• Journal of the Korea Organic Resources Recycling Association
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• v.12 no.1
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• pp.58-66
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• 2004

The purpose of this study is to examine the possibility of reuse fermented foodwaste as a bulking agent in livestock waste and foodwaste composting. Aerobic composting device was added to the following sample : Foodwaste + Sawdust, Livestock feces+Sawdust, Foodwaste + Ferment, Livestock feces + Ferment. Temperature, pH, OM/N ratio, moisture, heavy metals, and microbes were measured in process of aerobic composting. The results of this study are following. 1. The composting period is determined in 16~24days, according to the change of temperature and OM/N ratio. 2. The salinity contents in compost of livestock waste and foodwaste ferment is about 0.5%, which can be solved the problems of salinity contents in foodwaste composting. 3. The proper ratio of livestock waste composting is 40% of cow feces to 60% of foodwaste ferment. 4. Processing expense of aerobic composting of foodwaste and sawdust is 40 won/kg composting expense of foodwaste and ferment is 30 won/kg. Fermented product composting can cut down the expense of bulking agent than others.

• Korean Journal of Food Science and Technology
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• v.44 no.2
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• pp.179-184
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• 2012

The objectives of this study were to manufacture the red ginseng vinegar based on rice wine and red ginseng concentrate (RGC) using $Acetobacter$ $aceti$ and to evaluate its quality with remaining crude saponin contents and sensory score. The maximum prosapogenin (ginsenoside-Rh1, Rh2, Rg2, and Rg3) content in RGC regarding ginseng was obtained from such processes as steaming, drying, and extraction. When RGC was added into a rice wine in the range of 0-1% before acetic fermentation, pH decreased slowly during 20 days depending on RGC contents, but total acidity was not dependent on RGC contents. Compared to the crude saponin content (71.75 mg/g) of ginseng vinegar added RGC after acetic fermentation, the fermentation with RGC produced a lower crude saponin content (16.95 mg/g) in red ginseng vinegar. Sensory scores such as odor, taste, and overall preference, however, vinegar fermented with RGC were higher than those of vinegar added RGC after acetic fermentation.

• KSBB Journal
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• v.24 no.2
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• pp.207-211
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• 2009

In this study, the sensing membranes for detection of pH and dissolved oxygen(DO) were prepared by immobilizing 6-aminofluorescein or ruthenium complex onto the sol-gel matrixes of GPTMS, MTMS, and TEOS and then recoated with the mixture of hydrophobic sol-gel and graphite for light insulation. The pH and DO sensing membranes recoated with the light insulation layer showed a higher sensitivity than those without light insulation layer. The sensing membranes were immobilized on the wells of 24-well microplate and used to monitor the fluorescence intensity for pH and DO in E.coli JM109 and P.pastoris X-33 fermentation processes. The change of the fluorescence intensity in the DO sensing membrane agreed with the growth patterns of microorganisms, that the membranes are valuable to monitor the DO in fermentation processes. In the case of pH monitoring, the fluorescence intensity has showed good correlation to the off-line pH data, that the pH membranes are valuable to monitor pH values in fermentations.

• KSBB Journal
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• v.14 no.2
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• pp.212-219
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• 1999

lactic acid production from cellulose by simultaneous saccharification and fermentation(SSF) was studied. The SSF using cellulase enzyme Cytolase CL and Lactobacillus delbrueckii was strongly inhibited by the end product(lactic acid). An ion-exchange resin(RA-400) was used for in-situ product removal during SSF. The sorption capacity of the resin was 200mg/g-resin. The simple SSF and the extractive SSF resulted in lactic acid concentrations of 30.4g/L and 32.0g/L, respectively, at the initial substrate concentration of 50g/L. A model was developed to simulate the extractive SSF. The lactic acid conversion for the initial substrate of 100g/L was estimated to be improved from 60% to 09% by in-situ product removal. The experimentally determined kinectic parameters were pH dependent, and fitted as empirical expressions to establish their values at different pH's. Lactic acid productivity was predicted to be maximum at pH 4.5-5.0.

• KSBB Journal
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• v.14 no.5
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• pp.628-632
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• 1999

Optimization of the medium and fermentation conditions for erythritol production has been studied. We have found that the optimal carbon source was glucose at the concentration of 400 g/L. The optimal temperature was 3$0^{\circ}C$ with excessive aeration. Improved erythritol productivity was achieved by reducing the yeast extract from 5 g/L to 3g/L while adding 2.7 g/L urea, 1.79g/L $K_2HPO_4, and 0.18g/L MgSO$_4$. 7$H_2O. The erythritol productivity increased from 0.747 g/L/h to 1.071 g/L/h and the yield increased from 31.4% to 45.2%. The byproduct glycerol was reduced from 96.6g/L to 45.7g/L as well. We have performed 5L fermentation with and without the pH control. The erythritol productivity with the pH control was about 30% lower than that without pH control. Excessive foaming of 5L fermentation has been observed during fermentation.

• Microbiology and Biotechnology Letters
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• v.20 no.6
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• pp.677-680
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• 1992

The effects of pH, temperature and oxygen transfer rate(OTR) on L-Ieucine fermentation were investigated employing Corynebacterium glutamicum CH 1516 in 71 fermentor. The optimum pH, temperature and OTR were determined to be 7.0, $30^{\circ}C$ and 0.21 kmole $O_2$/$m^3{\cdot}hr$, respectively. For the values of OTR lower than 0.19 kmole $O_2$/$m^3{\cdot}hr$ a significant amount of lactic acid was accumulated, while the packed cell volume(PCV) was rapidly increased at higher OTR values above 0.23 kmole $O_2$/$m^3{\cdot}hr$ and glutamic acid was produced to some extent. Scale-up studies for L-Ieucine fermentation which was carried out in 12001 pilot scale fermentor reaffirmed the results of 71 fermentation. The optimum redox potential value for L-Ieucine production was found to be -150 to -170 mY.

• Transactions of the Korean hydrogen and new energy society
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• v.26 no.3
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• pp.247-259
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• 2015

This study was performed to investigate the application of dark $H_2$ fermentation to two-stage bioprocesses for organic waste treatment and energy production. We reviewed information about the two-stage bioprocesses combining dark $H_2$ fermentation with $CH_4$ fermentation, photo $H_2$ fermentation, microbial fuel cells (MFCs), or microbial electrolysis cells (MECs) by using academic information databases and university libraries. Dark fermentative bacteria use organic waste as the sole source of electrons and energy, converting it into $H_2$. The reactions related to dark $H_2$ fermentation are rapid and do not require sunlight, making them useful for treating organic waste. However, the degradation is not complete and organic acids remain. Thus, dark $H_2$ fermentation should be combined with a post-treatment process, such as $CH_4$ fermentation, photo $H_2$ fermentation, MFCs, or MECs. So far, dark $H_2$ fermentation followed by $CH_4$ fermentation is a promising two-stage bioprocess among them. However, if the problems of manufacturing expenses, operational cost, scale-up, and practical applications will be solved, the two-stage bioprocesses combining dark $H_2$ fermentation with photo $H_2$ fermentation, MFCs, or MECs have also infinite potential in organic waste treatment and energy production. This paper demonstrated the feasibility of two-stage bioprocesses combining dark $H_2$ fermentation as a novel system for organic waste treatment and energy production.

• Korean Journal of Food Science and Technology
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• v.44 no.2
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• pp.141-147
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• 2012

Biogenic amines have been used as chemical indicators to estimate bacterial spoilage of foods, particularly fish and fish products, cheese, and fermented foods. So far many chromatography methods have been developed to detect biogenic amines in foods. Although these instrumental analyses exhibit good sensitivity, they cannot be used as rapid detection methods due to the chemical treatment of the samples and the time-consuming process involved. For the rapid and simple detection of biogenic amines, enzyme linked immunosorbent assay kits are commercially available. In addition, analytical systems with enzyme-based amperometric biosensor detection have been increasingly developed. The biosensors used to detect the biogenic amines are based on the action of either amine oxidases or amine dehydrogenases that catalyzes the oxidative deamination of biogenic amines to the corresponding aldehydes and ammonia. This review mainly focused on the principle, development, and applications of the detection methods for rapid detection of biogenic amines in foods.

• KSBB Journal
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• v.5 no.2
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• pp.95-100
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• 1990

Ethanol fermentations of inulin by K.fraglis in aqueous two-phase system of PEG/Dextran were performed not only to investigate the characteristics of partition of ethanol, sugar, and cell in the upper phase and the bottom phase but also to compare the fermentation properties with those of single phase system. In the range of 1 to 3 wt% of Dextran, ethanol fermentability and ethanol productivity reduced according to the increase of the molecular weight of PEG. But the cell yield and the cell productivity showed the opposite trend. In the region of 6 to 10 wt% of PEG, the increase of the concentration of PEG, caused the minute decrease of ethanol productivity but the remarkable augmentation of cell productivity. According to the increase of the molecular weight of PEG, the partition coefficient of inulin slightly decreased. But with the increment of the concentration of Dextran, the partition coefficient and the partition yield of inulin in the bottom Phase represented the trends of increase.

• KSBB Journal
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• v.19 no.6 s.89
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• pp.478-483
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• 2004

The optimum fermentation conditions of Propionibacterium acidipropionici were determined for the maximum production of organic acids. Three strains of P. acidipropionici, ATCC 25562, 4875, 4965 were selected to test the productivity of organic acids in the batch fermentation. Nutrients and environmental conditions on cell growth were defined by series of experiments, and the optimum amounts of peptone, yeast extract were determined to be $1.5\%$ (w/v), $0.75\%$ (w/v), respectively. The yields and productivity were highest at pH 6 among the ranges of $5.0{\sim}7.5$, and ATCC 4965 was determined to be the best strain compared to the others by getting total productivity of 0.29 g total acids/L/h. Approximately $1.60{\sim}2.34$ moles of propionic acid and $0.74{\sim}1.05$ moles of acetic acid were produced from 1.5 moles of glucose.