• Title/Summary/Keyword: Removal process

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Laundering Factors in Soil Removal

  • Kadolph, Sara J.;Schofield-Tomschin, Sherryl A.;Kwon, Young-Ah
    • Fashion & Textile Research Journal
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    • v.3 no.5
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    • pp.455-465
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    • 2001
  • Assessing soil removal is of interest to the washing machine industry because of government-mandated energy savings and changes in detergent formulation and consumer laundry practices. We designed this study to examine the laundry process from a holistic perspective by integrating factors perceived to be of importance. Our purpose was to assess the impact of selected variables (fabric and soil type, wash temperature and time. detergent amount, and degree of agitation) on soil removal using accelerated laundry conditions. We used the Taguchi method to develop the research design and ANOVA to analyze the data. Although soil removal was affected by fabric type, soil type, type and amount of detergent, degree of agitation, wash time and temperature, and water hardness and volume, wash temperature was the most significant variable.

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Chromate Removal from Wastewater using Micellar Enhanced Ultrafiltration and Activated Carbon Fibre Processes; Validation of Experiment with Mathematical Equations

  • Bade, Rabindra;Lee, Seung-Hwan
    • Environmental Engineering Research
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    • v.13 no.2
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    • pp.98-104
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    • 2008
  • In this study, chromate and cetylperidinium chloride (CPC) removal from artificial wastewater was monitored by using micellar enhanced ultrafiltration (MEUF) and activated carbon fibre (ACF) adsorption hybrid processes. For the efficient chromate removal, molar concentration of the CPC should be five times that of chromate and it should be at least one critical micelle concentration (CMC). The MEUF was found to be effective in the chromate removal while ACF in the CPC adsorption to produce chromate and CPC free effluents. The chromate and CPC removal was 99.8% from MEUF-ACF process. Effluent chromate concentration was exponentially correlated with molar ratio of CPC to chromate and pH.

Removal of Pb2+ ion from aqueous solution Using crab shell treated by acid and alkali (산-염기 처리한 게 껍질에 의한 수풍의 납 이온 제거)

  • 김동석
    • Journal of Environmental Science International
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    • v.12 no.4
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    • pp.469-476
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    • 2003
  • In order to examine the pre-treatment effect of crab shell en Pb$^{2+}$ removal by crab shell in aqueous solution, acid and alkali pre-treated crab shell were used. Electron microscopy techniques such as TEM (transmission electron microscopy) and SEM (scanning electron microscopy), and EDX (energy dispersive X-ray) and FTIR (Fourier transform infrared) spectrometry techniques were used to investigate the process of Pb$^{2+}$ removal by acid and alkali pre-treated crab shell. The Pb$^{2+}$ removal by acid pre-treated crab shell was much lower than that by untreated crab shell because of the decrease of CaCO$_3$ from the crab shell. However, the Pb$^{2+}$removal by alkali pre-treated crab shell increased compared to that by untreated crab shell. The results were confirmed by TEM, SEM, EDX and FTIR.nd FTIR.

Manganese Removal in Water Treatment Processes (상수처리에서 망간 제거)

  • Kim, Jinkeun;Jeong, Sanggi;Kim, Jeongsook;Park, Sejin
    • Journal of Korean Society of Water and Wastewater
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    • v.19 no.5
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    • pp.595-604
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    • 2005
  • To determine the characteristics of manganese removal in Korea, 31 multi-regional water treatment plants (WTPs) were examined. The concentration of manganese in raw water was higher than the standards for drinking water at 2 WTPs. Manganese should be properly removed during water treatment processes to reduce the occurrence of black water in the distribution system because $Mn^{+2}$ can cause black deposits when it is oxidized. Manganese can effectively removed by oxidation, followed by sedimentation and filtration as well as absorption by greensand. Manganese absorption by greensand was the major mechanism for the removal of manganese, and it is effectively removed using this process. Regeneration of greensand using an oxidation agent was necessary for continuous and adequate removal of manganese.

Investigation on the Removal of Dissolved Aluminum Ion in Drinking Water (정수중(淨水中)의 용존(溶存)알루미늄 제어방안(制御方案)의 조사(調査))

  • Choi, Suing-Il;Kim, Moon-Jeong
    • Journal of Korean Society of Water and Wastewater
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    • v.11 no.1
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    • pp.42-52
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    • 1997
  • The affection of activated carbon on the dissolved aluminum ion in drinking water has been observed. In addition, the aluminum ion removal capability of activated, alumina, chitosan, and ion exchange resin have been investigated. Experimental results indicated that the coal based activated carbon released considerable amount of aluminum ion to the water while coconut shell based activated carbon didn't. However the release was not continuous. Activated alumina didn't show any recognizable removal capability for aluminum ion in water. Particulate chitosan has removed aluminum ion although dissolved chitosan has not. However it need to development a regeneration process for chitosan to be an effective mean for aluminum ion removal. Ion exchange resin showed a reliable aluminum ion removal capability. The ion exchange capacity was 2.63 meq/g resin for the aluminum ion in drinking water.

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Mixing effect on organic removal efficiency in treating low-strength wastewater using a modified anaerobic filter reactor (변형 혐기성 여상 반응조에서 교반강도가 유기물 제거효율에 미치는 영향)

  • 정병곤;이헌모
    • Journal of Environmental Science International
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    • v.5 no.4
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    • pp.513-524
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    • 1996
  • Laboratory investigation was conducted to evaluat the mixing effects on organic removal efficiency to treat low-strength synthetic wastewater using modified anaerobic - filter reactor combining anaerobic filter and upflow anaerobic sludge blanket. Using the modified process the low-strength wastewater like municipal sewage could be treated with 85% T-COD removal efficiency at hydraulic retention time of 6 hours. At the constant organic loading of 0.5 kg COD/m 3-day, the organic removal efficiency and effluent COD concentration are increased as influent COD concentration increased from 125 mg/l to 500 mg/l. Mixing effects on organic removal efficiency are evident and optimum mixing speed is found as 50RPM. Placing the granular sludge and media on which slime layer was pre-formed into the reactor seemed to be very effective In achieving short start-up period. Therefore, the steady state was achived after 4 weeks and 1 week based on T-COD and S-COD, respectively.

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Effect of the Total Organic Carbon(TOC) on phosphorus removal by Stapylococcus auricularis (Stapylococcus auricularis에 의한 인 제거에서 총유기탄소의 영향)

  • 최석순
    • Journal of environmental and Sanitary engineering
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    • v.15 no.3
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    • pp.57-61
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    • 2000
  • Stapylococcus auricularis was used for the simultaneous removal of phosphorus and Total Organic Carbon(TOC) in the wastewater from sewage and various industries. In this study, the characteristics of phosphorus removal was investigated with initial ratio of TOC phosphorus in the synthetic wastewater. When the synthetic wastewater containing 15mg/L of phosphorus was treated under anaerobic and conditions, phosphorus was removed completely within 6 hours of operation. And when the initial ratio of TOC to phosphorus was 30, as high as 10 times the removal rate of phosphorus by Acinetobacter calcoaceticus was achieved. These results implied that a long adaptation time, one of the chief problems in biological phosphorus removal process was overcome.

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Waste Treatment by an Anaerobic Filter (혐기성(嫌氣性) Filter Media 반응조(反應槽)에 의한 폐수처리(廢水處理))

  • Lee, Chan Ki;Rim, Jae Myung
    • Journal of Industrial Technology
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    • v.2
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    • pp.33-44
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    • 1982
  • This study mainly concentrated on the treatment of nightsoil by an anaerobic filter media process. Nightsoil has been one of the major water pollutants in this couotry. It represents high ROD and SS concentrations. A comprehensive laboratory study conducted at Kangwoon National University indicate: (1) In the case of anaerobic filter system, COD and BOD removal efficiencies were greatly influenced by hydraulic retention time(HRT), but SS removal efficiencies dropped slowly when HRT were 2~13 days. (2) COD removal efficiencies were 19% when HRT were 15 days, 14% when HRT were 8 days, 10% when HRT were 6 days, 9% when HRT were 4 days, 2% when HRT were 2 days. (3) BOD removal efficiencies were 23% when HRT were 15 days, 14% when HRT were 8 days, 18% when HRT were 6 days, 7% when HRT were 4 days, 5.8% when HRT were 2days. (4) SS removal efficiencies were 21%~25%(2~15 days HRT).

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Removal Characteristics of Cyclic Ethers in Biological Wastewater Treatment System (고리형 에테르의 생물학적 처리 특성)

  • Lee, Sung-Ryul;Jeong, Yeon-Koo
    • Journal of Environmental Science International
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    • v.17 no.3
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    • pp.343-350
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    • 2008
  • The fate of two cyclic ethers, THF(Tetrahydrofuran) and 1,4-Dioxane, in conventional biological wastewater treatment plants was investigated using sequential activated sludge process. Removal efficiency of THF were about 86% in average, which was greater than that of 1,4-Dioxane, 30%. However, it was not clear whether the removal of cyclic ethers in biological system was caused by microbial activity or not. Thus treatability tests were conducted by batch experiments. The effects of mixing, aeration and the addition of activated sludge on the removal of cyclic ethers were investigated in batch experiments. THF was totally removed by mixing and aeration in 24 hours while removal ratio of 1,4-Dioxane was at most 30% for the same period. This results could be ascribed to the differences in Henry's law constants between the two chemicals. In addition, biological degradation including biosorption was not obviously observed in these batch tests.

Simultaneous Nitrification and Denitrification by Anaerobic-Aerobic Biological Packed Bed Process

  • Lee, Min-Gye;Ju, Chang-Sik;Lee, Byung-Hyun;Kim, Jung-Kyun;Tadashi Hano
    • Journal of Life Science
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    • v.9 no.2
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    • pp.40-43
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    • 1999
  • In the wastewater treatment experiment by anaerobic-aerobic packed bed unit, it was found that the high and stable removal efficiency of nitrogen could be obtained. The extent of nitrogen removal gradually decreased with the rise of recycle ratio and DO concentration. On the other hand, the extent of phosphorus increased with the increase of DO concentration. COD showed high removal efficiency over the entire range tested. The simulation of T-N behavior was carried out satisfactorily by using the kinetic equations for biofilm and the reactor model which considered the packed bed as a plug flow reactor.