• Biotechnology and Bioprocess Engineering:BBE
• /
• 제5권4호
• /
• pp.288-305
• /
• 2000

A review on the main aspects associated with yeast flocculation and its application in biotechnological processes is presented. This subject is addressed following three main aspects-the basics of yeast flocculation, the development of "new" flocculating yeast strains and bioreactor development. In what concerns the basics of yeast flocculation, the state of the art on the most relevant aspects of mechanism, physiology and genetics of yeast flocculation is reported. The construction of flocculating yeast strains includes not only the recombinant constitutive flocculent brewer's yeast, but also recombinant flocculent yeast for lactose metabolisation and ethanol production. Furthermore, recent work on the heterologous $\beta$-galactosidase production using a recombinant flocculent Saccharomyces cerevisiae is considered. As bioreactors using flocculating yeast cells have particular properties, mainly associated with a high solid phase hold-up, a section dedicated to its operation is presented. Aspects such as bioreactor productivity and culture stability as well as bioreactor hydrodynamics and mass transfer properties of flocculating cell cultures are considered. Finally, the paper concludes describing some of the applications of high cell density flocculating bioreactors and discussing potential new uses of these systems.e systems.

• Journal of Microbiology and Biotechnology
• /
• 제5권6호
• /
• pp.364-369
• /
• 1995

Effect of two-phase culture on Mentha piperita cell growth and essential oil formation was investigated using shake flask and air-lift bioreactors. LiChroprep RP-B(RP-B) addition did not impair M. piperita cell growth, but resulted in stimulated formation of essential oils and increased ratios of extracellular oil to intracellular oil formation. However, the combined use of RP-B and chitosan elicitor was not synergistic. Volumetric productivity of essential oils in RP-B treated culture using cell-recycled air-lift bioreactor was $6.9\;\mu\textrm{g}/l{\cdot}day$ which was substantially higher than that obtainable from the control. Our results demonstrate the potential of a second phase to enhance overall productivity for M. piperita cell culture.

• Journal of Plant Biotechnology
• /
• 제33권2호
• /
• pp.117-122
• /
• 2006

Comparative studies on medium supply in bioreactors (raft, immersion and ebb and flood) have revealed that multiplication and growth of Alocasia Amazonica were greatest in the raft system, while lowest in ebb and flood system. In the raft system, the basal part of the shoots was continuously in contact with medium, which enabled a constant uptake of nutrients as well as aeration to the explants. The number and the size of leaf stomata were higher in the raft system compared with immersion and ebb&flood system. In the immersion system, plantlets were deformed and epidermal cells in leaves were irregular with a large intercellular space. The results suggested that the medium supply should be controlled properly to maintain normal and healthy plantlets during liquid cultures in bioreactors Which affects morphology and physiology Of the plantlets.

• Membrane and Water Treatment
• /
• 제3권1호
• /
• pp.1-23
• /
• 2012

The coupling of anaerobic biological process and membrane separation could provide excellent suspended solids removal and better biomass retention for wastewater treatment. This coupling improves the biological treatment process while allowing for the recovery of energy through biogas. This review gives a basic description of the anaerobic wastewater treatment process, summarizes the state of the art of anaerobic membrane bioreactors (AnMBRs), and describes the current research trends and needs for the development of AnMBRs. The research interest on AnMBR has grown over the conventional anaerobic processes such as upflow anaerobic sludge blanket (UASB). Studies on AnMBRs have developed different reactor configurations to enhance performances. The AnMBR performances have achieved comparable status to other high rate anaerobic reactors. AnMBR is highly suitable for application with thermophilic anaerobic process to enhance performances. Studies indicate that the applications of AnMBR are not only limited to the high strength industrial wastewater treatment, but also for the municipal wastewater treatment. In recent years, there is a significant progress in the membrane fouling studies, which is a major concern in AnMBR application.

• 상하수도학회지
• /
• 제23권2호
• /
• pp.175-180
• /
• 2009

This study was conducted to improve biological degradation efficiency of toluene as a model volatile organic compound (VOC) using yeast Candida tropicalis and to suggest an effective method for bioreactor operation. The yeast strain was immobilized with polyethylene glycol (PEG), alginate, and powdered activated carbon (PAC). The yeast-immobilized polymer media were used as fluidized materials in an airlift bioreactor. Polymer media without PAC were also made and operated in another airlift bioreactor. The two bioreactors showed toluene removal efficiencies ranging 80-96% at loading rates of $10-35 g/m^3-hr$, and the bioreactor containing the polymer media with PAC achieved higher removal efficiency. Protein contents in the liquid phase showed that the bioreactor using the yeast-immobilized polymer media with PAC had a higher rate of microbial growth initially than that without PAC. In addition, the microbial growth rate inside of the polymer media with PAC was five times higher than that without PAC. Consequently, the polymer media containing the yeast strain and PAC could enhance removal efficiencies for VOCs, and the immobilization method improve microbial activity and stability for a long-term operation of biological systems.

• Journal of Microbiology and Biotechnology
• /
• 제28권12호
• /
• pp.1955-1970
• /
• 2018

Several genetic strategies have been proposed for the successful transformation and expression of microbial transgenes in model and crop plants. Here, we bring into focus the prominent applications of microbial transgenes in plants for the development of disease resistance; mitigation of stress conditions; augmentation of food quality; and use of plants as "bioreactors" for the production of recombinant proteins, industrially important enzymes, vaccines, antimicrobial compounds, and other valuable secondary metabolites. We discuss the applicable and cost-effective approaches of transgenesis in different plants, as well as the limitations thereof. We subsequently present the contemporary developments in targeted genome editing systems that have facilitated the process of genetic modification and manifested stable and consumer-friendly, genetically modified plants and their products. Finally, this article presents the different approaches and demonstrates the introduction and expression of microbial transgenes for the improvement of plant resistance to pathogens and abiotic stress conditions and the production of valuable compounds, together with the promising research progress in targeted genome editing technology. We include a special discussion on the highly efficient CRISPR-Cas system helpful in microbial transgene editing in plants.

• KSBB Journal
• /
• 제14권4호
• /
• pp.440-444
• /
• 1999

S. clavulirerus ATCC 27064 균주는 약 200 mg/L의 clavulanic acid를 생산하였지만, 이 균주를 NTG에 의해 돌연변이 시킴으로써 얻어진 S. clavuligerus KK를 같은 배양조건에서 약 5배 많은 1150 mg/L의 clavulanic acid를 생산하였다. 무기염이 첨가되지 않은 clavulanic acid의 기본 생산 배지에서는 clavulanic acid의 생산량은 1150 mg/L였으나 다양한 무기염 중에서 MgSO$_4$가 첨가된 배지에서는 약 2000 mg/L나 생산되었다. 따라서 기본 배지조성인 1%(v/v) glycerol, 1.5%(w/v) soybean flour, 0.1%(w/v) $KH_2PO_4$, 0.2%(v/v) soybean oil에 0.4%(w/v) MgSO$_4$를 첨가함으로써 clavulanic acid의 생산을 높일 수 있었다.Airlift 와 bubble column 및 교반식 생물반응기에서 회분식 배양을 했을 경우 clavulanic acid의 생산은 airlift 생물 반응기에서는 1100 ng/L, bubble column 생물 반응기에서는 1450 mg/L, 교반식 생물 반응기에서는 1500 mg/L가 생산되어, 교반식 반응기가 적절하다고 생각되며 이는 배양액이 시간이 지날수록 점도가 높아지기 때문에 임펠러에 의한 교반 효과가 있는 교반식 반응기에서 물질전달이 가장 용이하기 때문인 것으로 보인다. 특히 교반식 생물 반응기에서 용존산소농도에 따라 교반속도를 조절하여 회분식 배양을 했을 경우가 수율이 0.18, 생산성은 250mg/Lㆍday로 가장 우수하게 나타났다.

• 한국미생물·생명공학회지
• /
• 제42권1호
• /
• pp.41-50
• /
• 2014

수소생산 유효세균을 유지하기 위해 열처리한 혐기소화슬러지를 접종원으로 하여 PVA 담체를 활용한 고정화와 비고정화 방법에 의한 수소생산능 및 세균 군집을 비교분석 하였다. 고정화에 의한 수소생산성은 비고정화 방법과 비교하여 수소생산성에 영향을 미치지 않았다. 그러나 고정화 방법은 유기물 분해결과 발생하는 유기산 축적 및 pH 강하 등의 환경변화에 있어 세균의 성장과 활성에 안정적 환경을 제공할 수 있는 가능성을 나타내었다. DGGE 분석에 의한 세균군집분석에서는 비고정화와 고정화 반응조간에 형성된 세균군집이 차이가 있는 것으로 나타났으며, 상대적으로 고정화 반응조내의 유효 수소생산 세균 군집이 좀 더 안정적으로 유지되는 것으로 확인되었다. Droplet digital PCR에 의한 6종의 유효한 수소생산 세균 절대정량 분석결과, encapsulation에 관계없이 두 반응기에서의 우점세균수는 유사하였다. Firmicutes, Clostridium, Enterobacter, Ruminococcus 및 Escherichia가 $1{\times}10^5-1{\times}10^6$ copy number of ml-sample 수준에서 존재하였다.

• 한국생물공학회:학술대회논문집
• /
• 한국생물공학회 2001년도 추계학술발표대회
• /
• pp.606-609
• /
• 2001

The anaerobic bacterium Clostridium ljungdahlii was known to produce ethanol from CO, $CO_2$ and $H_2$ In this research the production of ethanol at high concentration from carbon monoxide was studied. ethanol production using fed -batch, ceramic filter supported system, and 2-stage bioreactors were tested and optimized.

• 한국미생물·생명공학회지
• /
• 제17권6호
• /
• pp.629-633
• /
• 1989

In the continuous reactor, the hydrogen production rate and residual glucose concentration were increased with increase of input glucose concentration, dilution rate, and recycle rate. The maximum production rate was 91 mL/Lㆍh at dilution rate 0.4/h, input glucose concentration 5.4g/L, and recycle rate 70/h in this experimental range.