A centrifugal cyclone dust collecting apparatus includes a hydro cyclone dust collecting apparatus for separating solid or liquid using liquid or suspension as a medium. In this study, the formation mechanism and improvement of air core and inner air layer were confirmed through Particle Image Velocimetry. These results showed that the modified experimental model was designed in the conventional method suitable for the separation of juvenile fish and eggs. The inlet speed of the multi-stage hydrocyclone dust collector, which can increase the inlet velocity and minimize floatage in the turbulence chamber, was increased from 0.15 to 0.30 m/s. As a result, the air core was stably formed, the inner air layer was increased with increasing speed. In addition, the dust collecting efficiency of egg and juvenile fish was 97.8% on average, It can infer that this system confirmed the ability to efficiently collect particles of 40 μm or more.

The performance of inorganic sludge separation system is evaluated. Anaerobic digester effluent sludge is used for feed sludge of this system and hydrocyclone is used for inorganic sludge separation. For phosphorus removal and recovery MgCl2 is pumped into MAP growth tank, a component of inorganic sludge separation system. Using this system inorganic sludge which contained less than 40 % of organic matter can be discharged stably and the maximum amount of separated inorganic sludge is 13.4 % of influent sludge based on dry solid. The amount of phosphorus recovered as MAP(as P) is 16.7 % to influent T-P.

Ballast water of ten billion tons are transferred by the ship annually in the world. Because alien creatures are destroying aquatic ecosystems, ballast water treatment is needed. Physical methods of treatment using the filtration method is hydrocyclone. The advantage of hydrocyclone is to create a simple structure and a easy separation of good performance. A commercial CFD code CFX 11.0 is applied to analyze hydrocyclone. According to the shape changes of the hydrocyclone, separation performance was compared. The results show that when you reduce the height of hydrocyclone, hydrocyclone separation efficiency is lowered.

하이드로사이클론은 다양한 산업 방면의 고·액 분리를 위해 널리 사용되어왔다. 왜냐하면 하이드로사이클론의 적당한 응용으로 폭넓은 범위의 입자에 적용이 가능하기 때문이다. 불순물을 함유한 해수가 펌프나 열교환기로 흘러가면 그것은 해수 냉각시스템의 효율을 저하시키는 원인이 된다. 본 연구에서는 하이드로사이클론을 이용한 해수 냉각시스템에서 불순물을 분리하는 몇가지 방법을 제시했다. 설계의 영향을 미치는 인자로서 고체농도, 사이클론 입구압력, 하부배출구의 직경과 유량에 따른 하이드로사이클론의 분리효율에 대해 연구를 하였다. 이 연구의 결과는 다음과 같다. 1) 고형물질의 농도가 감소할수록 고·액 분리의 효율이 증가하였다. 2) 사이클론 입구압력이 증가함에 따라 분리효율이 증가하였다. 결과적으로 이 연구에서는 하이드로사이클론을 기계류 냉각시스템의 전처리장치로 사용한다면 엔진시스템에서 예상치 못했던 사고를 방지할 수 있을 것이다.

The purpose of this study was to evaluate the operational characteristics of wastewater treatment using Sequencing Batch Reactor (SBR) with Aerobic Granular Sludge (AGS) separator in the pilot plant. Pilot plant experiments were conducted using SBR with AGS separator and pollution removal efficiencies were evaluated based on the operational condition and surface properties of AGS. The results of the operation on water quality of the effluent showed that the average concentration of total organic carbon, suspended solids, nitrogen, and phosphorus was 6.89 mg/L, 7.33 mg/L, 7.33 mg/L, and 0.2 mg/L, respectively. All these concentrations complied the effluent standard in Korea. The concentration of mixed liquor suspended solid (MLSS) fluctuated, but the AGS/MLSS ratio was constant at 86.5±1.3%. Although the AGS/MLSS ratio was constant, sludge volume index improved. These results suggested that the particle discharged fine sludge and increased the AGS praticle size in the AGS. Optical microscopy revealed the presence of dense AGS at the end of the operation, and particles of > 0.6 mm were found. Compared to those of belt-type AGS separator, the required area and power consumption of the hydrocyclone-type AGS separator were reduced by 27.5% and 83.8%, respectively.

본 연구에서는 원심력을 이용한 하이드로싸이클론을 준설된 호소 퇴적물의 처리 공정에 적용하는 실험을 수행하였다. 준설된 퇴적물의 안정화 및 위생적 처리를 위해서는 경우에 따라 탈수 및 분급공정이 필요하다. 본 연구에서는 이러한 공정에 하이드로싸이클론을 적용하였으며, 실온에서 실제 호소 퇴적물과 폐 석탄회를 이용하여 분리효율을 실험하였다. 본 연구 결과 하부배출구의 크기는 한계분리입경(d(sub)50)에 큰 영향을 미치는 것을 알 수 있었고, 비중이 큰 입