• 한국양식학회지
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• 제18권3호
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• pp.180-188
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• 2005

The separation performances for thirty different dimensions of a low-pressure hydrocyclone (LPH) were tested in order to obtain an optimum dimension scale for fecal solid removal from an aquaculture system. The geometric variables were considered on two inlet diameters (Di: 30 and 50 mm), five overflow diameters (Do: 30, 50, 60, 70 and 100 mm), and three cylinder lengths (Lc: 250, 345 and 442 mm), while the cylinder diameter (Dc) of 335 mm, underflow diameter (Du) of 50 mm and cone angle (${\theta}$) of $68^{\circ}$ were kept constant. A small size for carp feces was regarded as the target for the removal of solids. Spherical polystyrene particles (1.1-1.3 mm dia., ${\rho}_s=1.05g/cm^3$), which demonstrate a similar settling velocity and specific gravity to the carp feces, were used as feed. The separation performance was tested in the range of 330 to 1200 ml/s of the inflow rate. Experimental results using ANCOVA and the Tukey test (${\alpha}=0.05$) demonstrated that the separation performances of LPH were significantly affected (P<0.05) by fi, Di and Do. In contrast, there was no significant Lc effect (P>0.05) on the separation performances. The maximum separation performance was detected at dimension combinations of 30 mm of inflow diameter (Di), 50, 60 and 70 mm of overflow diameter (Do), 345 mm of cylinder length (Lc). The dimension proportions were 0.09, 1.03, 0.15-0.21 and 0.15 (or Di/Dc, Lc/Dc, Do/Dc and Du/Dc, respectively.

• 한국양식학회지
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• 제18권3호
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• pp.189-195
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• 2005

By testing the separation performance for a fine settleable solid removal system in an aquaculture system using polystyrene particles as an experimental substitute, the optimal geometric dimensions for a Low-Pressure Hydrocyclone (LPH) were obtained. The design approach far the LPH took into consideration two inflow diameters (Di: 30, 50 mm), three overflow diameters (Do: 60, 70, 100 mm) and four cylinder lengths (Lc: 250, 345, 442, 575 mm), while the cylinder diameter (Dc) at 335 mm, the underflow diameter (Du) at 50 mm and the cone angle (${\theta}$) at $68^{\circ}$ were kept constant. The separation performances of 19 different dimension combinations of LPH were tested, ranging from 300 to 1200 ml/sec of inflow rate using substitute polystyrene particles (0.4-0.7 mm dia., ${\rho}_s=1.05g/cm^3$). These polystyrene particles exhibit a similar density and settling velocity to the fine fecal debris of the common carp. The total separation efficiency for the inflow rate ranged from a high of 97% to a low of 20%. Experimental results obtained by ANCOVA and the Tukey test (${\alpha}=0.05$) showed that the separation performances of the LPH were significantly affected (P<0.05) by the fi, Di, Do and Lc. The maximum separation performance was detected at a dimension combination of 30 mm of inflow diameter (Di), 60 mm of overflow diameter (Do), 442 and 575 mm of cylinder length (Lc). The dimension proportions were 0.09, 1.32-1.72, 0.18 and 0.15 for Di/Dc, Lc/Dc, Do/Dc and Du/Dc respectively.

• Fisheries and Aquatic Sciences
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• 제13권2호
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• pp.150-156
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• 2010

The separation performance of a low-pressure hydrocyclone (LPH) was evaluated for suspended-solids removal in a recirculating aquaculture system (RAS). The dimensions of the LPH were 335 mm cylinder diameter, 575 mm cylinder height, 60 mm overflow diameter, 50 mm underflow diameter, and $68^{\circ}$ cone angle. The inflow rate varied (400, 600, 800, and 1,000 mL $s^{-1}$) with 25%, 25%, 20%, and 10% of bypass ($R_f$), respectively. The maximum total separation efficiency (Et) and reduced separation efficiency (E't) for suspended solids from the effluent of the second settlement tank (before biofiltration) were 58.9% and 45.2%, respectively, at an inflow rate of 600 mL $s^{-1}$ and 25% of $R_f$. The maximum Et and E't for suspended solids from the water supply channel (after biofiltration) were 24.4% and 16%, respectively, at an inflow rate of 1,000 mL $s^{-1}$ and 10% of $R_f$. The maximum grade efficiency (Ei) was 51.6% for a 300 ${\mu}m$ particle size at an inflow rate of 600 mL $s^{-1}$ with 23% of $R_f$. The maximum reduced grade efficiency (E'i) was 37.6% for a 300 ${\mu}m$ particle size at an inflow rate of 1,000 mL $s^{-1}$ with 11% of $R_f$. The results indicate that the separation performance of the LPH for suspended solids removal was size selective and that maximum removal occurred at particle sizes ranging from 300 to 500 ${\mu}m$.

• 자원리싸이클링
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• 제24권4호
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• pp.56-60
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• 2015

광물찌꺼기의 효율적인 활용을 위하여 부유선별공정에서 배출되어 1차 분급된 시료를 대상으로 정밀분급을 실시하였다. 0.1 MPa - 0.3 MPa의 주입압력(공급유량)과 5% - 15%의 광액농도 조건에서 2인치 습식사이클론을 이용하여 분급시험을 진행한 결과, 주입압력 (공급유량)이 감소할수록 광액농도가 증가할수록 분리입도는 증가하였다. 광액농도 5%와 주입압력 0.3 MPa의 조건에서 overflow와 underflow의 평균입도는 각각 $6.56{\mu}m$와 $55.45{\mu}m$를 나타내었다. 분급효율은 광액농도를 증가시키거나 주입압력을 감소시킬수록 이상적인 분급효과에 근접하였다. 광액농도가 증가할수록 탈수효과는 증가하며, 주입압력에 따른 변화는 크지 않았다. 광액농도 15 %와 주입압력 0.3 MPa의 조건에서 underflow의 함수율은 27.9%로 나타났다.

• 자원리싸이클링
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• 제7권2호
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• pp.23-30
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• 1998

제철소의 고로에서 발생하는 슬러지로부터 산화철 및 탄소분과 같은 유용 성분을 회수하여 리싸이클링하기 위하여 슬러지의 물리화학적 특성과 습식 사이클론을 이용한 분급특성을 조사형T다. 슬러지 입자의 크기에 따른 성분의 부존 상태를 조사한 결과, 탄소는 graphite 상으로 주로 굵은 입자에, 아연은 zinc sulfide로서 주로 미세한 입자에 분포하였다. 그러나 슬러지 중에 hematite 및 magnetite 상으로 존재하는 철분은 입경에 따른 편석이 없었다. 내경 75mm인 습식 사이클론에서 적정한 조건으로 고로슬러지를 분급하면 저아연 슬러지의 회수율과 탈아연율이 각 67.9~73.6% 및 72.7~86.8% 수준에 도달하였다.

• 한국환경과학회지
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• 제30권12호
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• pp.1081-1092
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• 2021

In this study, the effect on the stability of Aerobic Granular Sludge (AGS) caused by an AGS separator was investigated. The AGS separator was a hydrocyclone. The main factors of the AGS separator were filter pore size (0.125~0.600 mm), conical-to-cylindrical ratio (1.5~3.0), and operating time (1~20 min). The AGS/mixed liquor suspended solid (MLSS) ratio gradually increased to 0.500 mm (AGS/MLSS: 84.3±3.0%). AGS was best separated at the conical-to-cylindrical ratio of 2.5 (AGS/MLSS: 84.7±3.3%). As the operating time increased, the AGS separation performance also tended to increase. The shortest AGS separator run time, but the highest AGS separation performance was 10 min (87.0±2.5%). AGS stability was evaluated by operating the selected AGS separator and sequencing batch reactor. The average removal efficiencies of TOC, TCOD_Cr, SS, TN, and TP were 95.7%, 96.9%, 93.0%, 89.0%, and 96.2%, respectively, which met the effluent standards in Korea. In addition, the AGS/MLSS ratio tended to remain constant, and the sludge volume index demonstrated a tendency to decrease from 140 mL/g to 70 mL/g. During the operation, the particles of AGS in optical microscope observations gradually increased.

• 한국기계가공학회지
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• 제20권11호
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• pp.17-23
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• 2021

A cyclone is a dust-separating mechanism that works on the principle of centrifugal force. The performance of a cyclone is evaluated using pressure loss and collection efficiency. A multi-cyclone arrangement is used to improve the collection efficiency within a limited area. In this study, experiments and numerical analyses were conducted on a dual arrangement of mini-hydrocyclone separators, which was fabricated using 3D printing. The experiment was performed at an inlet flow rate of 0.7 m/s, and alumina powder with a particle size of 0.5, 15, and 50 ㎛. ANSYS FLUENT, was used for the numerical analysis. The reliability of the numerical analysis was verified through a comparison with the experimental results. The errors in the experiment and numerical analysis were confirmed to be 2% at the outlet flow rate.

• 대한환경공학회지
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• 제33권11호
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• pp.834-846
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• 2011

본 연구의 목적은 하천, 호수의 준설 시에 발생하는 준설토 사토장에 저류된 부유물질을 hydrocyclone을 이용하여 모래입자를 분리하고, 부유미세입자 및 오염물질을 처리하기 위해 키토산 응집제를 이용하여 고속 응집과 침전이 가능한 IDFIS 시스템을 개발함에 있다. 응집교반실험 결과 키토산 주입농도는 하천퇴적물질의 경우 40 mg/L, 터널굴착 퇴적물질의 경우 5 mg/L에서 잔류탁도는 5 NTU 이하를 나타내었다. 키토산응집제는 응집, 응결조건에 pH 영향이 거의 없으므로 처리장치 운전의 용이성에 기여할 것으로 판단된다. IDFIS장치를 이용하여 황토입자, 하천퇴적물질, 하천부유사 퇴적물질, 터널굴착 퇴적물을 대상으로 제거특성을 분석한 결과 전반적인 평균 처리효율은 탁도 98%, SS 99%, COD 85%, TP 95%를 나타내었다. 키토산응집제는 다양한 탁도 범위에서도 입자물질의 제거에 매우 효과적인 것으로 분석되었다. IDFIS장치는 키토산응집제로 빠르게 형성된 플럭을 높은 수면적부하율로 처리 가능하여 집적화된 처리장치로서 활용도가 높을 것으로 판단된다.

• 한국자원리싸이클링학회:학술대회논문집
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• 한국자원리싸이클링학회 1993년도 EARTH 발표논문초록
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• pp.14.1-14
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• 1993

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2002년도 총회 및 춘계학술발표회
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• pp.54-57
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• 2002

Pretreatment technologies are defined as technologies that prepare or condition dredged material for subsequent, more rigorous treatment processes. The objectives of this study are to test the feasibility of treating dredged sediment using pretreatment process(hydrocyclone, sedimentation basin, and flotation), and to estimate design parameters for a pilot-plant design. The final goal of the project is to recycle the dredged sediment that is otherwise reused as construction materials.