• 대한환경공학회지
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• 제31권9호
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• pp.817-824
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• 2009

여과공정에서 수리적 충격부하로 인한 탁질누출을 방지하기 위하여, 여과지 유입량 변화에 대응하여 여과지 운영지수를 변화시키면서 여과수의 탁도 및 입자수를 고찰하였다. S 정수장은 여과지 유입량 최대/최소의 비가 2.2였으며, 이에 따라 여과속도도 변동하였다. S 정수장에서는 여과속도 변동 최소화를 위하여 여과유입수량 변동에 따라 여과지수를 변동시켰다. 여과지 유입유량 변화에 따라 가동, 휴지, 재가동을 반복하였을 경우 탁질누출은 심하지 않았다. 여과가동 누계시간이 10 h 이전이나 50 h 이후에 재가동시는 탁질누출현상이 일부 발견되었다. 이런 현상은 여재의 숙성이 충분하지 않거나 입자물질의 부착량 과다에 기인할 수 있다. 따라서 여과지를 재가동할 때는 누계여과지속시간이 10 h 이상, 50 h 미만인 여과지를 선택하는 것이 효율적인 것으로 조사되었다. 여과지 유입유량 변동에 따른 여과지수 변동은 UFRV 향상을 위한 방법으로 판단된다.

• 한국식품영양과학회지
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• 제32권5호
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• pp.745-751
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• 2003

밀 단백질에 효소가수 분해할 때 생산되는 peptide의 항균활성과 천연항균제로서의 이용가능성을 검토하기 위하여 실험을 행하였다. 밀 단백질에 7종의 단백질가수분해효소를 작용시켜 생성된 가수분해물의 항균활성을 측정하고 한외여과, membrane filtration, HPLC를 이용하여 항균성 peptide를 분리 정제한 후 분자량과 아미노산 결합순서를 측정한 결과는 다음과 같다. 밀 단백질에 7종의 단백질 분해효소를 적용시켜 제조한 가수분해물중 Asp. saito protease를 적용시켜 얻어진 peptide만이 항균활성을 나타내었다. Asp. saito protease는 37$^{\circ}C$, pH 6.0에서 작용시킨 경우에 항균활성이 가장 높았으며, 5$0^{\circ}C$ 이상에서는 활성을 나타내지 않았다. 밀단백 효소가수분해물은 membrane filtration에 의하여 분자량 1,000~3,000에서 항균활성이 나타났다. Membrane filtration으로 얻어진 항균활성분획을 HPLC로 분리한 결과 retention time 31.1~31.8 min에서 항균활성을 나타내었다. 밀단백 효소가수분해물은 121$^{\circ}C$에서 15분간 가열하여도 효소활성이 유지되는 매우 안정한 화합물이었다. 항균활성분획을 MALDI-mass로 질량을 분석한 결과 1,633이었다. 항균성 peptide의 아미노산 결합순서는 cysteine, glycine, prolin, valine, valine, alanine, alanine, arginine의 순서였다.

• 농업과학연구
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• 제29권2호
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• pp.78-90
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• 2002

밀 단백질에 효소가수분해 할 때 생산되는 peptide의 항균활성과 천연항균제로서의 이용가능성을 검토하기 위하여 실험을 행하였다. 밀 단백질에 7종의 단백질가수분해효소를 작용시켜 생성된 가수분해물의 항균활성을 측정하고 한외여과, membrane filtration, HPLC를 이용하여 항균성 peptide를 분리 정제한 후 분자량과 아미노산 결합순서를 측정한 결과는 다음과 같다. 밀 단백질에 7종의 단백질 분해효소를 적용시켜 제조한 가수분해물중 Asp. saito protease를 적용시켜 얻어진 peptide 만이 항균활성을 나타내었다. Asp. saito protease는 $37^{\circ}C$, pH 6.0에서 작용시킨 경우에 항균활성이 가장 높았으며, $50^{\circ}C$ 이상에서는 활성을 나타내지 않았다. 밀단백 효소가수분해물은 membrane filtration에 의하여 분자량 1,000~3,000 에서 항균활성이 나타났다. Membrane filtration으로 얻어진 항균활성분획을 HPLC로 분리한 결과 retention time 31.1~31.8 min에서 항균활성을 나타내었다. 밀단백 효소가수분해물은 $121^{\circ}C$에서 15분간 가열하여도 효소활성이 유지되는 매우 안정한 화합물이었다. 항균활성분획을 MALDI-mass로 질량을 분석한 결과 1,633이었다. 항균성 peptide의 아미노산 결합순서는 cysteine, glycine, prolin, prolin, prolin, valine, valine, alanine, alanine, arginine 의 순서였다.

• 한국항해항만학회:학술대회논문집
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• 한국항해항만학회 2006년도 춘계학술대회 및 창립 30주년 심포지엄(논문집)
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• pp.221-226
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• 2006

본 연구는 밸러스트수를 처리하기 연속여과 공정에서 역세척 조건에 따른 막오염 특성을 관찰하였다. 선박에서 발생되는 밸러스트수를 전처리하기 위하여 수중에 포함되어 있는 입자상 오염물질과 수중생물체를 자동역세척 여과장치를 이용하여 처리한 결과 클 나타내었다. 밸러스트수를 처리하기 위한 전처리의 장점은 입자상의 오염물질을 제거하여 후처리공정의 처리효과를 높이는데 있다. 처리장치의 용량은 $10m^3/h$ 이다. 테스트 결과 역세척 주기와 역세척 지속시간은 전체 시스템의 효율과 역세척 효율을 고려하여 역세척 지속시간은 6초가 적당한 것을 나타났으며, 도출된 지속시간을 기준으로 하여 95%의 제거효율은 얻었다. 1시간동안의 역세척 주기가 필요하였다. 여과처리를 통하여 $70{\mu}m$ 이상의 식물성 플랑크톤과 동물성 플랑크톤을 포함하는 수중생물체를 제거할 수 있었다. 실험결과를 통하여 밸러스트수 처리에 적용 가능한 기술임을 알 수 있었다. 이 연구에서 밸러스트수 처리를 위한 우수한 여과처리시스템임을 보여 주었다.

• 상하수도학회지
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• 제33권1호
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• pp.9-16
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• 2019

The algal blooms in stagnant streams and lakes have caused many problems. Excessive algae leads to disturbance of ecosystem and overload of water treatment processes. Therefore, phosphorus(P), source of algal blooms, should be controlled. In this study, a filtration trench has been developed to convert dissolved phosphorus into hydroxyapatite(HAP) so that it could be crystallized on the surface of 'phosphorus removal granular material'; and residual particulate phosphorus could be removed by additional precipitation and filtration. The front and rear parts of filtration trench consisted of 'phosphorus removal granular material contact bed' and 'limestone filtration bed', respectively. As a result of the column test using phosphorus removal granular material and limestone serially, $PO_4-P$ was removed more than 90% when EBCT(empty bed contact time) of the contact bed was over 20 minutes; and T-P represented 60% of removal efficiency when total EBCT was over 1.5 hours. The results of column tests to figure out the sedimentation characteristics showed that more than 90% of particulate phosphorus could be removed within 24 hours. It was necessary to optimize the filtration part in order to increase removal efficiency of T-P additionally. Also, it was confirmed through the simulation of Visual MINTEQ that most of particulate phosphorus in the column tests is the form of HAP. Based on the results of the study, it could be suggested that the design parameters are over 0.5 hour of EBCT for phosphorus removal granular material contact bed and over 1.5 hours of EBCT for limestone filtration bed.

• 상하수도학회지
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• 제13권2호
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• pp.41-46
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• 1999

Backwashing is an important process for the efficient operation of granular filters, and the efficiency of the surface washing among the backwashing processes can affect the filtrations rate and filter run-time. In this study, the efficiency of surface washing is evaluated using real filters for three cases: with surface washing (with and without drainage of water to the surface of filter bed) and without surface washing. As a result, in the case of adopting both the drainage and surface washing, the filter of which condition is initially worse than those of the other filters shows improvement in head-loss development, filtration velocity, filter run-time, and total filtration volume. On the other hand, the conventional method of surface washing rarely has an effect on the filter washing.

• 상하수도학회지
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• 제21권6호
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• pp.717-726
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• 2007

Fully-grown flocs in a mixing tank of membrane filtration with dead-end membrane are ruptured while passing through a pump and the ruptured flocs are aggregated again in a Membrane-Feed-Pipe (MFP). To look at more details, this study tries to relate the reaggregation to a parameter of mixing intensity in MFP, i.e., G-value. The G-value is a function of Reynolds number, pipe diameter, friction factor and average velocity in MFP. To deal with polydispersity condition, we develop a representative particle size called in this study EDPD (Effective Diameter for Polydispersity condition in Dead-end filtration). The experimental results show that as the G-value increases, the EDPD decreases and also the cake resistance increases. Through comparison between EDPD and cake resistance, these results show that cake resistances are controlled by reaggregation phenomenon in MFP. The effect of detention time in MFP, however, does not affect the reaggregation of the broken flocs as G-values are increased.

• 상하수도학회지
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• 제21권4호
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• pp.503-508
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• 2007

Small scale D-water treatment plant(WTP) where has slow sand filtration was using raw water containing high concentration of manganese (> 2mg/l). The raw water was pre-chlorinated for oxidation of manganese and resulted in difficulty for filtration. Thus, sometimes manganese concentration and turbidity were over the water quality standard. Two stage rapid manganese sand filtration pilot plant which can treat $200m^3/d$ was operated to solve manganese problem in D-WTP. The removal rate of manganese and turbidity were about 38% and 84%, respectively without pH control of raw water. However, when pH of raw water was controlled to average 7.9 with NaOH solution, the removal rate of manganese and turbidity increased to 95.0% and 95.5%, respectively and the water quality of filtrate satisfied the water quality standard. Manganese content in sand was over 0.3mg/g which is Japan Water Association Guideline. The content in upper filter was 5~10 times more than that of middle and lower during an early operation but the content in middle and lower filter was increased more and more with increase of operation time. This result means that the oxidized manganese was adsorbed well in sand. Rapid manganese sand filter was backwashed periodically. The water quality of backwash wastewater was improved by sedimentation. Thus, turbidity and manganese concentration decreased from 29.4NTU to 3.09NTU and from 1.7mg/L to 0.26mg/L, respectively for one day. In Jar test of backwash wastewater with PAC(Poly-aluminum chloride), optimum dosage was 30mg/L. Because the turbidity of filtrate was high as 0.76NTU for early 5 minute after backwash, filter-to-waste should be used after backwash to prevent poor quality water.

• 한국지반공학회:학술대회논문집
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• 한국지반공학회 2009년도 춘계 학술발표회
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• pp.154-163
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• 2009

The groutability depends on the properties of the grout, its injection processes, and on the mechanical properties of the soil formation. During the process of pouring cement-based grouting into a porous medium, a variation with time occurs in the viscosity of grout suspension. In addition the particle filtration phenomenon will limit the expansion of the grouted zone because cement particles are progressively stagnant within the soil matrix. In this paper, a closed-form solution was derived by implementing the mass balance equations and the generalized phenomenological filtration law, which can be used to evaluate the deposition of cement-based grout in the soil matrix. The closed-form solution relevant to a particular spherical flow was modified by a step-wise numerical calculation, considering the variable viscosity caused by a chemical reaction, and the decrease in porosity resulting from grout particle deposition in the soil pores. A series of pilot-scale chamber injection tests was performed to verify that the developed step-wise numerical calculation is able to evaluate the injectable volume of grout and the deposition of grout particles. The results of the chamber injection tests concurred well with that of the step-wise numerical calculation. Based on the filtration phenomenon, a new groutability criterion of cement-based grout in a porous medium was proposed, which might facilitate a new insight in the design of the grouting process.

• The Korean Journal of Physiology
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• 제20권1호
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• pp.103-124
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• 1986

Since it has been suggested that atrial receptor may be involved in the mechanism of extracellular volume regulation, it was shown that the granularity of atrial cardiocytes can be changed by water and salt depletion, and that an extract of cardiac atrial tissue, when injected intravenously into anesthetized rats, was shown to cause a large and rapid increase in renal excretion of sodium. Various natriuretic peptides were isolated and synthetized, and the effects were investigated by many workers. Most studies, however, have been carried out under anesthesia and there have teen some controversies over direct effect of the factor on the renal function. Therefore, it was attempted in this study to access the effects of an atrial extract and a synthetic natriuretic factor in unanesthetized rabbits. Intrarenal arterial infusion of atrial extract caused a rapid increase of urinary volume and excretion of sodium. Glomerular filtration rate and renal plasma flow were both increased with no change in filtration fraction. The ventricular extract produced no change in urinary excretion of electrolytes, nor in renal hemodynamics. Intrarenal infusion of synthetic atrial natriuretic factor caused increases of renal excretory rate of sodium, chloride and potassium, and $FE_{Na}$. Glomerular filtration rate, renal plasma flow increased. And free water clearance also increased. Accentuated excretory function correlated well with increased glomerular filtration rate and renal plasma flow during infusion and for 10 minutes following the cessation of the infusion. Renin secretion rate decreased during constant infusion of atrial natriuretic factor. However, no correlation was found with the changes in glomerular filtration rate, renal plasma flow, or urinary excretion of sodium. These results suggest that atrial extract or atrial natriuretic factor induces changes in renal hemodynamics, as in excretion of electrolytes either indirectly through hemodynamic changes or directly by inhibiting tubular reabsorption. At the same time, renin secretory function is affected by the factor possibly through an unknown mechanism.