure meters has been proposed as an alternative for real-time liquid level estimation. Here, machine learning techniques were used to improve the estimation accuracy and optimize the number of sensors required in this approach. Four algorithms, multiple linear regression (MLR), artificial neural network (ANN), random forest (RF), and support vector machine (SVM) with radial basis function kernel were compared for this purpose. All models outperformed the cubic model developed in the previous study, among which the ANN and RF models performed the best. Variable importance analysis suggested that the pressure readings from the top (in the headspace) were the most significant, while the other pressure meters showed varying significance levels depending on the model type. The sensor that experienced both headspace and liquid phases depending on the level variation incurred a higher error than other sensors. The results showed that the ML techniques can provide an effective tool to estimate digester liquid levels by optimizing the number of sensors and reducing the error rate

    ์œ ์šฉ๋ฏธ์ƒ๋ฌผ์„ ํ™œ์šฉํ•œ ์•„์กฐ์—ผ๋ฃŒ์˜ ์ƒ๋ถ„ํ•ด ๋ฐ ์ „์‚ฌ์ฒด ๋ถ„์„์„ ํ†ตํ•œ ๋ถ„ํ•ด๊ฒฝ๋กœ ํƒ์ƒ‰

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    The goal of this study was to select the most appropriate microbial consortium for efficient bioremediation of azo dye wastewater. A consortium composed of two bacterial cultures (Mesorhizobium sp. and Sphingomonas melonis) and two yeast cultures (Apiotrichum mycotoxinivarans and Meyerozyma guilliermondi) achieved more than 80% decolorization within 24 h (50 and 100 mg/L dye). The chemical oxygen demand (COD) removal rate for the bacterial consortium (B-C) reached 97% in 72 h while the yeast consortium (Y-C) and the total microbial consortium (T-C; bacterial and yeast consortia combined) achieved 98.0% and 97.5%, respectively, in 24 h, indicating potential mineralization of the azo dye Acid Blue 113. Moreover, there was a positive relationship between cell growth and the azo dye degradation rate in all consortia. The Fourier transform infrared (FT-IR) spectra profiles for yeast-containing consortia showed a rapid disappearance of absorbance at the azo bond specific wavenumber (1455 cm-1) (24 h), while the B-C showed disappearance within 72 h. Metabolic products containing -NH2 groups were also detected based on the absorbance at the 1300 cm-1 wavenumber, reflecting an occurrence of azo bond cleavage. It was concluded that the data for decolorization, COD removal, cell growth, and FT-IR spectra collectively provide evidence for azo dye decolorization and potential mineralization of the dye by the bacterial and yeast consortium. Moreover, transcriptomic analysis using RNA-sequencing further explained the potential mechanisms of azo dye biodegradation by Sphingomonas melonis. NAD(P)-dependent oxidoreductase and type 1 glutamine amidotransferase were differentially expressed in the dye treatment, indicating that degradations of the azo bond and the aromatic compounds could be catalyzed by these enzymes. The selected microbial consortia could be applied for the bioremediation of azo dye wastewater at the industrial scale of varying environmental conditions.|์ด ์—ฐ๊ตฌ์˜ ๋ชฉ์ ์€ ์•„์กฐ ์—ผ๋ฃŒ ํ์ˆ˜์˜ ํšจ์œจ์ ์ธ ์ƒ๋ฌผํ•™์  ๋ถ„ํ•ด๋ฅผ ์œ„ํ•œ ๊ฐ€์žฅ ์ ์ ˆํ•œ ๋ฏธ์ƒ๋ฌผ ์ปจ์†Œ์‹œ์—„์„ ์„ ํƒํ•˜๋Š” ๊ฒƒ์ด๋‹ค. 2 ์ข…์˜ ๋ฐ•ํ…Œ๋ฆฌ์•„(Mesorhizobium sp. ๋ฐ Sphingomonas melonis)์™€ 2 ์ข…์˜ ํšจ๋ชจ(Apiotrichum mycotoxinivarans ๋ฐ Meyerozyma guilliermondi)๋กœ ๊ตฌ์„ฑ๋œ ์ปจ์†Œ์‹œ์—„์€ 24 ์‹œ๊ฐ„๋งŒ์— 50 ๋˜๋Š” 100 mg/L์˜ azo ์—ผ๋ฃŒ(Acid Bule 113)๋ฅผ 80 % ์ด์ƒ ํƒˆ์ƒ‰์„ ๋‹ฌ์„ฑํ–ˆ์Šต๋‹ˆ๋‹ค. ํ™”ํ•™์  ์‚ฐ์†Œ ์š”๊ตฌ๋Ÿ‰ (COD) ์ œ๊ฑฐ์œจ์€ 24 ์‹œ๊ฐ„ ํ›„ ํšจ๋ชจ ์ปจ์†Œ์‹œ์—„ (Y-C)๊ณผ ์ด ๋ฏธ์ƒ๋ฌผ ์ปจ์†Œ์‹œ์—„ (T-C, ๋ฐ•ํ…Œ๋ฆฌ์•„ ๋ฐ ํšจ๋ชจ ์ปจ์†Œ์‹œ์—„ ๊ฒฐํ•ฉ)์ด ๊ฐ๊ฐ 98.0 %์™€ 97.5 %๋ฅผ ๋‹ฌ์„ฑํ•˜๋Š” ๋ฐ˜๋ฉด, ๋ฐ•ํ…Œ๋ฆฌ์•„ ์ปจ์†Œ์‹œ์—„ (B-C)์€ 72 ์‹œ๊ฐ„ ํ›„ 97 % ๋‹ฌ์„ฑํ•˜์˜€๋‹ค. ๋˜ํ•œ, ๋ชจ๋“  ์ปจ์†Œ์‹œ์—„์—์„œ ์„ธํฌ ์„ฑ์žฅ๊ณผ azo ์—ผ๋ฃŒ ๋ถ„ํ•ด์œจ์€ ๋น„๋ก€๊ด€๊ณ„๋ฅผ ๊ฐ€์ง€๊ณ  ์žˆ๋‹ค. Fourier transform infrared (FT-IR) ์ŠคํŽ™ํŠธ๋Ÿผ ๋ถ„์„ ๊ฒฐ๊ณผ, Y-C๋Š” ์•„์กฐ ๊ฒฐํ•ฉ์„ ๋‚˜ํƒ€๋‚ด๋Š” ํŠน์ • ์ฃผํŒŒ์ˆ˜ (1455 cm-1)์—์„œ 24 ์‹œ๊ฐ„ ํ›„ ํก๊ด‘๋„์˜ ๊ธ‰๊ฒฉํ•œ ๊ฐ์†Œ๋ฅผ ๋ณด์ธ ๋ฐ˜๋ฉด, BC๋Š” 72 ์‹œ๊ฐ„ ํ›„ ์†Œ๋ฉธ์„ ๋ณด์˜€๋‹ค. ๋˜ํ•œ, ์•„์กฐ ๊ฒฐํ•ฉ์˜ ์ ˆ๋‹จ์„ ์˜๋ฏธํ•˜๋Š” โ€“NH2 ๊ทธ๋ฃน์˜ ์ฃผํŒŒ์ˆ˜ (1300 cm-1)์—์„œ๋„ azo ์—ผ๋ฃŒ๊ฐ€ ๋ถ„ํ•ด๋˜๋Š” ์‹œ๊ฐ„์— ๋”ฐ๋ผ์„œ ๊ฒ€์ถœ๋˜์—ˆ๋‹ค. ํƒˆ์ƒ‰ ์‹คํ—˜, COD ์ œ๊ฑฐ, ์„ธํฌ ์„ฑ์žฅ ๋ฐ FT-IR ์ŠคํŽ™ํŠธ๋Ÿผ์— ๋Œ€ํ•œ ๊ฒฐ๊ณผ๋ฅผ ์ข…ํ•ฉํ•ด๋ณด๋ฉด, ๋ฐ•ํ…Œ๋ฆฌ์•„ ๋ฐ ํšจ๋ชจ ์ปจ์†Œ์‹œ์—„์ด ์˜ํ•œ ์•„์กฐ ์—ผ๋ฃŒ์˜ ์ž ์žฌ์ ์ธ ๋ฌด๊ธฐํ™” ์ž‘์šฉ์— ๋Œ€ํ•œ ์ฆ๊ฑฐ๋ฅผ ์ œ๊ณตํ•œ๋‹ค๊ณ  ํ‰๊ฐ€๋˜์—ˆ๋‹ค. ๋˜ํ•œ, RNA ์‹œํ€€์‹ฑ์„ ํ†ตํ•œ ์ „์‚ฌ์ฒด ๋ถ„์„์€ Sphingomonas melonis์˜ ์ž ์žฌ์  ์•„์กฐ ์—ผ๋ฃŒ ๋ถ„ํ•ด ๋งค์ปค๋‹ˆ์ฆ˜์„ ๋ฐํ˜€๋‚ด์—ˆ๋‹ค. ์ฆ‰, NAD(P)-dependent oxidoreductase ๋ฐ type 1 glutamine amidotransferase๋Š” ์—ผ์ƒ‰๋ฌผ์งˆ์˜ ์ฒ˜๋ฆฌ๊ตฌ์— ์ฐจ๋ณ„์ ์œผ๋กœ ๋งŽ์ด ๋ฐœํ˜„๋œ ๊ฒƒ์œผ๋กœ ๋ณด์•„, ์ด๋Ÿฌํ•œ ํšจ์†Œ๊ฐ€ ์—ผ์ƒ‰๋ฌผ์งˆ์˜ ์•„์กฐ๊ฒฐํ•ฉ๊ตฌ์กฐ ๋ฐ ๊ทธ ๋ถ„ํ•ด์‚ฐ๋ฌผ์ธ ๋ฐฉํ–ฅ์กฑํ™”ํ•ฉ๋ฌผ์˜ ๋ถ„ํ•ด์— ๊ด€์—ฌํ•œ ๊ฒƒ์œผ๋กœ ํŒ๋‹จ๋˜์—ˆ๋‹ค. ์„ ๋ฐœ ๋œ ๋ฏธ์ƒ๋ฌผ ์ปจ์†Œ์‹œ์—„์€ ๋‹ค์–‘ํ•œ ํ™˜๊ฒฝ์  ์š”์ธ์— ๋…ธ์ถœ๋˜์–ด ์žˆ๋Š” ์‚ฐ์—…๊ทœ๋ชจ์˜ ์•„์กฐ ์—ผ๋ฃŒ ํ์ˆ˜ ์ฒ˜๋ฆฌ์— ์ƒ๋ฌผํ•™์ ์ฒ˜๋ฆฌ๋ฅผ ์œ„ํ•ด ์ ์šฉ๋  ์ˆ˜ ์žˆ์„ ๊ฒƒ์œผ๋กœ ๋ณด์ธ๋‹ค.Chapter 1. Introduction 1 Chapter 2. Literature Review 4 2.1 Principles of color chemistry 4 2.2 Azo dye decolorization and degradation 5 2.2.1 Azo dye treatment 5 2.2.2 Biological treatment of azo dyes 6 2.2.3 Enzymatic decolorization and degradation of azo dyes 6 2.3 RNA sequencing for transcriptomic analysis 11 Chapter 3. Materials and methods 12 3.1 Isolation of efficient microorganisms for azo dye biodegradation and their identification 12 3.2 Experimental culture setup for biodegradation of the azo dye Acid Blue 113 15 3.3 UV-vis spectrophotometric analysis for cell growth and dye biodegradation 16 3.4 Monitoring of azo dye biodegradation based on FT-IR analysis 17 3.5 Monitoring of the fate of organic compounds (azo dye and glucose) based on COD analysis 17 3.6. RNA isolation and sequencing procedure for RNA-seq analysis for the dye degradation 18 Chapter 4. Results and discussion 19 4.1 Dye decolorization by various cultures 19 4.2 Monitoring of organics through COD analysis 22 4.3 Comparison of cultural growth and concomitant decolorization activity in the microbial consortia 24 4.4 FT-IR and GC-MS analyses of the biodegradation process by microbial consortia for the azo dye AB113 26 4.5 Implications of the synergistic effects of inter genus co-culture in terms of bioremediation of azo dyes 29 4.6. Transcriptomic analysis of degradation of Acid Blue 113 30 Chapter 5. Conclusion 35 References 37 Academic achievement 49Maste

    Effects of different pH control strategies on microalgal nutrient removal and biomass production from anaerobic digestion effluent

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    Long-term effectiveness of bioaugmentation with rumen culture in continuous anaerobic digestion of food and vegetable wastes under feed composition fluctuations

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    Biogas plants treating food waste (FW) often experience feed load and composition fluctuations. In Korea, vegetable waste from the preparation of kimchi comprises over 20% of the total FW production during the Kimjang season. The large production of Kimjang waste (KW) can cause mechanical and operational problems in FW digesters. This study investigated the long-term effectiveness of bioaugmentation with rumen culture (38 months) in an anaerobic reactor co-digesting FW with varying amounts of KW. The bioaugmented reactor maintained better and stabler performance under recurrent fluctuations in feed characteristics than a nonbioaugmented control reactor, particularly under high ammonia conditions. Bioaugmentation increased microbial diversity, thereby improving the resilience of the microbial community. Some augmented microorganisms, especially Methanosarcina, likely played an important role in it. The results suggest that the proposed bioaugmentation strategy may provide a means to effectively treat and valorize KW-and potentially other seasonal lignocellulosic wastes-by co-digestion with FW

    Effects of Different pH Control Strategies on Microalgae Cultivation and Nutrient Removal from Anaerobic Digestion Effluent

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    This study investigated nutrient removal from anaerobic digestion effluent by cultivating mixed-culture microalgae enriched from anaerobic sludge under different pH conditions: RUC (uncontrolled), R7???8 (maintained at 7???8), and R<8 (maintained below 8). Significant amounts of NH4+-N were lost by volatilization in RUC cultures due to increased pH values (???8.6) during the early period of cultivation. The pH control strategies significantly affected the biological NH4+-N removal (highest in R7???8), microalgal growth (highest in R7???8), biomass settleability (highest in R<8), and microalgal growth relative to bacteria (highest in R<8) in the cultures. Parachlorella completely dominated the microalgal communities in the inoculum and all of the cultures, and grew well at highly acidic pH (<3) induced by culture acidification with microalgal growth. Microalgae-associated bacterial community structure developed very differently among the cultures. The findings call for more attention to the influence and control of pH changes during cultivation in microalgal treatment of anaerobic digestion effluent

    Long-term effectiveness of bioaugmentation with rumen culture in continuous anaerobic digestion of food and vegetable wastes

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    Complex network analysis of slaughterhouse waste anaerobic digestion: From failure to success of long-term operation

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    The study explored slaughterhouse waste (SHW) as prime feedstock associated with and without supplement of an external slowly degradable lignocellulosic carbon source to overcome the synergistic co-inhibitions of ammonia and fatty acids. Long-term solid-state digestion (SSD) and liquid-state digestion (LSD) were investi-gated using a mixture of pork liver and fat. At 2.0 g volatile solids (VS) L-1 d-1 of organic loading rate (OLR), the two reactors of SSD experienced operational instability due to ammonia inhibition and volatile fatty acid (VFA) accumulation while LSD successfully produced 0.725 CH4 L CH4 g- 1VS during 197 d of working days under unfavorable condition with high total ammonia nitrogen (> 4.7 g/L) and VFAs concentration (> 1.9 g/L). The network analysis between complex microflora and operational parameters provided an insight for sustainable biogas production using SHW. Among all, hydrogenotrophic methanogens have shown better resistance than acetoclastic methanogens

    Tracking microbial community shifts during recovery process in overloaded anaerobic digesters under biological and non-biological supplementation strategies

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    Anaerobic digestion encounters operational instability due to fluctuations in organic loading. Propionic acid (HPr) is frequently accumulated due to its unfavorable reaction thermodynamics. Here, 'specific' bioaugmentation using HPr enrichment cultures (three different injection regimes of quantity and frequency) was compared with 'non-specific' bioaugmentation using anaerobic sludge, and with non-biological supplementation of magnetite or coenzyme M. The specific bioaugmentation treatments showed superior recovery responses during continuous feeding after a peak overload. A 'one-shot' bioaugmentation with enrichment showed the best remediation, with similar to 25% recovery time and >10% CH4 conversion efficiency compared to the control. Consecutive bioaugmentation showed evidence of increased stability of the introduced community. Families Synergistaceae, Syntrophobacteraceae, and Kosmotogaceae were likely responsible for HPr-oxidation, in potential syntrophy with Methanoculleus and Methanobacterium. The different supplementation strategies can be considered to reduce the effect of start-up or overload in anaerobic digesters based on the availability of supplementation resources.11Nsciescopu
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