• Title/Summary/Keyword: floc

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In situ measurement of settling velocity for suspended floc sediment with BW method (BW 방법을 이용한 현장 부유 플록 침강속도 측정)

  • Jung, Eui-Taek;Kim, Dong-Ho;Heo, Je-Woo;Hwang, Kyu-Nam
    • Proceedings of the Korea Water Resources Association Conference
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    • 2012.05a
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    • pp.722-726
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    • 2012
  • 각 해역의 부유 플록은 그 해역의 조건에 따라 각기 다르게 형성된 플록이므로, 부유 플록 자체의 특성(결합강도, 밀도 및 크기 등)은 현장특성에 따라 현저하게 다른 "site-specific"한 특성을 가질 뿐만 아니라, 동일 해역이라 하더라도, 조류 등에 의한 유속변화에 따른 흐름전단응력의 증감에 따라 플록의 특성 또한 시간적으로 크게 변화할 수 있다. 이에 현장의 플록 특성이 반영된 부유플록의 침강속도를 산정하기 위해 입도 측정원리중 하나인 BW방법을 응용한 전북대 Owentube를 자체 제작하여 연구가 수행되었으며, 본 연구를 통하여 도출된 현장에서의 점착성 부유 플록의 침강속도 산정 결과는 향후 퇴적물 이송 및 수질 예측을 위한 수치모형 적용시에 필수적으로 요구되는 침강 및 퇴적특성 입력자료로 유용하게 사용될 수 있을 것이다.

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Hydrodynamic Collision Efficiency and Flotation Characteristics of Inorganic Particles in DAF Process (DAF 공정에서 무기 고형입자의 유체역학적 충돌효율과 부상특성)

  • Kwak, Dong-Heui;Kim, Sung-Jin;Lee, Hwa-Kyung;Jung, Heung-Joe;Lee, Jae-Wook;Chung, Paul-Gene
    • Journal of Korean Society of Water and Wastewater
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    • v.16 no.6
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    • pp.655-662
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    • 2002
  • Separation characteristics of inorganic particles occurred during heavy rainwater were investigated in DAF (dissolved air flotation) process. In order to remove the inorganic particles effectively, the collision and flotation efficiencies were examined from a hydrodynamic point of view. Generally, the collision efficiency increased with floc size under the variation of fluid dynamic conditions including inertial force. However, more precise model should be required to analysis the collision efficiency expressed both the physical properties for inorganic particles and hydrodynamic conditions for a reactor.

Determination of Optimun Coagulant Dosage for Effective Water Treatment of Chinyang Lake -The Effect of Coagulant Dosing on Remoaval of Colloidal Pollutants- (진양호소수의 효과적인 정수처리를 위한 최적응집제 주입량 결정 -콜로이드성 오염물질 처리를 위한 응집제 주입효과-)

  • 이원규;조주식;이홍재;허종수
    • Journal of Environmental Science International
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    • v.7 no.6
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    • pp.761-772
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    • 1998
  • This study was performed to determine the optimum coagulant dosing amount for effective treatment of raw water. The removal rate of turbidity and the variations of water qualities according to various dosage of coagulants such as Alum, PAC and PACS were investigated. The optimum coagulant dosing amount to make the lowest turbidity of water were 35mg/ι t of Alum, 30mg/ι of PAC and 10mg/ι of PACS in case of 5 NTU of raw water turbidity, and 30mg/ι of Alum, 25mg/ι of PAC and 10mg/ι of PACS in case of 10 NTU of that, respectively. The removal rates of turbidity at 4 min. and 8 min. of settling time were 10 and 72% of Alum, 44 and 62% of PAC and 25 and 55% of PACS in case of 5 NTU, and 52 and 70% of Alum, 90 and 95% of PAC and 10 and 28% of PACS in case of 10 NTU, respectively. Judging from the settling capability of floc., the reaction time of floe. formation and removal efficiency of turbidity, PAC was evaluated as more effective coagulant than Alum and PACS. Also PAC was regarded as the most effective coagulant when the water supply was changed sharply and the fluctuation of the surface loading occured with wide and sharp in settling basin. pH and alkalinity of the water were decreased with increasing coagulants dosage. But pH and alkalinity were not decreased below 5.8 which is the standard for drinking water quality, and 10mg/ι which is the limit concentration of floc. breakage, respectively. Residual Al of the treated water was decreased with increasing coagulants dosage in case of 5 and 10NTU of raw water turbidity. $KMnO_4$ consumption of the water was decreased with increasing coagulants dosage. The reduction rate of $KMnO_4$ consumption at the optimum coagulants dosage were 39% of Alum. 18% of PAC and 11% of PACS in case of 5 NTU of raw water turbidity, and 42% of Alum, 27% of PAC and 36% of PACS in case of 10 NTU of that, respectively. Any relationship was not found between the removal rate of turbidity and KMnO$_4$ consumption. TOC of the water was a bit decreased with increasing coagulants dosage up to 30mg/ι but not changed above 30mg/ι of coagulants dosage. The degree of TOC reduction was increased in the order of Alum, PAC and PACS treatment. Zeta potential of the colloidal floe. at the optimum coagulants dosage was in the range of -20~-15mV in case of 5 NTU of raw water turbidity and 0~0.5mV in case of 10 NTU of that. respectively. Although the kinds and dosages of coagulants were different, zeta potential range were fixed under the conditions of the best coagulation efficiency.

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A Study on Solid-liquid Separation of Swine Wastewater Using Coagulation and Dissolved Air Flotation (응집침전 및 부상분리에 의한 돈사폐수의 고액분리에 관한 연구)

  • Kim, Jong-Oh;Jeong, Seong-Uk
    • Journal of the Korea Organic Resources Recycling Association
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    • v.12 no.2
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    • pp.101-109
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    • 2004
  • In this study, the solid-liquid separation characteristics of swine wastewater were investigated for the coagulation and dissolved air flotation (DAF). Coagulation characteristics were studied using jar-tester with the different coagulants and dosage amounts. DAF characteristics were also investigated in terms of the different flotation conditions with the raw swine wastewater, pH adjustment only, and adding coagulants. When the raw swine wastewater was coagulated with the only inorganic coagulants, the proper inorganic coagulants were founded as $FeCl_3$ > PAC > Alum orderly, and the optimal coagulant dosages were founded as $1,000mg/{\ell}$, $1,500mg/{\ell}$, $1,500mg/{\ell}$, respectively. As the raw swine wastewater was treated with the polymer coagulants, the only cationic polymer coagulant showed an effective coagulation and the optimal dosage of cationic coagulant was founded as $200mg/{\ell}$. When the different dosages of cationic polymer was added to each $500mg/{\ell}$ of the inorganic coagulants, the proper inorganic coagulants were founded as $FeCl_3$ > Alum > PAC orderly, and optimal cationic polymer dosages was founded as $25mg/{\ell}$, $25mg/{\ell}$, and $100mg/{\ell}$, respectively. Resulting from the raw swine wastewater experiments using DAF without coagulation, the proper operation conditions of DAF were set to 400% of recycling ratio, 4 atm in air dissolving tank, and under pH 3. But the raw swine wastewater was difficult to successfully operate DAF without pre-coagulation. While the DAF separation after pre-coagulation using inorganic coagulants was not accomplished due to the low intensity of the floc, DAF after pre-coagulation using both the inorganic and cationic polymer coagulants was accomplished very well. Optimal dosage of cationic polymer coagulant in case of $500mg/{\ell}$ Alum dosage was founded as $500mg/{\ell}$.

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Sequential Washing Techniques for Arsenic-Contaminated Soils near the Abandoned Iron-Mine (폐 철광산 주변 비소로 오염된 토양에 대한 연속 세척기법의 적용)

  • Hwang Jung-Sung;Choi Sang-il;Han Sang-Geun
    • Journal of Soil and Groundwater Environment
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    • v.10 no.1
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    • pp.58-64
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    • 2005
  • Several tests were conducted to determine the optimum operational conditions of soil washing techniques for floe-forming arsenic-contaminated soils, collected from D abandoned Iron-mine in Korea. The optimum cut-off size was 0.15 mm $(sieve\;\#100)$, about $94\%$ of the mass of soils. Both sodium hydroxide and hydrochloric acid were effective to remove arsenic and the optimum mixing ratio (soil [g] : washing solution [mL]) was 1:5 for both washing agents. Arsenic concentrations, determined by KST Methods, for the dried floe solids obtained from flocculation at pH 5-6 were $990\~1,086\;mg/kg$ dry solids, which were higher concentrations than at the other pH values. Therefore, batch tests for sequential washings with or without removing floc were conducted to find the enhancement of washing efficiencies. After removing floe with 0.2 M HCl, sequential washings of 1 M HCl followed by 1 M NaOH showed the best results (15 mg/kg dry soil). The arsenic concentrations of washing effluent from each washing step were about $2\~3\;mg/L$. However, when these acidic and basic effluents were mixed together, arsenic concentration was decreased to be less than $50\;{\mu}g/L$, due to the pH condition of coagulation followed by precipitation for arsenic removal.

The Treatment of Domestic Wastewater by Coagulation-Crossflow Microfiltration (응집-정밀여과에 의한 도시하수의 처리)

  • Sim, Joo-Hyun;Kim, Dae-Hwan;Seo, Hyung-Joon;Chung, Sang-Won
    • Journal of Korean Society of Environmental Engineers
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    • v.27 no.6
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    • pp.581-589
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    • 2005
  • Recently, membrane processes have been replacing the conventional processes for waste water treatment to produce better quality of effluent and to meet more stringent regulations because of water shortage. However, using membrane processes for water treatment has confronted with fouling and difficulty in treating dissolved organic pollutants. In this study, membrane process equipped with crossflow microfiltration is combined with coagulation process using alum and PAC to improve permeability and treatment efficiency. The effects of coagulant dosage and optimum membrane operating conditions were investigated from measurement of permeate flow, cumulative volume, total resistance, particle size, dissolved organic pollutant, dissolved aluminium and quality of effluent. Characteristic of PAC coagulation was compared with that of alum coagulation. PAC coagulation reduced membrane fouling because of forming larger particle size and increased permeate velocity and cumulative volume. Less dissolved organic pollutants and dissolved aluminum made decreasing-rate of permeate velocity being lowered. At using $0.2\;{\mu}m$ membrane, cake filtration observed. At using $0.45\;{\mu}m$ membrane, there was floc breakage due to shear stress occurred born circulating operation. It made floc size smaller than membrane pore size, which subsequently to decrease permeate velocity and to increase total resistance. The optimum coagulation dosage was $300{\pm}50\;mg/L$ for both alum and PAC. PAC coagulation was more efficiently used with $0.2\;{\mu}m$ membrane, and the highest permeate flux was in using $0.45\;{\mu}m$membrane. The greatest efficiency of treatment was as follows; turbidity 99.8%, SS 99.9%, $BOD_5$ 94.4%, $COD_{Cr}$ 95.4%, T-N 54.3%, T-P 99.8%.

Bio-floc technology application in olive flounder, Paralichthys olivaceus aquaculture according to the difference of closed recirculating systems (바이오플락 기술을 활용한 순환침전시스템에 따른 넙치(Paralichthys olivaceus)의 양성)

  • Cho, Yeong-Rok;Kim, Hyun-Soo;Kim, Su Kyoung;Kim, Su-Kyoung;Kim, Seok-Ryel;Hur, Young Baek;Kim, Jun-Hwan
    • Korean Journal of Environmental Biology
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    • v.37 no.2
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    • pp.129-135
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    • 2019
  • Juvenile Paralichthys olivaceus (mean weight 685.3±36.7 g) were raised in different and closed recirculating bio-floc system (control, bio-ball, and shelter) for 7 months. The water environment such as water temperature, dissolved oxygen, salinity, pH, and alkalinity according to the difference of closed recirculating system remained stable during the rearing period. No significant changes were observed in dissolved inorganic nitrogen such as ammonia, nitrite, and nitrate were observed in different closed recirculation system. The final weights according to the difference of closed recirculating were 1,524 g (control), 1,674 g (bio-ball), and 1,630 g (shelter). The survival rate was higher than 98%, and the final FCRs (Feed coefficient ratio) were 1.2, 1.1, and 1.2. The results of this study indicated high growth and survival rate in all systems.

Effects of the Water Quality on the Dispersion Properties of Bentonites Used for Drilling Fluid (시추이수용 벤토나이트의 분산 특성에 미치는 수질의 영향)

  • Akther, Shamima;Hwang, Jin-Yeon;Lee, Hyo-Min
    • Journal of the Mineralogical Society of Korea
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    • v.20 no.1 s.51
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    • pp.21-33
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    • 2007
  • The dispersion/flocculation behavior of bentonite is a major concern in performance of drilling fluid. We studied the dispersion/flocculation characteristics of three commercial bentonites [two CMC (carboxymethyl cellulose) treated and one untreated] in waters of different pHs and salt concentrations. We also examined changes in the viscosity of bentonite suspensions in such waters as a major rheological property of drilling fluid. The dispersion/flocculation behaviors of bentonites were measured by two methods: colorimetric and light scattering method. Light scattering method allows estimating the floc diameter and flocculation rate. The dispersion and flocculation behaviors were diverse with the different bentonites and water qualities. In distilled water, all the bentonites were well dispersed up to first 10 minutes. After that, the CMC-bearing bentonites were flocculated. In salt waters, all the samples were flocculated and the flocculation rate is varied with salt concentration and polymer content. The volume of settled flocs decreased with increasing salt concentration. The flocculation rate and floc diameter increased with decreasing pH of solutions, whereas the volume of settled flocs increased with increasing pH of solutions. The bentonites of fast flocculation behavior had low viscosity. The results of the present study will be helpful in applying bentonites to drilling fluids in diverse environments.

Treatment of Dredging Suspended Solids Using Chitosan Coagulant (Chitosan 응집제를 이용한 준설토 부유물질 처리)

  • Lee, Jun-Ho;Yang, Seung-Ho;Shin, Yiung-Kyewn;Bang, Ki-Woong
    • Journal of Korean Society of Environmental Engineers
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    • v.33 no.11
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    • pp.834-846
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    • 2011
  • The objective of this study is to development of IDFIS system, that are consisted of hydrocyclone, rapid flocculation and inclined settler with chitosan coagulant. As the results of Jar test, a chitosan optimum dosage of 40 mg/L for river sediment, and 5 mg/L for tunnelling wastewater sediment, which these conditions leaves of residual turbidity of less than 5 NTU. Because of the effectiveness of chitosan in removing turbidity was independent on pH, the operation of IDFIS system would be simple. The synthesized turbidity was made with clay particles, river sediment, river suspended sediment, and tunnelling wastewater sediment. Results indicate that the mean overall removal efficiency of turbidity, SS, COD and TP were 98%, 99%, 85% and 95%, respectively. Chitosan is very efficient in removing turbidity in the entire turbidity range examined. IDFIS system would have possibility with compact design, because of the increase of floc size favours the floc settling speed and reduces the settling time.

Complete genome sequence of Comamonas sp. NLF-7-7 isolated from biofilter of wastewater treatment plant (폐수처리장의 바이오 필터로부터 분리된 Comamonas sp. NLF-7-7 균주의 유전체 염기서열 해독)

  • Kim, Dong-Hyun;Han, Kook-Il;Kwon, Hae Jun;Kim, Mi Gyeong;Kim, Young Guk;Choi, Doo Ho;Lee, Keun Chul;Suh, Min Kuk;Kim, Han Sol;Lee, Jung-Sook;Kim, Jong-Guk
    • Korean Journal of Microbiology
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    • v.55 no.3
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    • pp.309-312
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    • 2019
  • Comamonas sp. NLF-7-7 was isolated from biofilter of wastewater treatment plant. The whole-genome sequence of Comamonas sp. NLF-7-7 was analyzed using the PacBio RS II and Illumina HiSeqXten platform. The genome comprises a 3,333,437 bp chromosome with a G + C content of 68.04%, 3,197 total genes, 9 rRNA genes, and 49 tRNA genes. This genome contained pollutants degradation and floc forming genes such as sulfur oxidization pathway (SoxY, SoxZ, SoxA, and SoxB) and floc forming pathway (EpsG, EpsE, EpsF, EpsG, EpsL, and glycosyltransferase), respectively. The Comamonas sp. NLF-7-7 can be used to the purification of wastewater.