• 제목/요약/키워드: Cleaning Efficiency

검색결과 412건 처리시간 0.023초

윈치커튼식 비육돈사에서 습식공기정화기의 공기정화 효율 분석 (An Air Cleaning Efficiencies of Wet Air Cleaner in the Swine Finishing Winch Curtain Stall)

  • 오인환;김운걸;이한성
    • 한국축산시설환경학회지
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    • 제14권2호
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    • pp.75-80
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    • 2008
  • High concentration of $NH_3$, $CO_2$, and lots of dust are found in modern densely raising stall system, as results, they provide a negative influence on animal and lamer health, and production ability. Therefore, it is necessary to keep clean the inside of stall air to increase the productivity. A wet type air cleaner has been developed to clean the stall air. The work principle is that the inside air are sucked through the fan, and the rotating discs make a water into a fineness spray and blows into the stall. The spray can take the dust, $NH_3$, and odor from the stall inside air and give back to the circulating water, which can be refreshed in 2 hours interval. In the Present study, we measured the $NH_3$, dust, odor, temperature and humidity in a swine stall that were installed two wet air cleaners with 700 fattening swine with on-mode and off-mode of wet air cleaners. In fall, the concentrations of $NH_3$ in off-mode stall were maximum 24 ppm and minimum 16 prm, and the average was 18.2 ppm. However in on-mode stall the $NH_3$ concentrations were maximum 7ppm and minimum 1ppm, and the average was 2.7ppm. The concentration of $NH_3$ in on-mode was 74% lower than off-mode stall. Odor was measured by olfactometer. In the off-mode stall, the odor unit was 3,800 OU/$m^3$, but in the on-mode stall the odor unit was 2,100 OU/$m^3$ Odor removal efficiency was about 45% in on-mode stall. The dust measure was divided into 3 categories, $PM_{10}$, $PM_{2.5}$ and $PM_{1.0}$. Whereas the $PM_{10}$ showed no significant differences between the tests, $PM_{2.5}$ and $PM_{1.0}$ in the fine particle range reduced remarkably in the on-mode.

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저소음 청소기 개발 (Low Noise Vacuum Cleaner Design)

  • 주재만;이준화;홍승기;오장근;송화규
    • 한국소음진동공학회:학술대회논문집
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    • 한국소음진동공학회 2007년도 추계학술대회논문집
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    • pp.939-942
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    • 2007
  • Vacuum cleaner is a close life product that can remove various dusts from our surroundings. However well vacuum cleaner clean our environments, many people are looking away from it, due to its loud noise. Its noise causes a big trouble in the usual life, for example, catch calls, TV watching and discussing etc. To reduce these inconveniences, noise reduction methods and systematic design of low noise vacuum cleaner are studied in this paper. At first, sound quality investigation is performed to get the noise level and quality that make people TV watching and catch calls available. Based on the European and domestic customer SQ survey result, sound power, peak noise level and target sound spectrum guideline are studied and introduced. As a second, precise product sound spectrums are designed into each part based on the sound quality result. Fan-motor, brush, mainbody, cyclone spectrums are decided to get the final target sound based on the contribution level. Fan-motor is the major noise source of vacuum cleaner. Specially, its peak sound, RPM peak and BPF Peak, cause the people nervous. To reduce these peak sounds, high rotating impeller and diffuser are focused due to its interaction. A lot of experimental and numerical tests, operation points are investigated and optimization of flow path area between diffusers is performed. As a bagless device, cyclones are one of the major noise sources of vacuum cleaner. To reduce its noise, previous research is used and adopted well. Brush is the most difficult part to reduce noise. Its noise sources are all comes from aero-acoustic phenomena. Numerical analysis helps the understanding of flow structure and pattern, and a lot of experimental test are performed to reduce the noise. Gaps between the carpet and brush are optimized and flow paths are re-designed to lower the noise. Reduction is performed with keeping the cleaning efficiency and handling power together and much reduction of noise is acquired. With all above parts, main-body design is studied. To do a systematic design, configuration design developments technique is introduced from airplane design and evolved with each component design. As a first configuration, fan-motor installation position is investigated and 10 configuration ideas are developed and tested. As a second step, reduced size and compressed configuration candidates are tested and evaluated by a lot of major factor. Noise, power, mass production availability, size, flow path are evaluated together. If noise reduction configuration results in other performance degrade, the noise reduction configuration is ineffective. As a third configuration, cyclones are introduced and the size is reduced one more time and fourth, fifth, sixth, seventh configuration are evolved with size and design image with noise and other performance indexes. Finally we can get a overall much noise level reduction configuration. All above investigations are adopted into vacuum cleaner design and final customer satisfaction tests in Europe are performed. 1st grade sound quality and lowest noise level of bagless vacuum cleaner are achieved.

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$UV/H_2O_2,\;UV/TiO_2/H_2O_2$, Photo-Fenton 산화방법에 의한 Citric Acid의 분해효율 비교 (Comparative Studies Of the $UV/H_2O_2,\;UV/TiO_2/H_2O_2$ and Photo-Fenton Oxidation for Degradation of Citric Acid)

  • 서민혜;조순행;하동윤
    • 대한환경공학회지
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    • 제28권4호
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    • pp.429-437
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    • 2006
  • 화학세정폐수에 함유되어 있는 citric acid의 효율적인 처리방안을 수립하기 위해 $UV/H_2O_2,\;UV/TiO_2/H_2O_2$, Photo-Fenton 산화방법을 이용하여 각각 citric acid의 제거효율 및 그에 따른 전력소비량을 평가하였다. 그 결과 조사된 최적 처리조건에서 $UV/H_2O_2,\;UV/TiO_2/H_2O_2$, Photo-Fenton 산화방법을 이용한 citric acid 농도에 근거한 TOC 제거효율은 각각 95.5%, 92.3%, 91.5%로 조사되었으며, 그에 따른 전력소비량은 $11.26kWh/m^3,\;3.85kWh/m^3,\;0.799kWh/m^3$으로 조사되었다. 이 결과에 의하면 세가지 광화학적 산화방법 모두 유기물질이 90% 이상 제거되어 citric acid의 분해에 효과적인 것으로 판단되었다. 그러나 Photo-Fenton 산화방법이 다른 방법에 비해 처리에 소요되는 반응시간이 짧은 것으로 나타났다. 또한 광화학적 산화방법의 운영비를 결정짓는데 중요한 요소인 전력소모량 측면에서도 Photo-Fenton 산화방법이 다른 방법에 비해 우수한 것으로 조사되어 본 연구에서 비교하는 세가지 방법 중 citric acid 처리에는 Photo-Fenton 방법이 효율적인면과 경제성면에서 가장 적합한 처리기술로 결론지을 수 있었다.

축산폐수 처리를 위한 막결합형 이상 혐기성 반응조에서 여과막 저항특성 (Fouling Characteristics in Submerged Membrane System of Two-Phase Anaerobic Reactor for Piggery Wastewater Treatment)

  • 이상민;정진영;정윤철
    • 대한환경공학회지
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    • 제22권3호
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    • pp.523-533
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    • 2000
  • 본 연구는 재래식 혐기성 공법에 비해 메탄회수율과 처리효율이 우수한 막분리형 이상 혐기성 반응시스템을 개발하여 산생성 반응조의 미생물 체류시간을 증대시키고 시스템 운전효율을 향상시키기 위해 수행하였다. Pilot plant 운전에 사용된 막은 셀룰로오스 계통으로 $0.5{\mu}m$의 막공경과 $0.8m^2$의 유효 표면적을 가졌으며 메탄발효조는 UASB와 AF로 구성되어 있다. 혐기성 침지형 반응조를 운전한 결과 COD 제거율은 70~80%, 생성가스 중 메탄함율은 90%까지 향상시킬 수 있었다. Pilot plant 운전동안 막의 케이크 저항이 중요한 막오염원으로 나타남에 따라 이를 최소화하기 위해 세가지 공경 (40, 53, $63{\mu}m$)을 가진 전처리 필터로 적용하였다. 적용된 prefilter중 $63{\mu}m$ 전처리 필터의 경우가 가장 효과적으로 케이크 저항을 줄이고 막 유속을 증가시켜 50일 이상 장기운전을 가능케 하였다. 또한 장기 운전으로 인한 막 오염물질은 산과 알카리 세척용액에 의해 연속적으로 세척함으로써 최초 막유속의 89% 까지 회복할 수 있었다.

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이산화염소수 생성기의 생성효율 및 과.채류에 대한 침지 세정 살균효과 (Effect of an Aqueous Chlorine Dioxide Generator and Effect on Disinfection of Fresh Fruits and Vegetables by Immersion Washing)

  • 박기재;정진웅;임정호;장재희;박희주
    • 한국식품저장유통학회지
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    • 제15권2호
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    • pp.236-242
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    • 2008
  • 이산화염소수 발생 최적조건을 검토하기 위하여 생성원료인 $NaClO_2$ 농도(0.01-0.1%)와 $Cl_2$ gas 투입량(100-1,000 g/hr)에 따른 chlorite, chlorate, FAC 및 chlorine dioxide의 생성량을 조사하였다. Chlorate, FAC 및 chloride dioxide 생성량은 $NaClO_2$$Cl_2$ 투입량이 증가할 수록 생성량이 증가하는 경향을 나타내었다. 이산화염소수 최적 생성조건은 0.1% $NaClO_2$, 900 g/hr $Cl_2$ gas 농도였으며 발생한 이산화염소수의 $ClO_2$는 882 ppm, FAC는 8.0 ppm, chlorite는 검출되지 않았고 chlorate는 43.32 ppm이었다. 이때의 수율과 순도는 각각 97.0%, 96.0%였다. 상추, 치콘, 깻잎, 케일의 채소류에 대한 세정 침지 살균에서는 이산화염소수 농도의존성 감균 효과를 나타내어 3-4 log의 총균수 감소 효과가 있었다. 과일의 경우에도 농도 의존성 감균 효과는 동일하였으며 대략 3-5 log의 총균수 감균 효과가 있었다.

장루 보유자 교육용 자료에 대한 조사 연구 (A Survey on the Ostomate Education Materials)

  • 박경숙;김명숙;최경숙
    • 대한간호학회지
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    • 제28권3호
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    • pp.705-717
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    • 1998
  • Ostomates have suffered from many difficulties due to their physical, psychosocial handicaps and changes of life style to include ostoma management that influences their daily and quality of life. An appropriate nursing education for ostoma management is very important. Practical educational materials needs revision because those were developed by pharmaceutical companies and hospital institutions. The purpose of this study is to provide more practical and reasonable education materials for ostomates by doing analysis and survey of educational materials now being used. We surveyed 8 types of educational materials used in 23 university hospitals and medical centers in Seoul ; four of them were developed by department of nursing and the remainder by an Ostomy Company Data, collected from July 14, 1997 through July 31, 1997 were analyzed. The results are as follows ; 1. The analysis of education guide, on ostomate included 14 subcategories : introduction, structure and function of gastrointestinal tracts, definition of stoma, types of ostomy, definition of peristalsis, methods of defecation management, selection of instrument, resolution of problems and general situations following surgery, daily life, where to ask for help, explanations for terms, information about where to buy instrument, explanations for enterostomal therapist, a matter of consultation with doctor, etc. 2. Introduction contained specific contents on practical ostomate management that ostomates would experience through their lives. Ostomate education guides were developed 3 hospitals except one which missed this point. 3. Most ostomate education guides, except one hospital, helped ostomates to understand their physical structure changes with specific explanations on gastrointestinal tracts with figures. 4. Six institutions did not talk about the definition of peristalsis. 5. All institutions, except two, helped ostomates to understand types of ostomy with figures. 6. More detailed explanations on natural defecation are needed. The benefits and pitfalls of natural defecation should be more specified. 7 No psychosocial difficulties of ostomy management were addressed. 8. The efficiency of enema can be better understood through all explanations with figures. Some institutions did not mention items about definition, benefits, pitfalls of enema, sequency of enema, how to wash, cautions performing and enema, skin management, cleaning instrument after enema proper time to spend. 9. There were no detailed contents and what to do in case of not being able to do enema. 10. Only one educational material mentioned emotional aspects after the surgrey. 11. Most institutions explained subcategory of daily life but did not provide specific contents on the difficulties of physical, psychological, and sociocultural controls. 12. The subcategory of ureterostomy education guides included explanations on normal structure and function of urinary tracts, types of ureterostomy, how to manage skin, usage and types of instrument, commercial urostomy, how to manage instrument, daily life, introduced the general contents. However, more specific explanations were needed.

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저농도 이산화탄소 포집용 흡착제 개발 및 최적조건에 관한 연구 (A Study on the Low Concentration Carbon Dioxide Adsorbent and Optimal Conditions)

  • 이주열;박덕신;조영민;권순박;황윤호;송형진;이상봉
    • 한국응용과학기술학회지
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    • 제29권1호
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    • pp.1-12
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    • 2012
  • 본 논문은 다양한 시설내에 적은 농도의 $CO_2$ 제거를 위한 선택적 $CO_2$ 흡수능력을 향상시킨 흡착제의 효율평가에 관한 것이다. 직경 4mm의 구형 흡착제는 시판용 제올라이트에 첨가제, 물, 바인더, LiOH를 섞어 제조하였다. 칼럼테스트에서 400분 이내에 90% 이상의 $CO_2$흡착효율을 나타내었고, 흡착필터모듈 흡착능력을 평가하기 위해 회분식과 연속식타입의 챔버테스트가 시행되었다. 회분식테스트에서 30분 이내에 약 92%의 $CO_2$가 제거되는 것을 확인하였다. 연속식테스트에서 30분 이내 70%의 $CO_2$가 제거효율을 보였으며, 2,500ppm 이상의 $CO_2$가 제거되는 것을 확인하였다. 재현성테스트를 수차례 수행한 결과 15일동안 1,000ppm 이상의 $CO_2$가 연속적으로 제거됨을 보였다. TGA 분석법을 이용한 흡착량 분석에서 흡착제 g당 5.0mmol의 $CO_2$를 흡착하는 것으로 나타났다. 본 연구에서 개발된 흡착제는 상온에서 저농도 $CO_2$ 실내환경에 적용가능한 것으로 판단된다.

복합 막분리 공정에 의한 섬유가공 공정에서의 가성소다 회수 (Recovery of Caustic Soda in Textile Mercerization by Combined Membrane Filtration)

  • 양정목;박철환;조진구;김상용
    • 대한환경공학회지
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    • 제30권12호
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    • pp.1273-1280
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    • 2008
  • 본 연구에서는 섬유가공공정 중 머서화공정으로부터 가성소다액를 회수하기 위한 최적의 운전조건을 확립하고자 하였다. 주요 인자들로는 NF/RO막의 적용을 위해 세라믹 막을 이용하여 파울링 지수를 평가, 고분자 막의 적용을 위해 가성소다액의 회수율을 측정, 막의 재생율 향상, 화학세정 조건, 유기물부하, 탁도 및 색도의 최적 제거조건, 그리고 세라믹 막과 고분자막의 복합공정에서의 투과플럭스를 조사하였다. 결과에 따르면, 1단계 공정의 세라믹 한외여과막과 2단계 공정의 나노여과막은 총부유고형물, 잔류유기물, 색도를 포함한 탁도의 제거 그리고 가성소다 용액의 회수에 적합한 공정구성임을 확인하였다. 한외여과막만을 단독으로 사용했을 경우, 총 부유물질과 탁도를 99.0%이상 제거하였고, 색도와 TOC는 각각 74.7%와 49.2%의 제거효율을 얻을 수 있었다. 반면에 세라믹 UF+NF 복합막 공정에서는 총 부유물질과 탁도를 99.9%이상 제거할 수 있었고, 색도는 87.7%, TOC는 78.2%의 제거효율을 얻을 수 있었다. 특히, 복합막 공정에서는 83.7%의 부피회수율일 때 91.3% 가성소다를 성공적으로 회수 할 수 있었다. 이러한 측면에서 복합공정을 통해 가성소다 폐수로부터 순도 높은 가성소다액을 회수할 수 있었으며, 회수된 가성소다액은 공정 내에 재사용이 가능하여 경제적인 이득을 기대할 수 있다.

Prevention of P-i Interface Contamination Using In-situ Plasma Process in Single-chamber VHF-PECVD Process for a-Si:H Solar Cells

  • Han, Seung-Hee;Jeon, Jun-Hong;Choi, Jin-Young;Park, Won-Woong
    • 한국진공학회:학술대회논문집
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    • 한국진공학회 2011년도 제40회 동계학술대회 초록집
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    • pp.204-205
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    • 2011
  • In thin film silicon solar cells, p-i-n structure is adopted instead of p/n junction structure as in wafer-based Si solar cells. PECVD is a most widely used thin film deposition process for a-Si:H or ${\mu}c$-Si:H solar cells. For best performance of thin film silicon solar cell, the dopant profiles at p/i and i/n interfaces need to be as sharp as possible. The sharpness of dopant profiles can easily achieved when using multi-chamber PECVD equipment, in which each layer is deposited in separate chamber. However, in a single-chamber PECVD system, doped and intrinsic layers are deposited in one plasma chamber, which inevitably impedes sharp dopant profiles at the interfaces due to the contamination from previous deposition process. The cross-contamination between layers is a serious drawback of a single-chamber PECVD system in spite of the advantage of lower initial investment cost for the equipment. In order to resolve the cross-contamination problem in single-chamber PECVD systems, flushing method of the chamber with NH3 gas or water vapor after doped layer deposition process has been used. In this study, a new plasma process to solve the cross-contamination problem in a single-chamber PECVD system was suggested. A single-chamber VHF-PECVD system was used for superstrate type p-i-n a-Si:H solar cell manufacturing on Asahi-type U FTO glass. A 80 MHz and 20 watts of pulsed RF power was applied to the parallel plate RF cathode at the frequency of 10 kHz and 80% duty ratio. A mixture gas of Ar, H2 and SiH4 was used for i-layer deposition and the deposition pressure was 0.4 Torr. For p and n layer deposition, B2H6 and PH3 was used as doping gas, respectively. The deposition temperature was $250^{\circ}C$ and the total p-i-n layer thickness was about $3500{\AA}$. In order to remove the deposited B inside of the vacuum chamber during p-layer deposition, a high pulsed RF power of about 80 W was applied right after p-layer deposition without SiH4 gas, which is followed by i-layer and n-layer deposition. Finally, Ag was deposited as top electrode. The best initial solar cell efficiency of 9.5 % for test cell area of 0.2 $cm^2$ could be achieved by applying the in-situ plasma cleaning method. The dependence on RF power and treatment time was investigated along with the SIMS analysis of the p-i interface for boron profiles.

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계면 활성제 첨가한 암모니아수의 소수성 실리콘 웨이퍼와의 반응 세정 효과 (The Effect of Surfactants in $\textrm{NH}_4\textrm{OH}$ on Silicon Surfaces and Particle Removal)

  • 박진우;박진구;김기섭;송형수
    • 한국재료학회지
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    • 제9권9호
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    • pp.872-877
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    • 1999
  • 본 연구에서는 NH(sub)4OH에 계면 활성제를 첨가한 세정액의 특성 및 세정 효과를 H(sub)2O(sub)2가 첨가된 NH(sub)4OH 세정액과 비교 연구하였다. NH(sub)4OH에 계면 활성제를 첨가한 경우 용액의 pH 및 산화 환원전위(Eh) 는 NH(sub)4OH의 값과 거의 유사하고 H(sub)2O(sub)2를 첨가한 경우에 pH는 감소하고 Eh는 증가하는 경향을 보였다. 표면장력은 계면 활성제를 첨가한 경우 약 72 dynes/cm에서 약 38dynes/cm로 감소하였으나 H(sub)2O(sub)2를 첨가한 경우에는 NH\ulcornerOH 용액과 비교 거의 변화가 없었다. 실리콘 웨이퍼의 식각 속도를 측정한 결과 H(sub)2O(sub)2나 계면 활성제를 첨가하지 않은 초순수와 1 : 5(NH(sub)4OH : H(sub)2O(sub)2)의 부피비의 NH(sub)4OH용액이 첨가한 용액에 비해 최소 50배 이상의 높은 식각 속도를 보였다. 파티클 제거 실험에서 H(sub)2O(sub)2가 첨가된 NH(sub)4OH 세정액은 실험에 사용한 실리콘 표면위의 직경 0.67$\mu\textrm{m}$의 PSL파티클을 세정액의 온도와 무관하게 잘 제거하였으나 계면 활성제를 첨가한 NH\ulcornerOH경우에 상온에서는 파티클을 제거할 수 없었으나 온도를 5$0^{\circ}C$와 8$0^{\circ}C$로 증가시킨 경우 H(sub)2O(sub)2가 첨가된 NH(sub)4OH와 유사한 세정 효과를 나타내었다.

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