• Journal of Korean Ophthalmic Optics Society
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• v.15 no.3
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• pp.227-234
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• 2010

Purpose: The cleaning effect of protein deposit and the change of contact lens parameters by ultrasonic cleaner for eye glasses on the soft contact lenses were investigated. Methods: Etafilcon A contact lenses contaminated with protein, was ultrasonicated by ultrasonic cleaner for eye glasses and for the control group, spoiled contact lenses were cleaned by multi-purpose solution. The remaining protein deposits on the contact lenses were determined after extraction and the changes of overall diameter, base curve, center thickness power, and water contents on contact lenses were measured and surfaces of contact lenses were observed by scanning electron microscope. Results: The cleaning efficacies of multi-purpose solution on protein deposited etafilcon A contact lenses were 6.08%, and 23.73~33.92% in the group of ultrasonic cleaner for eye glasses with multi-purpose solution and 0~12.99% in the group of ultrasonic clear for contact lens with multipurpose solution depending on the treatment time. The changes of parameters and surface on contact lenses by ultrasonication were not observed. Conclusions: Ultrasonic cleaner for eye glasses can be used to eliminate protein deposits for the diagnostic soft contact lens in the office since it was effective to eliminate protein deposits and not caused change of parameters on soft contact lenses.

• Journal of Korean Society on Water Environment
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• v.23 no.3
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• pp.391-396
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• 2007

Dry washing by air and sand to clean dishes was investigated for establishing a dry washing process in a kitchen. Thirty seasonings and foods as dirt markers and fourteen kinds of dishes were used for the experiment, and washing efficiency was evaluated by COD-MN (mg/L). It was found that air dry washing effectively reduced COD-MN of some dirt markers but not effective at all to some dirt markers. It could be also said that dirt markers would not be completely removed by air dry washing. The shape of dishes also affected COD-MN reduction by air dry washing. Sand dry washing showed excellent efficiency on COD-MN reduction. Combination of air and sand dry washing may be necessary to make a dish dry washing system which is completely independent from water.

• Electric Engineers Magazine
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• s.375
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• pp.46-47
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• 2013

2013. 8. 5(월) 14:22경, 서울시 성북구 정릉동 소재 ${\bigcirc}{\bigcirc}$ 고등학교 3층 여자화장실 앞에서 학교청소 등을 하는 건물관리업체의 직원(남 54세) 이 고압세척기로 바닥 물청소를 하던 중 세척기의 누전으로 감전 사망한 재해임.

• The Korean Journal of Pesticide Science
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• v.17 no.4
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• pp.237-243
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• 2013

Pesticides were sprayed on perilla leaf and leafy lettuce in a greenhouse and the reduction rate of pesticide residues on each vegetable by washing were tested. The reduction rate of pesticide residues by washing for 30 sec~3 min on perilla leaf were 3~63% in tap water, 2~58% in salt water, 6~74% in green tea water, and 8~86% in detergent solution. The detergent solution only showed significant difference in reduction rates compared to the tab water washing. Considering reduction effects of the washing duration, it was showed that the reduction rates were a pattern of inclining as the duration of washing process increased, but there was no significant difference in the reduction rates except the reduction rates between washing in the detergent solution for 1 min and 3 min. Comparing washing in flowing tab water and in stagnant tab water with leafy lettuce, the reduction rate by one time washing were 8~68% in flowing tab water and 7~64% in stagnant tab water. The water and the time used in this experiment were 17.5 L, 2.9 min with flowing tab water and 4 L, 1 min with stagnant tab water. The reduction rate by 3 times washing in stagnant tab water were 16.5~76.6%, and the water and the time used were 12 L, 3 min. Therefore, when the water and the time used to wash vegetables were considered, washing two or three times in stagnant tab water could be more effective than washing one time in flowing tab water.

• Proceedings of the Korean Society of Postharvest Science and Technology of Agricultural Products Conference
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• 2003.10a
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• pp.174-175
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• 2003

현재 유통되고 있는 일반백미의 경우 소비자가 밥을 짓기 위해서는 쌀을 씻어야하는 번거로움 뿐만아니라 쌀 중량의 약 15배의 물이 소요되고, 또한 이때 발생된 쌀뜨물이 수질오염의 원인이 되기 때문에 무세미가공 및 보급 필요성이 점차 높아지고 있다. 무세미 가공분야의 선진국인 일본의 경우 ‘92년부터 습식 무세미조제기가 실용화되기 시작, 현재 사다께 등 6개사에서 기계장치를 생산보급 하고 있으며, 무세미의 유통도 일반화되어가고 있는 추세이다. 국내의 경우 무세미조제기는 근래에서야 습식 무세미 조제설비가 국산화되어 보급초기 단계 있으며, 무세미의 안정적 가공 및 보급을 위해서는 앞으로 많은 연구가 이루어져야 할 것으로 생각된다. 특히 습식의 경우 쌀이 물에 접촉하는 시간이 길 경우 품질저하의 우려가 크고, 쌀중량의 1.4배에 해당하는 물이 가공과정에 필요하기 때문에 물사용량을 억제할수 있는 가공기술의 개발 필요성이 커지고 있다. 따라서 본 연구에서는 물사용량을 최소화 할 수 있는 무세미 조제시스템을 개발하고자 하였으며, 주요결과를 요약하면 다음과 같다. 시작기는 연마 및 공기세척부, 정전기 세척부, 미세가수세척부로 구성하여 쌀이 단계적으로 세척될 수 있도록 제작되었다. 성능시험 결과, 각 세척공정별 세척수의 탁도 감소효과는 연마 및 공기크리닝부에서 22.67ppm, 정전기 크리닝부에서 8.33ppm, 미세가수세척부에서 17.34 ppm이 감소되는 것으로 나타났다. 특히 정전기세척부의 탁도감소 효과는 다른 두공정에 비해 작지만 제거가 쉽지 않은 미세한 쌀겨들을 제거하여 탁도를 개선을 시켰기 때문에 미세가수세척장치에서 가수량을 적게 사용하는데 기여한 것으로 판단된다. 가공시 적정 탁도를 확보할 수 있는 가수량은 430cc/kg로 기존의 습식에 비해 약 69%정도 세척수 절감효과가 있었다. 이때 미세가수세척부의 원통스크린 회전수는 108, 205rpm범위가 적정한 것으로 나타났다. 쌀의 품위는 탁도가 가공전 97.33ppm(일반백미)에서 가공후 최대 48.00ppm으로 낮아졌으며, 백도도 가공전 36.80에서 42.80으로 향상되어 씻지 않고도 밥을 지을수 있는 무세미 가공이 가능하였다. 이밖에 쇄립률은 가공전 5.30%에서 7.37%로 다소 증가하는 것으로 나타났고, 함수율은 가공전 15.60%에서 15.80%로 약 0.2%가 증가하였으나 기존의 연구결과에 비춰볼 때 문제가 되지 않을 것으로 여겨진다.

• Proceedings of the Korean Institute of Information and Commucation Sciences Conference
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• 2011.05a
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• pp.760-761
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• 2011

본 연구에서는 치과용 유니트체어의 용수공급 시스템 중 수관 내부에 생성되는 바이오필름을 보다 효율적으로 제거하기위하여 공기와 물을 혼합한 버블을 생성하고 가변적인 압력을 인가하여 살균과 세척을 동시에 수행할 수 있는 시스템을 개발하고자 하였다. 이를 위하여 공기와 물의 혼합 세척을 통한 바이오필터 세척 및 전기분해를 이용한 용수 살균 시스템을 구현하였으며, 물과 공기의 흐름제어 및 가변적인 압력 조절 제어시스템을 구현하였다. 그리고 무선으로 제어가 가능한 솔레노이드밸브로 구성된 벨브조립체를 구성하여 세척모드 및 용수공급모드의 선택적 운용이 가능한 시스템을 구현하였다.

• Journal of Korea Soil Environment Society
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• v.3 no.3
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• pp.55-62
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• 1998

Soils contaminated with hydrocarbons and residual metals can be effectively treated by soil washing. In developing the soil washing process several major effects for separating contaminants from coarse soils progressively improved upon combinations of mining and chemical processing approaches. The pilot-scale soils washing process consists of the four major parts : 1) abrasive scouring, 2) scrubbing action using a washwater that is sometimes augmented by surfactants or other agents, 3) rinsing, and 4) regenerating the contaminated washwater. The plant was designed based upon the treatment capacity > 5 ton/hr on site. The lumpy contaminated soil fractions first experience deagglomeration and desliming passing through a rolling mill pipe. In the second unit the attrition scrubbing module equipped with paddles uses high-energy to remove contaminants from the soils. And a final rinsing system is assembled to separate the washwater containing the contaminants and very fine soils from the washed coarse soils. For recycling the contaminated washwater passes through a washwater clarifier specifically designed for flocculation, sedimentation and gravity separation of fine as well as flotation and separation of oils from the washwater. In order to more rapidly assess the applicability of soil washing at a potential site while minimizing the expense of mobilization and operation, a mobile-type soil washing process which is self-contained upon a trailer will be further developed.

• Journal of Korean Society of Environmental Engineers
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• v.39 no.11
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• pp.626-633
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• 2017

The present study investigated the effect of a water-washing process, which is part of the acid hydrometallurgical process for recovery of high purity of zinc, on the removal of alkali metals and chlorides (Na, K, Ca, Cl) from Electric arc furnace dust (EAFD). Two EAFD samples with different properties were characterized by particle size, XRD and element analysis, and their washing efficiencies (%) on alkali metals and chlorides were compared according to pH, washing time, liquid to solid (L/S) ratio and number of washings. The results show that the alkali metals and chlorides could be effectively removed by the washing (at L/S ration of 3 for more than 30 min., pH 10~11) while minimizing loss of zinc (<0.1%), in which the washing efficiency was Na-78%, K-76%, Cl >99%, respectively. Na and K could be removed up to 97% and 89% respectively by 3 times of repeated washings. With increased sample volume (10 times) of the mixed (1:1, w/w) sample with two types of EAFD, it was confirmed that the pH(10~11) can be used as the main process control parameter for the washing of the alkali metals regardless of EAFD properties.

• Journal of Korea Soil Environment Society
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• v.5 no.1
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• pp.45-54
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• 2000

Several chemical washing procedures were applied to Zn and Cd contaminated soil. Batch and column tests were performed to determine the metal extraction efficiency as a function of pH and concentration. Washing efficiencies by water and NaOH are very low but those by HCI, EDTA and Oxalic acid are high. The most efficient washing occurs in case of using HCI because heavy metal is ionized easily at the condition of low pH. EDTA and Oxalic acid are also effective to extract Zn and Cd because they have a high complexation affinity for heavy metals forming active surface complexes. More Zn is released than Cd is and release trend is increased as pH is decreased and concentration of washing solution is increased. When heavy metal contaminated soil is remediated, HCI and EDTA are more effective to remove Zn than others are. Meanwhile HCI and Oxalic acid are more effective to remove Cd than others are.

• Korean Journal of Food Science and Technology
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• v.33 no.5
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• pp.534-539
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• 2001

To utilize oyster cannery processing waste water effectively, this study was carried out to prepare instant powdered soup using oyster wash water. Instant powdered soup from oyster hot-water extracts (HWE) was prepared by mixing oyster spray-dried hot-water extracts (15 g) with table salt (5 g), cream powder (19 g), milk replacer (12 g), wheat flour (20 g), corn flour (15 g), starch (5 g), glucose (7.5 g) and onion powder (1.5 g). In preparing instant powdered soup from oyster wash water (OWW), powder from oyster spray-dried wash water instead of the spray-dried hot water extracts, was added and other additives were added in proportion to those in the HWE. The OWW consists mainly of carbohydrates (71.1%). It was not different from the instant powdered soup from hot-water extracts. The volatile basic nitrogen, vaible cell counts, coliform group of instant powdered soup from oyster wash water contains 29.4 mg/100g, $4.6{\times}10^4\;CFU/g$, <18 MPN/100g, respectively and its water activity has 0.246. So it was a hygienically safe and conservable instant food. The main fatty acid of OWW was 16 : 0 and 18 : 1n-9. Its chemical score of protein was 59.4% and its main inorganic matter was iron. According to a sensory evaluation, in contrast to the HWE, the OWW had a slightly lower aroma but better taste. It was concluded from the above chemical and sensual evaluation that the oyster wash water can be used as a flavor enhancer for instant powdered soup.