• 제목/요약/키워드: H-continuous

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연주롤용 육성용접 재료의 고온마모 및 부식특성에 미치는 Nb, V의 영향 (The Effects of Nb, V on the High Temperature Wear and Corrosion of the Overlaying Materials for Continuous Casting Rolls)

  • 김창규;황동수;윤재홍;강창룡;곽희환
    • 동력기계공학회지
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    • 제8권3호
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    • pp.30-35
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    • 2004
  • In the steel making industries, the continuous casting process has been applied to the number of company because of its economical benefit. Casting rolls are utilized for frictional drive and transport of solidifying slap. Dimensional tolerances, mechanical stability and surface condition of the cast roll can affect both the surface and internal quality of the product being cast. To overcome these problems, the industry is accelerating on the rate of technology improvements. Samples were overlaid on the S45C steel by submerged arc welding process. And the hardness, wear, electrochemical corrosion and oxidation tests were carried out. Test results were that all these materials were satisfying basic requirements of caster rolls. By these results, the addition of 0.1%Nb and 0.15%V increase mechanical properties and tempering resistance by its superior carbide forming characteristics in low carbon $12{\sim}13%Cr$ martensitic stainless steels.

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Production of Beijerinckia indica HS-2001 in Fed-batch and continuous culture.

  • 양재균;서형필;신명교;이진우
    • 한국생물공학회:학술대회논문집
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    • 한국생물공학회 2003년도 생물공학의 동향(XII)
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    • pp.245-248
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    • 2003
  • As a result of broth substitutions when each culture-mediums were difference, whole culture-medium was found to be best feeding solution for production of PS-7 by B. indica. Maximal production of PS-7 was 1$10.0\;g/{\ell}$ and its conversion rate from 2% (w/v) glucose to PS-7 was 50%. After 48 hr, 50%(v/v) medium of working volume began to substitute in 7L jar fermenter. Production of PS-7 increased after 48hr, recovered productivity of PS-7. Following this preliminary culture, the resultant culture was subjected to continuous flow conditions controlled that the dilution rate were $0.01\;{\sim}\;0.04\;h^{-1}$. Production of PS-7 increased at dilution rate $0.0100\;h^{-1}$ whereas productivity of PS-7 decreased gradually in dilution rate $0.0200\;{\sim}\;0.0400\;h^{-1}$. Maximal production of PS-7 was $10.0\;g/{\ell}$ in continuous culture.

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Physiological Characteristics of Immobilized Streptomyces Cells in Continuous Cultures at Different Dilution Rates

  • Kim, Chang-Joon;Chang, Yong-Keun;Chun, Gie-Taek;Jeong, Yeon-Ho;Lee, Sang-Jong
    • Journal of Microbiology and Biotechnology
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    • 제12권4호
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    • pp.557-562
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    • 2002
  • Physiological characteristics such as specific productivity, morphology of Streptomyces cells Immobilized on celite beads, and operational stability at different dilution rates were investigated in continuous immobilized-cell cultures for the production of kasugamycin. At a dilution rate (D) of 0.05 $h^{-1}$, a relatively high specific productivity was attained and the loss of cell-loaded beads was negligible. At D=0.1 $h^{-1}$, a higher specific productivity and cell concentration could be obtained, resulting in a significantly improved volumetric kasugamycin productivity. However, no stable operation could be maintained due to a significant loss of cell-loaded beads from the reactor that was caused by their fluffy morphology developed in the later stage. At D=0.2 $h^{-1}$, the production of kasugamycin and cell growth were observed to be severely inhibited by the high concentration of residual maltose.

Catalytic Biofilms on Structured Packing for the Production of Glycolic Acid

  • Li, Xuan Zhong;Hauer, Bernhard;Rosche, Bettina
    • Journal of Microbiology and Biotechnology
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    • 제23권2호
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    • pp.195-204
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    • 2013
  • While structured packing modules are known to be efficient for surface wetting and gas-liquid exchange in abiotic surface catalysis, this model study explores structured packing as a growth surface for catalytic biofilms. Microbial biofilms have been proposed as selfimmobilized and self-regenerating catalysts for the production of chemicals. A concern is that the complex and dynamic nature of biofilms may cause fluctuations in their catalytic performance over time or may affect process reproducibility. An aerated continuous trickle-bed biofilm reactor system was designed with a 3 L structured packing, liquid recycling and pH control. Pseudomonas diminuta established a biofilm on the stainless steel structured packing with a specific surface area of 500 $m^2m^{-3}$ and catalyzed the oxidation of ethylene glycol to glycolic acid for over two months of continuous operation. A steady-state productivity of up to 1.6 $gl^{-1}h^{-1}$ was achieved at a dilution rate of 0.33 $h^{-1}$. Process reproducibility between three independent runs was excellent, despite process interruptions and activity variations in cultures grown from biofilm effluent cells. The results demonstrate the robustness of a catalytic biofilm on structured packing, despite its dynamic nature. Implementation is recommended for whole-cell processes that require efficient gas-liquid exchange, catalyst retention for continuous operation, or improved catalyst stability.

엇갈린 V-형 리브가 부착된 냉각유로에서의 열유동 수치해석 (Numerical Simulation of Flow and Heat Transfer in Cooling Channel with a Staggered V-shaped Rib)

  • 명현국;김광용
    • 대한기계학회:학술대회논문집
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    • 대한기계학회 2008년도 추계학술대회B
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    • pp.2448-2453
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    • 2008
  • The present study numerically investigates the flow and heat transfer characteristics of rib-induced secondary flow in a cooling channel with staggered V-shaped ribs, extruded on both walls. The rib-height-to-hydraulic diameter ration (h/$D_h$) is 0.17; the rib pitch-to-height ratio (p/h) equals 2.8; the Reynolds number is 50,000. Shear stress transport (SST) turbulence model is used as a turbulence closure. The present results are compared with those for a continuous V-shaped rib. Computational results show that, for average heat transfer rate the staggered V-shaped rib gives about 2.5 times higher values than the continuous V-shaped rib, while, for the streamwise pressure drop the former gives about 5 times higher values than the latter. Consequently, for the thermal performances, based on the equal pumping power condition, the staggered one gives about 2 times higher values than the continuous one. Also, for the staggered V-shaped rib, complex secondary flow patterns are generated in the duct due to the snaking flow in the streamwise direction, and more uniform heat transfer distributions are obtained.

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A geometric criterion for the element of the class $A_{1,aleph_0 $(r)

  • Kim, Hae-Gyu;Yang, Young-Oh
    • 대한수학회지
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    • 제32권3호
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    • pp.635-647
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    • 1995
  • Let $H$ denote a separable, infinite dimensional complex Hilbert space and let $L(H)$ denote the algebra of all bounded linear operators on $H$. A dual algebra is a subalgebra of $L(H)$ that contains the identity operator $1_H$ and is closed in the $weak^*$ operator topology on $L(H)$. For $T \in L(H)$, let $A_T$ denote the smallest subalgebra of $L(H)$ that contains T and $1_H$ and is closed in the $weak^*$ operator topology.

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Effect of Environmental pH on End Products, Fermentation Balances and Bioenergetic As-pects of Lactobacillus bulg-aricus in a Glucose-limited “pH Stat” Continuous Culture.

  • Rhee, Sang-Ki;Pack, Moo-Young
    • 한국미생물생명공학회:학술대회논문집
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    • 한국미생물생명공학회 1979년도 추계학술대회 심포지움
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    • pp.246.1-246
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    • 1979
  • A glucose-limited “pH-stat” continuous culture study of Lactobacillus bulgaricus NLS-4 in an anaerobic condition showed the marked effects of environmental pH on end products, fermentation blances and bioenergetic aspects of the organism. Lactic acid was the major end product of fermentation with minor products, such as acetic acid, formic acid and ethanol throughout the pH range tested. In acidic conditions below pH 6.5, a typi-cal pattern of homofermentation was revealed whereas in alkaline conditions, the metabolic pattern was changed from homofermentation to heterofermentation and led to acquire much energy. This metabolic change was likely due to the pH-dependent lactate dehydrogenase activity. Molar growth yields (Yglc=35.5-44.4) and YATP, $18.5\pm2.5$ in average which was 80% higher than the value ever postulated seemed to be accounted for less requirement of maintenance energy of the organism in the culture conditions.

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아민화 아크릴계 이온교환섬유의 폐수 중 Linear Alkylbenzene Sulfonate 흡착에 관한 연구 (Studies on the Adsorption of Linear Alkylbenzene Sulfonate from Waste Water by Fibrous Aminated Acrylic ion-Exchanger)

  • 황택성;박진원;김원종
    • 폴리머
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    • 제26권4호
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    • pp.516-522
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    • 2002
  • 4급 암모늄기를 관능기로 갖는 아민화 아크릴계 이온교환섬유를 이용하여 연속식 흡착공정 중 linear alkylbenzene sulfonate(LAS)의 흡착특성을 확인하였다. 아민화 아크릴계 이온교환섬유의 LAS흡착성능은 온도가 증가함에 따라 증가하였으며 $40^{\circ}C$에서 최적 흡착성능을 나타내었다. 또한 컬럼 베드 충진비(L/D)의 변화에 따른 LAS 이온의 흡착능은 L/D>2에서 최대 흡착능을 나타내었다. pH 변화에 따른 LAS이온 흡착능은 pH가 증가함에 따라 증가하는 경향을 나타내었고, pH 7에서 최대 흡착능을 나타내었다. 유속변화에 따른 LAS 흡착능은 유속이 증가할수록 낮아졌으며 농도가 높을수록 떨어졌다.

응집성 효모를 이용한 연속 알코올 발효 (Continuous Alcohol Fermentation by a Flocculating Yeast)

  • 남기두;이인기;조훈호
    • 한국미생물·생명공학회지
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    • 제19권5호
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    • pp.487-490
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    • 1991
  • 효모 재순환계에 의한 당밀의 연속발효를 하였다. 단계적으로 YPD배지 농도를 10g/l에서 183.5g/l로 증가시킨 후 최종 발효배지는 당밀로 하였다. 최고의 효모농도는 25g/l였고, 운전중 평균 효모농도는 23.5g/l으로 종래 회분식보다 3.4배 높았다. 최적 발효조건은 180g/l의 당밀배지를 공급하였을 때 교반속도 500rpm, 희석을 0.037$h^{-1}$였다. 이 조건을 645시간 연속 운전하였으며 최고 알코올 생산성은 4.9g$l\cdot h$로서 이때의 희석율은 0.091$h^{-1}$, 알코올 농도는 53.9g/l이었다.

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글리세롤 기반의 바이오에탄올 생산을 위한 연속생산반응기의 성능 비교 (Performance Comparison of Continuous Reactors for Bioethanol Production Based on Glycerol)

  • 이상준;송윤석;김성봉;강성우;한성옥;박철환;김승욱
    • KSBB Journal
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    • 제26권4호
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    • pp.328-332
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    • 2011
  • Ethanol production using glycerol as a carbon source was performed by Enterobacter aerogenes immobilized on calcium alginate beads. To improve the ethanol production, the optimal conditions such as loading amount of immobilized cells and glycerol concentration were investigated. The optimal loading amount of immobilized cells and glycerol concentration were 10 mL of calcium alginate bead and 10 g/L, respectively. Consequently, glycerol consumption rate, ethanol concentration and yield were 0.32 g/$L{\cdot}h$, 3.38 g/L and 0.43 g/g on the batch production, respectively. Continuous production of ethanol was successfully achieved using two types of immobilized cell reactors (continuous stirred tank reactor and packed bed reactor) from 10 g/L of glycerol. In the continuous stirred tank reactor, glycerol consumption, ethanol concentration, specific productivity and yield were 9.8 g, 4.67 g/L, 1.17 g/$L{\cdot}h$, 0.48 g/g, respectively. The concentration of produced ethanol was 38-44% higher comparison to batch fermentation, and continuous stirred tank reactor showed better performance than packed bed reactor.