• 제목/요약/키워드: In-water cleaning

검색결과 652건 처리시간 0.026초

수계세정제의 계면활성제 종류에 따른 물성, 세정성 및 유수분리 영향 연구 (Effect of surfactant types in aqueous cleaning agents on their physical properties, cleaning ability and oil-water separation)

  • 박선우;차안정;김현탁;김한성;배제흠
    • 청정기술
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    • 제9권1호
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    • pp.9-21
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    • 2003
  • CFC-113, 1,1,1-TCE는 오존파괴물질로 선진국에서는 이미 사용이 전면 규제되고 있고 MC, TCE는 유해성 또는 발암성물질로 판명되어 일부사업장에서 제한적으로 사용되고 있다. 그러므로 세정성이 좋고 환경/안전성이 우수한 대체세정제를 개발하여 사용하거나 기존 개발된 세정제 중에서 우수한 세정제를 선정하여 사용하는 것이 필요한 실정이다. 대체세정제로는 수계세정제가 환경성과 경제적면에서 유망한 것으로 평가받고 있어 많은 사업장에서 사용될 전망이다. 본 연구에서는 환경친화적인 수계세정제를 개발하기 위하여 수계세정제의 주요성분인 여러 형태의 계면활성제를 선정하여 이들의 물성, 거품성, 오염물 종류에 따른 세정성, 유수분리성을 평가하여 비교하였다.

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Autopsy of Nanofiltration membrane of a decentralized demineralization plant

  • El-ghzizel, Soufian;Jalte, Hicham;Zeggar, Hajar;Zait, Mohamed;Belhamidi, Sakina;Tiyal, Fathallah;Hafsi, Mahmoud;Taky, Mohamed;Elmidaoui, Azzedine
    • Membrane and Water Treatment
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    • 제10권4호
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    • pp.277-286
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    • 2019
  • In 2014, the first demineralization plant, using nanofiltration (NF) membrane coupled with renewable energies was realized at Al Annouar high school of Sidi Taibi, Kenitra, Morocco. This project has revealed difficulties related to the membrane performances loss (pressure increase, flux decline, poor water quality of the produced water and increase of energy consumption), as consequences of membrane fouling. To solve this problem, an autopsy of the membrane was done in order to determine the nature and origin of the fouling. The samples of membrane and fouling were then analyzed by scanning electron microscopy using a scanning electron microscope (SEM) connected with an energy dispersive X-ray (EDX) detection system and X-ray diffractometer (XRD). Moreover, three cleaning solutions (hydrochloric acid, nitric acid and sulfuric acid) were tested and assessed in a single cleaning step to find the suitable one for the fouled membrane to regain its initial permeability and performances. The analysis of the experimental results showed that the fouling layer is mainly composed of calcium carbonate (inorganic fouling). Results showed also that the permeability is improved by the hydrochloric acid cleaning (pH=3) with a cleaning efficiency of 93%. Cleaning efficiency did not exceed 75 % with nitric acid (pH=3) and 40 % with sulfuric acid (pH=3).

세라믹 막여과 정수처리 공정에서 유입수질 및 막여과유속이 막오염 형성에 미치는 영향 (Effects of membrane fouling formation by feed water quality and membrane flux in water treatment process using ceramic membrane)

  • 강준석;박서경;이정준;김한승
    • 상하수도학회지
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    • 제32권2호
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    • pp.77-87
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    • 2018
  • In this study, the effects of operating conditions on the formation of reversible and irreversible fouling were investigated in the filtration using ceramic membrane for water treatment process. The effect of coagulation pretreatment on fouling formation was also evaluated by comparing the performance of membrane filtration both with and without addition of coagulant. A resistance-in-series-model was applied for the analysis of membrane fouling. Total resistance (RT) and internal fouling resistance (Rf) increased in the membrane filtration process without coagulation as membrane flux and feed water concentrations increased. Internal fouling resistance, which was not recovered by physical cleaning, was more than 70% of the total resistance at the range of the membrane flux more than $5m^3/m^2{\cdot}day$. In the combined process with coagulation, the cake layer resistance (Rc) increased to about 30-80% of total resistance. As the cake layer formed by coagulation floc was easily removed by physical cleaning, the recovery rate by physical cleaning was 54~90%. It was confirmed from the results that the combined process was more efficient to recover the filtration performance by physical cleaning due to higher formation ratio of reversible fouling, resulted in the mitigation of the frequency of chemical cleaning.

A Development of Shoes Cleaner Control System using Raspberry Pi

  • Deukchang Hyun
    • 한국컴퓨터정보학회논문지
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    • 제29권7호
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    • pp.21-32
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    • 2024
  • 가죽제품 신발은 물 세척을 할 수 없기 때문에 물을 이용하지 않으면서 신발 내⋅외부의 이물질을 제거하고, 신발 내부를 살균할 수 있는 세척 방법이 필요하다. 이를 위해 이 논문에서는 물을 사용하지 않고 고압의 압축공기와 살균 약액 및 자외선 램프롤 이용하여 신발 내⋅외부를 신속하게 세척하는 신발세척기에서 신발 세척의 전 과정을 자동으로 제어하는 신발세척기 제어 시스템을 개발한다. 개발 시스템은 범용 단일보드 컴퓨터(SBC:single board computer)인 라즈베리파이(RaspberryPi)를 이용하여 신발 세척기의 각종 구동 장치들(actuators)을 제어한다. 개발 시스템에 의해 운영되는 신발 세척기는 1분 이내의 세척 시간에 99% 이상의 살균력과 86%이상의 악취제거 효율을 보여준다.

계면활성제 무첨가 세정제의 배합 및 물성/세정성 평가 연구 (A Study on Formulation of Surfactant-free Aqueous Cleaning agents and Evaluation of Their Physical Properties and Cleaning Ability)

  • 이재령;윤희근;이민재;배재흠;배수정;이호열;김종희
    • 청정기술
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    • 제19권3호
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    • pp.219-225
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    • 2013
  • 본 연구에서는 계면활성제에 의한 수계 세정제의 문제점을 해결하고자 친환경적이고 계면활성제가 없는 수계세정제 개발연구를 진행하였다. 이를 위하여 전자 부품 세정대상의 주 오염물인 플럭스(flux)에 대해 용해력이 있고 수용성인 propylene glycol과 propylene glycol alkyl ether계 용제를 주성분으로 하고 여기에 여러 첨가제를 가하여 수계 surfactant-free 세정제 S-1, S-2를 배합하였고, 이들 개발세정제와 비교대상의 수계 surfactant-free 수입 세정제의 물성을 측정하여 세정성능을 예측하고 오염물인 플럭스와 솔더(flux and solder) 대하여 중량법을 이용한 초음파 세정성 평가를 진행하였다. 물성 측정 결과 비교대상 세정제인 수입세정제 V는 본 연구에서 개발한 배합세정제 S-1과 S-2의 세정제와 전반적으로 비슷한 결과 값을 가짐을 확인할 수 있었다. 비교대상 세정제 V와 배합세정제 모두 원액을 희석함에 따라 pH가 저하되다가 다시 상승하는 것이 관찰되었으며 습윤지수값은 세정능력에는 크게 영향을 주지 않는 것으로 판단되었다. 다양한 초음파 주파수(28, 45, 100 kHz)를 사용한 세정성 평가 실험 결과에서 솔더(solder)의 세정은 주파수 45 kHz에서 세정 성능이 가장 좋게 나타났고 플럭스(flux)의 세정 성능 결과는 실험 대상의 모든 세정제가 주파수 28 kHz에서 세정 성능이 가장 좋게 나타났다. 희석하지 않은 원액세정제의 플럭스 및 솔더(flux and solder) 세정의 경우 배합세정제 S-1, S-2 모두 수입세정제 V보다 빠른 세정력을 보여주었다. 그러나 수입세정제 V의 권장 사용농도인 25%에서는 수입 세정제 V가 배합세정제 보다 초기 세정효율이 좋음이 확인되었다. 따라서 본 실험결과를 가지고 판단할 때, 본 연구에서 개발한 배합세정제 S-1, S-2는 충분히 산업현장의 플럭스 및 솔더(flux and solder) 세정에 적용이 가능할 것으로 판단되어진다.

전해 양극수를 이용한 새로운 디스플레이 세정 (A New Cleaning Concept for Display Manufacturing Process with Electrolyzed Anode Water)

  • 류근걸
    • 한국산학기술학회논문지
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    • 제6권1호
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    • pp.78-82
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    • 2005
  • 디스플레이 세정의 개념은 기존의 반도체 세정인 RCA 세정을 근간으로 하고 있으며, 대면적화와 환경친화적인 관점으로 발전하여 왔다. 본 연구에서는 프베이 도표에 근거하여 전리수를 이용하여 입자를 제거할 수 있음을 예측하고 이를 확인하였다. 이 때 연구 대상으로 MgO 분말을 사용하였다. 사용된 전리수는 산화전위가 800 mV 이상이고 pH가 3.1으로 산화상이 강하였다 전리수에 용해되는 MgO 분말의 무게를 pH에 조사하였으며, 250 ml 전리수에 100-500 microgram 범위로 용해됨을 알 수 있었다. 이는 $1E18 ea/cm^3$정도의 용해 물질을 내포하고 있음을 의미하며, 따라서 $1E15 ea/cm^3$ 정도 수준의 불순물을 다루는 디스플레이 세정에 적용할 수 있음을 알 수 있었다. 특기할 것은 전리수는 반도체의 기판인 실리콘 웨이퍼의 자연산화막을 식각하여 표면거칠기를 증가시킴을 처음으로 관찰하였다.

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Harvesting of microalgae via submerged membranes: flux, fouling and its reversibility

  • Elcik, Harun;Cakmakci, Mehmet
    • Membrane and Water Treatment
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    • 제8권5호
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    • pp.499-515
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    • 2017
  • The purpose of this study was to investigate membrane fouling caused by microalgal cells in submerged membrane systems consisting of polymeric and ceramic microfiltration membranes. In this study, one polymeric (flat-sheet, pore size: $0.2{\mu}m$) and two ceramic (flat-sheet, pore size: $0.2{\mu}m$ and cylindrical, pore size: $1{\mu}m$) membranes were used. Physical cleaning was performed with water and air to determine the potential for reversible and irreversible membrane fouling. The study results showed that substantial irreversible membrane fouling (after four filtration cycles, irreversible fouling degree 27% (cleaning with water) and 38% (cleaning with air)) occurs in the polymeric membrane. In cleaning studies performed using water and air on ceramic membranes, it was observed that compressed air was more effective (recovery rate: 87-91%) for membrane cleaning. The harvesting performance of the membranes was examined through critical flux experiments. The critical flux values for polymeric membrane with a pore size of $0.20{\mu}m$ and ceramic membranes with a pore size of $0.20{\mu}m$ and $1{\mu}m$ were ${\leq}95L/m^2hour$, ${\leq}70L/m^2hour$ and ${\leq}55L/m^2hour$, respectively. It was determined that critical flux varies depending on the membrane material and the pore size. To obtain more information on membrane fouling caused by microalgal cells, the characterization of the fouled polymeric membrane was performed. This study concluded that ceramic membranes with a pore size of $0.2-1{\mu}m$ in the submerged membrane system could be efficiently used for microalgae harvesting by cleaning the membrane with compressed air at regular intervals.

이류체 노즐을 이용한 FPD 세정시스템 및 공정 개발 (Optimization of FPD Cleaning System and Processing by Using a Two-Phase Flow Nozzle)

  • 김민수;김향란;김현태;박진구
    • 한국재료학회지
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    • 제24권8호
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    • pp.429-433
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    • 2014
  • As the fabrication technology used in FPDs(flat-panel displays) advances, the size of these panels is increasing and the pattern size is decreasing to the um range. Accordingly, a cleaning process during the FPD fabrication process is becoming more important to prevent yield reductions. The purpose of this study is to develop a FPD cleaning system and a cleaning process using a two-phase flow. The FPD cleaning system consists of two parts, one being a cleaning part which includes a two-phase flow nozzle, and the other being a drying part which includes an air-knife and a halogen lamp. To evaluate the particle removal efficiency by means of two-phase flow cleaning, silica particles $1.5{\mu}m$ in size were contaminated onto a six-inch silicon wafer and a four-inch glass wafer. We conducted cleaning processes under various conditions, i.e., DI water and nitrogen gas at different pressures, using a two-phase-flow nozzle with a gap distance between the nozzle and the substrate. The drying efficiency was also tested using the air-knife with a change in the gap distance between the air-knife and the substrate to remove the DI water which remained on the substrate after the two-phase-flow cleaning process. We obtained high efficiency in terms of particle removal as well as good drying efficiency through the optimized conditions of the two-phase-flow cleaning and air-knife processes.

배수문에서 실내모형실험에 의한 무동력 토사제거시스템의 수리 특성 (Hydraulic Characteristics of the Non-power Soil Cleaning and Keeping System by the Large-Scale Model Test at the Dike Gate)

  • 박찬근;오범환;이달원
    • 한국농공학회논문집
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    • 제56권5호
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    • pp.67-75
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    • 2014
  • In this study, the large-scale hydraulic model test was performed to investigate the hydraulic characteristics for development of the non-power soil cleaning and keeping system at the dike gate. The outlet height, outflow number, outflow discharge, and outflow cycle were compared and analyzed. The non-power soil cleaning and keeping system was most effective at 11.2 mm in the outlet height. And then the mean outflow cycle was 1.09 sec, and the mean outflow discharge was $0.00164m^3/s$. The total outflow number increased gradually as the water level of a water tank increased, and the outlet height decreased. As a level of water tank decreased, the mean outflow cycle was lengthened, and the unit outflow discharge increased. This result showed this system was most effective. To remove the silty clay deposited in facilities, the methods of excavation, dredging, high pressure washing, etc have been applied to the tidal facilities such as land reclamation, a small size fishing port, and a harbor for maintenance. However, this is extremely cost-ineffective, whereas the non-power soil cleaning and keeping system will bring about an enormously positive economic effect. In addition, when the non-power soil cleaning and keeping system is applied to the dike gate of land reclamation, a thorough examination of the local tidal data and the careful system planning are required to prevent the disaster damage caused by flooding.

전해 양극수를 이용한 디스플레이 신 세정 공정 (A new cleaning concept for display process with electrolyzed anode water)

  • 최민기;차지영;김영근;류근걸
    • 한국산학기술학회:학술대회논문집
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    • 한국산학기술학회 2004년도 추계학술대회
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    • pp.99-102
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    • 2004
  • Display process has adopted RCA clean, being applied to large area and coped with environmental issue for last ten years. However, the approaching concept of ozonized, hydrogenised, or electrolyzed water cleaning technologies is within RCA clean paradigm. In this work, only electrolyzed anode water was applied to clean particles and organics as well as metals based on Pourbaix concept, and as a test vehicle, MgO particles were introduced to prove the new concept. The electrolyzed anode water is very oxidative with high oxidation reduction potential(ORP) and low in pH of more than 900mV and 3.1, respectively. MgO particles were immerged in the anode water and its weight losses due to dissolution were measured with time. Weight losses were in the ranges of 100 to 500 micrograms in 250m1 anode waters depending on their ORP and pH. Therefore it was concluded that the cleaning radicals in the anode water was at least in the range of 1 to 5E20 ea per 250 ml anode water equivalent to IE18 ea/cm3. Hence it can be assumed that the anode water be applied to display cleaning since 1E10 to IE15 ea/cm3 ranges of contaminants are being treated. In addition, it was observed that anode water does not develop micro-roughness on hydrophobic surface while it does on the native silicon oxide.

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