• 제목/요약/키워드: dry mass production

검색결과 187건 처리시간 0.032초

Effects of Cadmium on Radial Growth and Dry Mass Production of Ectomycorrhizal Fungi

  • Kim, Chang-Gi;Power, Sally Anne;Bell, John Nigel Berridge
    • The Korean Journal of Ecology
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    • 제27권5호
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    • pp.301-306
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    • 2004
  • The sensitivity to Cd of three ectomycorrhizal fungi, Paxillus involutus, Suillus bovinus and Rhizopogon subcaerulescens, was assessed and compared in terms of radial growth and dry mass production, using both agar and liquid culture. The radial growth of S. bovinus and R. subcaerulescens was significantly reduced at the lowest concentration (0.1mg Cd/L). The 50% effective concentration (EC$_{50}$) values calculated from radial growth rates of the ectomycorrhizal fungi showed that the sensitivity of the fungi to Cd was greatest in S. bovinus and lowest in R. subcaerulescens. Cadmium addition also significantly decreased dry mass production of the ectomycorrhizal fungi. The sensitivity of the fungi to Cd in terms of dry mass production, was greatest in S. bovinus and lowest in P. involutus. Higher growth rates of P. involutus and melanisation of R. subcaerulescens appeared to contribute to reduced Cd toxicity.

Bacillus licheniformis SCD121067 균체 생산성 증가를 위한 통계적 생산배지 및 발효조건 최적화 (Optimization of Medium and Fermentation Conditions for Mass Production of Bacillus licheniformis SCD121067 by Statistical Experimental Design)

  • 정유민;이주희;정혜종;전계택;윤순일;정용섭
    • KSBB Journal
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    • 제25권6호
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    • pp.539-546
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    • 2010
  • In this work, mass production of Bacillus licheniformis SCD121067 through medium optimization by statistical experimental method was studied. First, galactose, yeast extract and potassium phosphate dibasic were selected as carbon, nitrogen and phosphate sources for mass production of B. licheniformis SCD121067 by using one factor at a time method. Second, according to the result of Plackett-Burman experimental design, key factors was yeast extract and $K_2HPO$. Finally, the response surface methodology was performed to obtain the optimum concentrations of two selected variables. The optimized medium composition consisted of 20 g/L galactose, 36 g/L yeast extract, 0.41 g/L $K_2HPO4$, 0.25 g/L $Na_2CO_3$, 0.4g/L $MgSO_4$ and 0.01g/L $CaCl_2$. Dry cell weight (15.4 g/L) by optimum production medium were increased 10 times, as compared to that determined with basic production medium (1.5 g/L). Fermentation conditions were examined for the mass production of B. licheniformis. The effect of temperature, agitation speed, pH and aeration rate on the mass production of B. licheniformis were also studied in a batch fermenter which was carried out in a 2.5 L bioreactor with a working volume of 1.5 L containing optimized production medium. As a result, dry cell weight of batch culture was 30.7 g/L at $42^{\circ}C$, 300 rpm, pH 8.0 and 2 vvm.

3단압축 드라이아이스 제조사이클의 압축동력과 엑서지 해석 (Compression Power and Exergy Analysis in a Dry Ice Production Cycle with 3-stage Compression)

  • 이근식
    • 설비공학논문집
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    • 제12권6호
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    • pp.550-560
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    • 2000
  • In order to minimize compression power and analyze the cause of exergy loss for a dry ice production cycle with 3-stage compression, the variation of compression power was investigated and the exergy analysis was peformed for the cycle. In this cycle, $CO_2$, is used both as a refrigerant and as a raw material for dry ice. The behavior of compression power and irreversibility in the cycle were examined as a function of intermediate pressure. From this result, the conditions for the minimum compression power were obtained in terms of the first stage or the third stage pressure. In addition, the irreversibilities for the cycle were investigated with respect to the efficiency of compressor. Result shows that the optimum pressure is not consistent with the conventional pressure obtained from the equal-pressure-ratio assumption. This is mainly due to the change in mass flow rate of the intermediate stage compressor by the flash gas evaporation from the flash drums. Most important is that the present exergy analysis enabled us to find bad performance components for the cycle and informed us of methods to improve the cycle performance.

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고압나트륨등 조사가 파프리카의 동적 생장과 건물분배율에 미치는 영향 (Effects of the High Pressure Sodium Lamp Lighting on the Dynamics of Growth and Dry Mass Partitioning in Sweet Pepper Plant)

  • 김은정;이상현;이정현
    • 원예과학기술지
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    • 제31권5호
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    • pp.565-572
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    • 2013
  • 본 연구의 목적은 고압나트륨등 광원(HPS)을 조사하여 파프리카의 동적생장과 기관별 건물분배율 및 광이용효율에 미치는 효과를 구명하고자 수행하였다. 파프리카 육묘는 2010년 9월 29일에 $m^2$당 3.75주를 정식하여 2010년 12월 14일부터 HPS 광원을 실험종료일까지 하루 16시간 조사하였다. HPS 처리는 엽수를 증가시켰으나, 절간수와 엽면적에는 미비한 영향을 미쳤다. HPS 처리구의 초장은 대조구에 비해 짧았으나, 줄기당 착과수의 증가를 나타냈다. 줄기와 과실 및 총건물중은 HPS 처리구가 대조구보다 각각 28.5%, 97.1%, 67.8%를 증가시켰다. 총 건물중의 증가율 대비 엽과 줄기 생장율을 비율로 나타낸 각 기관의 건물분배율은 생육초기에 45-47%로 동일하다가 과실의 생장이 시작되는 시점에서 급격히 감소하였다. 영양생장기관으로의 건물분배율은 대조구에서 HPS 처리구보다 4% 높았다. 과실로의 평균 건물 분배율을 HPS 처리구에서 대조구에 비해 14.2% 증가하였다. 동적생장량은 지수선형함수의 최대상대생장율, 최대 절대생장율 및 손실일수로 잘 묘사할 수 있었다. 대조구에 비해 처리구의 엽의 최대절대생장율은 18.6%, 줄기는 74.7%, 과실은 143.5%가 증가하는 것으로 추정되었다. 총 건물중에 대한 광이용효율(LUE)은 HPS 처리구에서 $4.90g{\cdot}MJ^{-1}$로 대조구의 $3.84g{\cdot}MJ^{-1}$ 높았으며, 영양생장기관의 LUE는 HPS 처리구가 $1.56g{\cdot}MJ^{-1}$로 대조구의 $1.61g{\cdot}MJ^{-1}$보다 약간 낮았으며, 과실 생산에 대한 LUE는 처리구가 $3.34g{\cdot}MJ^{-1}$로 대조구 $2.23g{\cdot}MJ^{-1}$보다 49.8% 증가하였다. 처리간 총 건물중의 LUE의 차이는 HPS 처리구의 과실생산에 대한 LUE가 높았기 때문에 발생되었다.

Effect of Aeration-Agitation on Coenzyme Q10 Production Using Rhodobacter sphaeroides

  • Jeong, Soo-Kyoung;Kim, Joong-Kyun
    • Fisheries and Aquatic Sciences
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    • 제11권4호
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    • pp.224-228
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    • 2008
  • With the aim of increasing the $CoQ_{10}$ production in mass culture, the effect of aeration-agitation on the $CoQ_{10}$ production using Rhodobactor sphaeroides was investigated in a l-L bioreactor. The maximum $CoQ_{10}$ production was 1.69 mg/g of dry cell weight under conditions of 50 Lux, $30^{\circ}C$, 300 rpm, and 5-vvm aeration. The $CoQ_{10}$ production was improved to produce 2.91 mg/g of dry cell weight under reduced conditions of agitation speed (200 rpm) and aeration rate (0.2 vvm). When R. sphaeroides was cultivated under more reduced DO levels during the exponential phase of the cell, the $CoQ_{10}$ production yield of 3.88-mg/g dry cell weight was the maximum obtained. Therefore, poorer conditions of aeration-agitation resulted in higher production of $CoQ_{10}$, and thus DO content was a crucial factor in the production of $CoQ_{10}$. Accordingly, it was necessary to control the DO concentration in order to enhance the $CoQ_{10}$ biosynthesis within a large-scale production.

Effects of pH and Light Irradiation on Coenzyme Q10 Production Using Rhodobacter sphaeroides

  • Jeong, Soo-Kyoung;Dao, Van Thingoc;Kien, Ngyuen;Kim, Joong-Kyun
    • Fisheries and Aquatic Sciences
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    • 제11권4호
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    • pp.219-223
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    • 2008
  • To increase the level of $CoQ_{10}$ production in mass culture, the effects of pH and light irradiation on $CoQ_{10}$ production by Rhodobacter sphaeroides were investigated in a 1-L bioreactor. $CoQ_{10}$ production was growth-associated, and the highest production of $CoQ_{10}$ (1.69 mg/g dry cell) was obtained under uncontrolled pH: this production was 1.7 times higher than that obtained at controlled pH 7. Therefore, pH was a key factor affecting $CoQ_{10}$ production. The effect of light irradiation on $CoQ_{10}$ production was negligible. This result offers an advantage for mass production of $CoQ_{10}$.

Use of Sucrose-Agar Globule with Root Exudates for Mass Production of Vesicular Arbuscular Mycorrhizal Fungi

  • Thangaswamy Selvaraj;Kim, Hoon
    • Journal of Microbiology
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    • 제42권1호
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    • pp.60-63
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    • 2004
  • A sucrose-agar globule (SAG) was newly introduced to increase production of the vesicular arbuscular mycorrhizal (VAM) fungal spores, Gigaspora gigantea and Glomus fasciculatum. An SAG inoculum and a sucrose-agar globule with root exudates (SAGE) inoculum were prepared, and their spore productions were compared with a soil inoculum. When the SAGE was used as the inoculum on sucrose-agar medium plates the number of spores was increased (35% more than the soil inoculum). After the soil inoculum and SAGE were inoculated on an experimental plant, Zingiber officinale, the percentage root colonization, number of VAM spores, and dry matter content were analyzed. It was observed that the SAGE showed a higher percentage of root colonization (about 10% more), and increases in the number of spores (about 26%) and dry matter (more than 13%) for the two VAM fungal spores than the soil inoculum. The results of this study suggested that the SAGE inoculum may be useful for the mass production of VAM fungi and also for the large scale production of VAM fungal fertilizer.

자외선-B 증가에 따른 소나무 유묘의 생장 단계별 생장 반응 (Growth Responses at Different Growth Stage of Pinus densiflora Seedlings to Enhanced Uv-B Radiation)

  • 김종진
    • 임산에너지
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    • 제19권1호
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    • pp.1-6
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    • 2000
  • 본 연구는 소나무(Pinus densifora S. et Z.) 유묘의 발아전 단계, 자엽 단게 및 1차엽 발생후 단계 등 각각의 생육단계에서의 UV-B 증가 환경에 노출될 때의 생장반응을 탐구하고자 16주 동안 3수준의 UV-B(ambient UV-BBE, ambient + 3.2, ambient + 5.2 KJm-2s-1) 조사량이 설치된 야외 포장에서 실시되었다. UV-B 조사에 의하여 소나무 유묘의 수고생장, 근원경생장 및 건물생산량은 감쇠되었으며 T/R율은 증가하였다. 유묘에 대한 UV-B 처리시작 단계 차이에 따른 생장차이도 관찰되었는데, ambient +3.2 처리구내에서 보면 발아전 단계부터 UV-B 처리를 받은 유묘의 수고생장 및 근원경생장이 상대적으로 높았다. 주 수준의 UV-B 증가 처리구에서 모두 자엽단계부터 처리를 잗은 유묘의 건물생산량이 각 처리구내에서 가장 낮앗다. 한편 UV-B 증가에 의해 소나무 유묘 침엽의 엽롭소 함량은 감소하였으며 엽록소 a/b율은 증가하였다.

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High Cell Density Cultivation of Pseudomonas oleovorans for the Production of Poly(3-Hydroxyalkanoates)

  • Lee, Sang-Yup
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제1권1호
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    • pp.51-53
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    • 1996
  • Fed-batch culture of Pseudomonas oleovorans was carried out for the production of medium-chain-length polyhydroxyalkanoates (MCL-PHAs) using octanoate as a carbon source. Octanoate and the salt solution containing ammounium sulfate and magnesium sulfate were intermittently fed in the course of fermentation. Cell mass and PHA concentrations of 42.8 and 16.8g/L, respectively, could be obtained in 40 h. The PHA content and the PHA productivity were 39.2% and 0.42 g PHA/L-h, respectively. The yields of cell mass and PHA were 0.71 g dry cell mass/g octanoate and 0.28g PHA/g octanoate, respectively. Therefore, octanoate can be used for the production of MCL-PHAs to a high concentration with high productivity.

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WS$_2$ 고체윤활제의 양산 및 적용 (Mass-production of WS$_2$ Solid Lubricant and Its applications)

  • 신동우;최인혁;윤대현;김경도
    • 한국윤활학회:학술대회논문집
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    • 한국윤활학회 1998년도 제28회 추계학술대회
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    • pp.221-226
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    • 1998
  • The processing conditions for the mass production of platelet WS$_2$ lubricant powder were optimized. The mixture of tungsten and sulfur powders was sealed in a vacuum of 10$^{-3}$ torr and heat-treated at 850$\circ$C for 2 h. The internal pressure of reaction chamber was maintained at certain level by controlling the release valve automatically. The reaction product was the platelet WS$_2$ powder with an average size of 15 $\mu$m. The synthesized WS$_2$ powder was then coated on the wiper-blade of automobiles and the commercial deep-grooved ball bearing using wet and dry coating methods, respectively. High lubricity and wear resistance of wet coated wiper-blade were confirmed by the life test of 70,000 cycles. The life-time of the ball bearing assembled after WS$_2$ coating onto each part increased 50 times compared to the non-coated ball bearing.

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