• 열처리공학회지
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• 제34권6호
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• pp.272-280
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• 2021

The influence of acetylene flow rates on the carburizing behavior of an AISI 4115 steel in 1 ton-class mass production-type vacuum carburizing furnace has been studied through microstructure, carbon concentration, hardness analyses. The AISI 4115 steels were carburized with various flow rates (20, 32.7, 60 l/min) and locations in the furnace (top, center, bottom) at 950℃. The acetylene flow rate played an important role in controlling the carburizing properties of carburized samples, such as effective case depth and uniformity carburizing according to location in the furnace. At an acetylene flow rate of 20 l/min, the carburized samples had a shallow average hardened layer (0.645 mm) compared to the target hardening depth (1 mm) due to low carbon flux and spatial uniformity of carburization (17.8%) in the furnace. At a flow rate of 60 l/min, the carburized samples showed an average hardened layer (1.449 mm) deeper than the target hardening depth and had the spatial uniformity of carburization (98.8%). In particular, at a flow rate of 32.7 l/min, the carburized samples had an average hardened layer (1.13 mm) close to the target hardening depth and had the highest carburizing uniformity (99.1%). As a result, an appropriate flow rate of 32.7 l/min was derived to satisfy the target hardening depth and to have spatial uniform hardened layer in the furnace.

• Ocean and Polar Research
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• 제32권3호
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• pp.229-236
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• 2010

A study was conducted to investigate the effect of water temperature and photoperiod on the oxygen consumption of the fasting juvenile Pacific cod Gadus macrocephalus (mean body weight 79.9${\pm}$2.0 g) in order to quantify metabolic response of the species under given conditions. The oxygen consumption rate (OCR) of G. macrocephalus was measured under a combination of four different water temperatures (7, 10, 13 and $16^{\circ}C$) and three different photoperiods (24L:0D, 12L:12D and 0L:24D) with an interval of 5 minutes over a 24-hour period using a closed recirculating respirometer. Three replicates were set up in each treatment. OCRs increased with increased water temperatures under all photoperiod conditions (P<0.001). Mean OCRs at 7, 10, 13 and 16oC ranged from 793.7~1108.4, 1145.7~1570.3, 1352.8~1742.5 and 1458.2~1818.6 mg $O_2$ $kg^{-1}$ $h^{-1}$, respectively. Under all water temperature conditions except $7^{\circ}C$ (P<0.001), mean OCRs of G. macrocephalus were the highest in continuous light (24L:0D) followed by 12L:12D and 0L:24D photoperiods. Mean OCRs of fish exposed to the 12L:12D photoperiod were significantly higher during the light phase than during the dark phase under all temperature conditions (P<0.001). $Q_{10}$ values ranged from 3.19~5.13 between 7 and $10^{\circ}C$, 1.41~1.74 between 10 and $13^{\circ}C$ and 1.15~1.35 between 13 and $16^{\circ}C$, respectively. Based on overall results, water temperature, photoperiod and their combinations exerted a significant influence on the metabolic rate of juvenile cod. This study provides empirical data for estimating the amount of oxygen demand and managing the culture of cod under the given water temperatures and photoperiods.

• Environmental Engineering Research
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• 제20권4호
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• pp.347-355
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• 2015

The growth kinetics of phototrophic microorganisms can be controlled by the light irradiance, the concentration of an inorganic nutrient, or both. A multi-component kinetic model is proposed and tested in novel batch experiments that allow the kinetic parameters for each factor to be estimated independently. For the cyanobacterium Synechocystis sp. PCC6803, the estimated parameters are maximum specific growth rate $({\mu}_{max})=2.8/d$, half-maximum-rate light irradiance $(K_L)=11W/m^2$, half-inhibition-rate light irradiance $(K_{L,I})=39W/m^2$, and half-maximum-rate concentration for inorganic carbon $(K_{S,Ci})=0.5mgC/L$, half-maximum-rate concentration for inorganic nitrogen $(K_{S,Ni})=1.4mgN/L$, and half-maximum-rate concentration for inorganic phosphorus $(K_{S,Pi})=0.06mgP/L$. Compared to other phototrophs having ${\mu}max$ estimates, PCC6803 is a fast-growing r-strategist relying on reaction rate. Its half-maximum-rate and half-inhibition rate values identify the ranges of light irradiance and nutrient concentrations that PCC6803 needs to achieve a high specific growth rate to be a sustainable bioenergy source. To gain the advantages of its high maximum specific growth rate, PCC6803 needs to have moderate light illumination ($7-62W/m^2$ for ${\mu}_{syn}{\geq}1/d$) and relatively high nutrient concentrations: $N_i{\geq}2.3 mgN/L$, $P_i{\geq}0.1mgP/L$, and $C_i{\geq}1.0mgC/L$.

• 약학회지
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• 제27권4호
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• pp.249-256
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• 1983

When the reaction rate constant k of phospholipase D on liposome was measured by the ANS fluorometry, k of phospholipase D on DMPC liposome which was made of L-$\alpha$-PI, cholesterol and L-$\alpha$-PS decreased than that of phospholipase D on DMPC liposome with cholesterol or with PI and cholesterol. Optimal $Ca^{2+}$ concentration, the most important factor on effect of phospholipase D, also decreased to 1mM, as compared with 10mM and 60mM respectively when cholesterol and PI were added, and cholesterol only was added. The change of cholesterol Mol% had a great influence on k value of phospholipase D. But in case of addition of L-$\alpha$-PS to cholesterol, the influence was relatively diminished.

• 한국미생물·생명공학회지
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• 제25권1호
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• pp.68-74
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• 1997

The conversion of D-sorbitol to L-sorbose by Gluconobater suboxydans was analyzed, and continuous production of L-sorbose was carried out in immobilized cell reactors. L-Sorbose production by high densities of resting cells was more effective than by conventional batch fermentations. Sorbitol dehydrogenase, an enzyme converting D-sorbitol to L-sorbose, did not suffer from substrate inhibition, but from product inhibition. When L-sorbose production was carried out with Ca-alginate-immobilized cells, about 60 g/l of L-sorbose was obtained. On the other hand, when the corn steep liquor (CSL) concentration of medium was reduced to 0.08%, 80 g/l of L-sorbose was obtained. Outgrowth inside the immobilized carriers was thought to block the pores of the carriers so that substrate could not easily diffuse through the carriers. Continuous production of L-sorbose was well accomplished in a bubble column reactor, and 6. 5 g/l.h of productivity and 81.2% of yield were obtained at a substrate feeding rate of 0.08h$^{-1}$ under the optimum conditions with carrier volume of 55% and aeration rate of 3 vvm.

• 설비공학논문집
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• 제7권4호
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• pp.681-693
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• 1995

A new set of capillary tube selection charts for R-22 is proposed. The set of charts takes into account of the roughness effect on the mass flow rate. For this purpose, a set of numerical model is developed and a series of experiments is conducted to verify the numerical model. A numerical model is used to calculated the mass flow rate for several sets of tube diameter, length, inlet pressures and degree of subcooling. The outlet of the tube is controlled to be at critical condition. The experimental flow rate is compared with calculated values. The calculated values are consistently less than the experimental ones except for the flow rate range below 40kg/hr. The deviation is within 10---. Based on the nunmerical model and results of experiments, the set of capillary tube selection charts for R-22 is constructed. The set of charts consists of standard capillary tube chart(L=2030mm, d=1.63mm, ${\varepsilon}=2.5{\mu}m$), non -standard flow factor(${\phi}_1$) chart, and non-standard roughness factor(${\phi}_2$) chart. The mass flow rate, flow factor, and the roughness factor are defined respectively as; $\dot{m}={\phi}_1{\phi}_2\dot{m}_{standard}\\{\phi}_1=\frac{\dot{m}(L,\;d,\;\varepsilon_{standard})}{\dot{m}_{standard}(L_{standard},\;d_{standard},\;{\varepsilon}_{standard})}\\{\phi}_2=\frac{\dot{m}(L_{standard},\;d_{standard},\;{\varepsilon})}{\dot{m}_{standard}(L_{standard},\;d_{standard},\;{\varepsilon}_{standard})}$.

• 한국축산시설환경학회지
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• 제19권2호
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• pp.191-196
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• 2013

In this study, the mixture ratio included 20% (GLY 20), 40% (GLY 40), and 60% (GLY 60) based on VS with the control group (GLY 0) with no crude glycerin added. Maintaining stable pH, GLY 20 and GLY 0 showed the highest total output of biogas (1.24 L/L/d) and methane(0.78 L/L/d) as its volatile solids reduction rate was 53.56%. In case of GLY 40 and GLY 60, their pH was rapidly reduced after seven days of the study, so that their anaerobic digestion was all stopped.In the results of the study, it is desirable to add crude glycerin less than 20%, and it would be necessary to have the future researches on more detailed organic loading rate of each ratio, and analysis on economic feasibility.

• 미생물학회지
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• 제46권3호
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• pp.233-239
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• 2010

Bacillus subtilis에 존재하는 DEAD-box RNA helicase에 대한 유전자 상동성 검색을 통해 yqfR, yfmL, ydbR, deaD 의 4종류의 유전자를 확인하였고 이들 유전자 각각의 결손 돌연변이체를 제조하였다. 이들 돌연변이체들의 특성을 알아보기 위하여 LB 배양액을 사용하여 여러 온도에서의 생장 속도를 조사하였다. LB 배양액에서 $37^{\circ}C$의 생장 결과 ydbR 결손 균주가 다소 생장이 느려지나($T_d$=53 min) 다른(yqfR, yfmL, deaD) 결손 돌연변이체들은($T_d$=30-40 min) 결손이 없는 야생형 균주 CU1065와($T_d$=32 min) 유사하였다. 반면에 $22^{\circ}C$에서의 생장은 CU1065 ($T_d$=102 min)에 비해 yqfR ($T_d$=151 min), yfmL ($T_d$=214 min), ydbR ($T_d$=343 min) 결손 균주 순으로 생장속도가 느린 저온 민감성을 보인다. deaD의 $22^{\circ}C$에서의 생장 속도는 ($T_d$=109 min) CU1065와 ($T_d$=102 min) 매우 유사하여 저온 민감성을 보이지 않았다. 그리고 이들 유전자들의 이중, 삼중, 사중의 결손 균주들을 제조하였고, 여러 온도에서 ($42^{\circ}C$, $37^{\circ}C$, $22^{\circ}C$) LB 배양액을 사용하여 생장 속도를 측정 하였다. 다중 결손은 단일 결손보다 더 심한 저온 민감성을 보이며, 이중 결손의 경우, ydbR과 yfmL의 결손이 다른 조합의 결손보다 보다 큰 저온 민감성을 나타내었다 ($T_d$=984 min). 이러한 저온 민감성은 E. coli의 csdA 혹은 srmB 결손의 결과와 유사하며 리보솜 조립과 관련이 있는 생리적 기능으로 보인다.

• 대한환경공학회지
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• 제38권6호
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• pp.279-290
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• 2016

중화하지 않은 주정폐수를 처리할 때 상향류식 혐기성반응조에 전극을 배치한 생물전기화학반응조의 성능을 UASB 공정과 비교하였다. UASB 공정은 유기물부하율 4.0 g COD/L.d 이하에서 pH, VFA 및 알카리도 등에 있어서 안정한 상태를 유지하였지만, 4.0 g COD/L.d 이상의 유기물부하율에서는 불안정하였다. 그러나, 생물전기화학 반응조는 UASB 반응조에 비하여 유기물부하율 배가시 상태변수들의 변동폭이 작았으며, 빠르게 정상상태로 회복하였다. 생물전기화학 반응조는 4.0-8.0g COD/L.d의 높은 유기물부하율에서 상태변수들이 UASB 반응조에 비하여 안정하였으며, 유기물부하율 8.0 g COD/L.d에서 비메탄발생율(2,076mL $CH_4/L.d$), 바이오가스의 메탄함량(66.8%) 그리고 COD 제거율(82.3%) 등의 측면에서 UASB 반응조보다 우수하였다. 생물전기화학 반응조의 메탄수율은 유기물부하율 4.0 g COD/L.d에서 약 407mL/g $COD_r$로 최대값을 보였으며, 이 값은 UASB의 282mL/g $COD_r$보다 크게 높았다. 중화하지 않은 산성 주정폐수를 처리하는 생물전기화학 반응조의 전극반응에서 율속단계는 산화전극반응이었으며, 전극반응은 높은 유기물부하율에서 pH에 의해서 크게 영향을 받았다. 생물전기화학 반응조는 유기물부하율 4.0 g COD/L.d에서 99.5%의 최대에너지효율을 보였다. 중화하지 않은 산성 주정폐수를 처리하는 생물전기화학 반응조는 UASB 공정보다 진보된 고율 혐기성 기술이 될 수 있다.

• 상하수도학회지
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• 제18권1호
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• pp.15-21
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• 2004

The purpose of this research was to investigate loading rate of influent for acidogenic fermentation. Laboratory batch experiments were conducted, at $35^{\circ}C$, HRT 18hr, pH 6 and used 3.5L reactor. Loading rate of influent was varied 2.0 to 4.0g VSS/L, TOA concentration is decreased according to increasing loading rate Over 2.5g VSS/L. When loading rate is 2.0g VSS/L, hydrolysis percentage show the maximum value of 87%. Most of SCFA is consist of HAc, HPr, I-HBu and MBu. HAc concentration is 5,233mg/L in the 2.0g VSS/L condition. So, for this study, we think that limiting loading rate is 2.5g VSS/L. SCFA species was investigated to HAc, HPr, I-HBu and n-HBu during our studying. HAc/SCFA ratio is about 89.3%, SCFA production rate is highest to $1,104mg\;COD/L/d{\cdot}gPCOD$ for 2.0g VSS/L loading rate.