• 제목/요약/키워드: filtration rate

검색결과 715건 처리시간 0.036초

PLASMA ALLANTOIN CONCENTRATION IN RESPONSE TO CHANGES IN NUTRITIONAL STATUS OF CALVES

  • Kagiyama, K.;Funaba, M.;Iriki, T.;Abe, M.
    • Asian-Australasian Journal of Animal Sciences
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    • 제9권2호
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    • pp.165-170
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    • 1996
  • Two experiments were conducted to search factor(s) affecting the plasma allantoin concentration in infant calves. In experiment 1, five male Holstein calves aged 1 week were given only milk replacer free from nucleic acids for 28 days Plasma allantoin concentration varied in a reverse proportion to daily amounts of milk replacer, and the concentration when calves received 750 g/d of milk replacer was significantly lower than that when they received 250 g/d. Contrary to plasma allantoin concentration, glomerular filtration rate(GFR) was directly proportional to daily amounts of milk replacer, leading to a constant filtration of allantoin across the glomeruli. Renal handling of allantion was also unaffected by the amount of milk replacer, resulting in the constant urinary excretion of allantoin. These results suggested that GFR, which was affected by the nutritional status, could affect plasma allantoin concentration. In experiment 2, the effect of age-related changes in nutritional status after weaning on GFR was examined in eight calves weaned at 5 weeks of age. The GFR expressed as body weight basis was lower immediately after weaning, but linearly increased up to the 19th week post-weaning. The present results suggested that the changes in GFR in response to nutritional status would be one of the possible causes of atypical plasma allantoin concentration immediately after weaning. We conclude that plasma allantoin concentration would not be a proper estimator of intestinal flow of microbial protein in cattle.

키토산 및 키틴 막에 의한 단백질의 친화 여과 크로마토그래피: 2. BSA 및 Lysozyme의 분리 (Affinity Filtration Chromatography of Proteins by Chitosan and Chitin Membranes: 2. Separation of BSA and Lysozyme)

  • 염경호;육영재
    • 멤브레인
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    • 제19권2호
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    • pp.113-121
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    • 2009
  • 실리카 입자를 기공 형성제로 사용하여 물리적 강도와 단백질 결합용량이 높은 다공성 키토산 및 키틴 친화 막을 제조하였다. 키토산 친화 막의 BSA 단백질 결합용량은 최대 21.8mg/mL이었으며, 키틴 친화 막의 lysozyme 효소 결합용량은 최대 26.1mg/mL이었다. 제조된 다공성 키토산 및 키틴 친화 막을 사용하여 단백질 용액의 loading 유량, loading 양 및 농도 변화에 따른 BSA와 lysozyme의 친화 막 여과 크로마토그래피 분리 실험을 수행하였다. 친화 막 여과 크로마토그래피 분리 실험을 통해 얻어진 loading/washing/elution의 단계로 구성된 일련의 크로마토그램으로부터 단백질 용출량과 결합수율을 구하였다. 키토산 및 키틴 친화 막에의 BSA 및 lysozyme 단백질의 결합량과 결합수율은 loading용액의 유량이 작을수록, 주입량 및 농도가 클수록 증가하였다. 이 결과로부터 실리카 입자를 기공 형성제로 사용하여 제조된 다공성 키토산 및 키틴 막은 단백질의 대규모 여과 크로마토그래피 분리를 위한 친화 막으로서 효과적인 활용이 기대된다.

고속 비디오 시스템을 이용한 정밀여과 막오염의 시각화 (Visualization of Microfiltraton Membrane Fouling by High Speed Video System)

  • 정건용;김래현
    • 멤브레인
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    • 제13권3호
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    • pp.174-181
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    • 2003
  • 본 실험에서는 십자형 흐름 정밀여과 모듈에서 분리막 투과시 막표면에 일어나는 입자층의 형성을 고속비디오 시스템으로 관찰하였다. 공칭세공이 0.2 {\mu}m$ 정밀여과막과 기공크기보다 휠씬 큰 100 내지 180{\mu}m$ 크기의 polyacryl-copolymer 0.05 wt%의 농도 용액을 제조하여 투과실험에서는 공급유속을 0.5, 0.75, 1.0, 1.25 그리고 1.5 cm/sec으로 변화시키면서 공급유속의 $20{\pm}3%$로 투과유량을 유지하였다. 공급유량이 증가할수록 입자가 보다 신속히 분리막 표면에 축적되는 것을 관찰할 수 있었고 공급유량이 낮은 0.5 cm/sec 에서는 입자층이 형성되지 않았다. 또한 입자층 형성 후 공급 유속을 1.88 cm/sec로 증가시키면 30초이내에 분리막 표면에 입자들이 대부분 제거됨을 확인하였다.

전오존이 세라믹 막의 차압에 미치는 영향 (Effect of Pre-ozonation on the Trans-membrane Pressure of Ceramic Membrane)

  • 배병욱
    • 대한환경공학회지
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    • 제33권9호
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    • pp.656-661
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    • 2011
  • 본 연구에서는 공경 $0.1{\mu}m$, 막여과 유속$3.0m^3/m^2{\cdot}d$의 국산 세라믹 막을 이용하여 음용수를 생산하는 기술에 대해 조사하였다. 세라믹 막의 성능 평가를 위해 $1m^3/d$ 규모의 pilot-scale 실험장치를 제작하였으며, 역세주기에 따른 차압변화와 전오존이 차압변화에 미치는 영향을 조사하였다. 차압상승률은 역세주기에 비례하여 증가하였으나, 전오존 주입을 통해 차압상승률을 낮출 수 있었다. 이 결과는 전오존이 파울링 감소에 효과가 있음을 의미한다. 1 mg/L의 전오존을 주입하고 5 min간 접촉하였을 때, 역세주기 1시간에서 차압상승률은 약 30% 감소하였다. 전오존 접촉시간을 5~15 min으로 변경하면서 운전한 결과, 접촉시간에 따른 차압상승률에는 차이가 없었다. 그러나, 차압상승률은 오존 주입농도가 증가하면 감소하는 경향을 보였다.

상하수처리를 위한 새로운 고효율 응집/여과 장치 (A Novel High Rate Flocculator/Filter in Water and Wastewater Treatment)

  • ;;권대영
    • 상하수도학회지
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    • 제19권2호
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    • pp.149-154
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    • 2005
  • Conventionally used flocculation tanks require large space and high energy requirement for mixing. Static flocculators using gravel bed filter operate at a lower flow rate ($5-10m^3/m^2{\cdot}h$). Further, the cleaning of this system is difficult. A novel high rate static flocculator/filter developed at UTS packed with buoyant media such as polystyrene, polypropylene has been found to operate at higher filtration rates (30-45 $5-10m^3/m^2{\cdot}h$). They can easily be cleaned with minimal energy. Detailed experiments conducted with an artificial kaolin clay solution show that buoyant media is an excellent static flocculator in producing uniform filterable microflocs (12-15 m) even when it is operated at a high rate of 30-40 m/h. Detailed filtration experiments were conducted in a wastewater treatment plant to treat the biologically treated effluent with a floating media of depth of 120 cm. This filter was able to remove majority of phosphorus and remaining solids. It reduced significantly the fecal coliforms and fecal streptoccoci, thus requiring less amount of chlorine for disinfection. The advantage of this system is the low energy and water requirement for cleaning of filter bed. The periodic backwash adopted 30 seconds air and water and 30 seconds water cleaning every 90 minutes filter operation. Thisis equivalent to 1-2% of filtered water production. Mechanical cleaning system on the other hand, requires very low energy requirement (<1% of filtered water production).

맥동식 침전지에서 맛·냄새 유발물질 제거 특성 (Removal Property of Taste and Odor Causing Material in Pulsator Clarifier)

  • 정일용;차민환
    • 한국물환경학회지
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    • 제27권1호
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    • pp.104-109
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    • 2011
  • The removal efficiencies of 2-methylisoborneol (MIB) and geosmin were investigated to reveal removal characteristics of typical organic compounds causing disagreeable taste and odor at the conventional water treatment plant installed with pulsator clarifier patented by the French company $Degr{\acute{e}}mont$. The injection rate of Powdered Activated Carbon (PAC) into water was changed step wisely as we conducted jar tests in the laboratory and water treatment in the actual plant. 2-MIB concentration decreased linearly while geosmin did exponentially along with the injection rate of PAC at our jar tests. The removal efficiency of geosmin by PAC injection was considerably higher than that of 2-MIB. In the real pulsator clarifier, 2-MIB concentration started decreasing as the injection rate reached up to 10 mg/L of PAC. On the other hand, the concentration of geosmin in water decreased proportional to the injection rate of PAC. In the sand filtration, removal efficiencies of 2-MIB and geosmin on July were much higher than those on March. It was carefully suggested beforehand and found afterwards that general microorganisms notably existed in the sand filter with no chlorine in filter influent and backwash water and the sand filter biologically activated removed much more odor compounds. It was considered as the reason why the removal efficiency of 2-MIB and geosmin was increased. The microbial activity maybe increased in summer with water temperature rising and low filtration rate possibly increased contact time between odor compounds and general microorganisms.

신안해저 고대선의 과학적 보존처리(IV)

  • 최광남;모운종;김익주;정양호;김민욱
    • 보존과학연구
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    • 통권7호
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    • pp.56-86
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    • 1986
  • The aim of this study is to scientifical conservation for the Sin An Ship. The test object is Pinus massoniana and Cunninghamia lanceolata of Sin An Ship's timber .Comtrast object is water soaked fresh wood of Pinus densiflora and Cryptomeria japonica The results were as follows.1. M. C is 280.9% in high degraded Planking board,237.5% in low degraded Planking board,158.6% in fresh wood of Pinus densiflora,222.6% in Bulkhead167.3% in fresh wood of Cryptomeria japonica2. Absorption rate of P.E.G is good at heating condition ($55∼60^{\circ}C$), especially in highdegraded wood.3. The dimensional change of wood during air drying is somewhat shrinked That's 7.22% in low degraded Planking board9.8% in high degraded Planking board and 4.11% in water soaked Pinus densiflora.4. The dimensional change of wood during P.E.G treatment is mostly swollen of wery small quantity.5. Salinity in desalinization tank showed below 50 p.p.m. It's indicate the end of desalinization treatment.6. Filtration with filter paper was possible up to 40% concentration only. Key words :M.c ; Moisture Content, Absorption rate, Dimension change, Salinity, Filtration.

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측뇌실내(側腦室內) Nalprphine의 가토신장기능(家兎腎臟機能)에 미치는 영향(影響) (Influence of Intracerebroventricular Nalorphine on the Renal Function of the Rabbit)

  • 국영종;최봉규;김흥규
    • 대한약리학회지
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    • 제16권2호
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    • pp.1-7
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    • 1980
  • As it has been reported that morphine induce antidiuresis, and antinatriuresis along with decrease in renal hemodynamics when given intracerebroventricularly[ivt], the renal action of nalorphine, a partial antagonist of morphine action, and its influence upon the morphine action were investigated in this study. $10{\mu}g/kg$ of nalorphine given into the lateral ventricle of the rabbit brain tended to decrease renal plasma flow and glomerular filtration rate and increase the reabsorption of free water in the tubules. $100{\mu}g/kg$ ivt significantly decreased urine flow rate and increased free water reabsorption, and tended to increase electrolyte excretion in spite of decrease in renal plasma flow and glomerular filtration, suggesting that ADH also involved in the antidiuresis. Morphine hydrochloride, $10{\mu}g/kg$, ivt, produced marked decrement in renal hemodynamics along with decreased excretions of sodium, potassium and water, and these morphine actions were alleviated by nalorphine given 20 min later. The natriuretic action of ivt nalorphine manifested itself uninfluenced by the morphine. These observations indicate that nalorphine ivt produces renal actions similar to those of morphine, though less potent, and that it can antagonize the latter action. It is suggested that morphine influences renal hemodynamics through nerve by stimulating the 'morphine receptor' in the brain, whereas nalorphine liberates ADH by the agonistic action on the 'nalorphine receptor'.

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