• 한국정밀공학회:학술대회논문집
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• 한국정밀공학회 1995년도 춘계학술대회 논문집
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• pp.429-433
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• 1995

Compound solid is maded for specially fixed object. A number of compound soild are devided as a unit germetric solid. The special case of rotation about an arbitrary axis makes according selection modelfor transformation. View plane and View region are estiblished for back face removal. After back-face removal eachedge is checked for point of intersection. The designing of of fset surface id maded and tool-path gernerted on the part surface. In tersection point is checked among the offset surfaces. The paper used an efficient algorithm for generating tool paths to apply a notion view volume. Through machining experiments with a 3-axis machining centre, the adequacy of the analysis was confirmed.

• 대한환경공학회지
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• 제29권2호
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• pp.229-234
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• 2007

본 연구에서는 고형물 체류시간, 수리학적 체류시간, 생흡착시간 및 온도 변화가 이단슬러지 유형의 연속회분식반응기 공정 운영에 어떻게 영향을 주는지를 조사함으로서 본 공정을 최적화 하고자 하였다. T-N 제거에 있어서 고형물 체류시간이 증가할수록 T-N 제거효율이 증가하는 경향을 관찰할 수 있었는데 이는 SRT가 증가할수록 SCOD 생흡착효율의 증가와 관련이 있을 것으로 판단된다. HRT 영향에 있어서 HRT 8시간, 10시간 및 15시간에서 암모니아성 제거효율 및 T-N 제거효율은 각각 HRT 영향에 관계없이 거의 같았다. 생흡착시간을 20분 이상 증가시켜도 T-N 제거효율 향상에는 도움이 되지 않는 것으로 관찰되었다. 서로 다른 온도 조건에서 공정 제거 효율 비교에 관해 조사한 결과 온도의 감소가 공정 성능에 영향을 주지는 않았으나 인 제거 효율에 있어서 높은 온도에서보다 낮은 온도에서 인 제거효율이 다소 높게 관찰되었다. 결과적으로 본 연구에서 개발된 공정은 낮은 온도 조건 및 높은 유입 부하를 가진 폐수처리에 적합한 것으로 나타났다.

• 한국광물학회지
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• 제32권1호
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• pp.1-14
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• 2019

본 연구는 금 정광에 함유된 비소(As) 및 비스무스(Bi)와 같은 페널티 원소(penalty elements)를 제거하기 위한 목적으로 마이크로웨이브-질산침출을 이용하였다. 또한, 금 정광 시료로부터 금 함량을 증가시키고자 하였다. 침출조건은 페널티 원소의 제거를 향상시키기 위해 질산농도, 침출시간 그리고 고액비를 변화하였다. 실험결과 고체-잔류물에서 시료무게 감소율, 비소와 비스무스의 제거율 그리고 금 함량은 질산농도와 침출시간이 증가할수록 그리고 고액비가 감소할수록 증가하였다. 최대 비소와 비스무스 제거율 및 금 함량이 얻어지는 침출조건은 질산용액의 농도 6 M, 침출시간 5분이었다. 이때, 고체-잔류물 시료의 무게 감소는 87 %, 비소 제거율은 98.23 %, 비스무스는 거의 제거(100 %)되었고 금 함량은 81.36 g/t에서 487.32 g/t으로 증가하였다. 고체-잔류물을 XRD로 분석한 결과, 질산농도가 증가할수록 황철석 피크들은 사라지고 반면에, 원소 황의 피크들이 증가하였다.

• 청정기술
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• 제16권1호
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• pp.39-45
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• 2010

본 연구에서는 국내 우리텍사의 PVDF계 중공사 막을 4 bundle 씩 묶어 모듈을 제작하였으며, 처리용량은 10 ton/day로 설정하여 반응조 내 부유고형물(suspended solid; SS) 의 농도구배가 없도록 하부로부터 간헐 폭기하는 방식을 선택하여 부산 수영하수처리장에 pilot plant를 설치하였다. Pilot plant는 정상 운전을 위하여 하수처리장의 폭기조로부터 유입된 mixed liquor suspended solid (MLSS) 1,000 ppm 정도의 원수를 시험 여과하고, 세척수로 2회 세척, 10% 에탄올 용액으로 1회 세척, 그리고 NaOCl 5% 용액으로 1회 세척 과정을 거치고 마지막으로 세척수로 최종 세척한 후 운전하였다. 결과적으로, 화학세정 후 membrane bioreactor (MBR) 내의 잔류수를 원수로 운전한 결과 SS 제거효율이 99.9% 이상을 보이고 있는 결과와 폭기조 유입수를 원수로 운전하여, 여과 수량은 초기 조건에 비해 16% 감소, suction pressure 는 30% 상승하고 있음을 확인한 결과를 연속 운전 조건으로 설정하였다. 연속 운전한 결과, 유입수 mixed liquor suspended solid (MLSS)가 1,900 mg/L의 조건에서 SS 제거 효율은 99.99% 이었으며 여과수량은 $42{\sim}52L/m^2$ h, suction pressure가 16~20 cmHg로 안정 상태로 운전되고 있음을 확인하였다. 다만, 여과수 저장조의 유출구와 유입구에서의 SS 제거 효율에 영향을 미치는 조류의 발생 억제에 관한 방법이 재고되어 여과수의 재이용 범위를 설정할 필요가 있을 것으로 판단된다.

• 한국분말재료학회지
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• 제9권4호
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• pp.235-244
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• 2002

The effects of residual impurities on solid state sintering of the powder injection molded (PIMed) W-15wt%Cu nanocomposite powder were investigated. The W-Cu nanocomposite powder was produced by the mech-ano-chemical process consisting of high energy ball-milling and hydrogen reduction of W blue powder-cuO mixture. Solid state sintering of the powder compacts was conducted at $1050^{\circ}C$ for 2~10 h in hydrogen atmosphere. The den-sification of PIM specimen was slightly larger than that of PM(conventional PM specimen), being due to fast coalescence of aggregate in the PIM. The only difference between PIM and PM specimens was the amount of residual impurities. The carbon as a strong reduction agent effectively reduced residual W oxide in the PIM specimen. The $H_2O$ formed by $H_2$ reduction of oxide disintegrated W-Cu aggregates during removal process, on the contrary to this, micropore volume rapidly decreased due to coalescence of the disintegrated W-Cu aggregates during evolution of CO.It can be concluded that the higher densification was due to the earlier occurred Cu phase spreading that was induced by effective removal of residual oxides by carbon.

• 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.

• 한국환경과학회지
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• 제31권1호
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• pp.1-8
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• 2022

In this study, solid-liquid separation conditions for coagulation and sedimentation experiments using inorganic coagulant (aluminum sulfate and Poly-Aluminum Chloride (PAC)) were optimized with brine wastewater discharged by the epoxy-resin process. When the turbidity and suspended solid (SS) concentration in raw wastewater were 74 NTU and 4.1 mg/L, respectively, their values decreased the lowest in a coagulant dosage of 135.0 - 270.0 mg Al³⁺/L. The epoxy resin was re-dispersed in the upper part of wastewater treated above 405.0 mg Al³⁺/L. The removal efficiencies of turbidity and SS via dosing with aluminum sulfate and PAC were evaluated at initial turbidity and SS of 74 - 630 NTU and 4.1 - 38.5 mg/L, respectively. They increased most in the range from 135.0 - 270.0 mg Al³⁺/L. The solid-liquid separation condition was quantitatively compared to the correlation of SS removal efficiency between the coagulant dosage and SS concentration based on the concentration of aluminum ions. The empirical formula, R = be^aD, shows the relationship between SS removal efficiency (R) and coagulant dosage (D) at 38.5 mg/L; it produced high correlation coefficients (r²) of 0.9871 for aluminum sulfate and 0.9751 for PAC.

• 한국환경과학회:학술대회논문집
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• 한국환경과학회 1994년도 봄 특별 환경 심포지움 및 학술발표회 초록집
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• pp.51-58
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• 1994

• 한국물환경학회지
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• 제33권5호
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• pp.572-579
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• 2017

Increased impervious surface caused by rapid urbanization serves to produce the discharge of non-point source pollutants such as total suspended solid (TSS). There exist various methods of removing TSS, including a filtration process using granular media (a well-known method to be practically used after the consideration of removal efficiency, clogging, and backwashing efficiency). To determine the TSS removal capability of the filter, we initially performed lab-scale experiments which assessed flow rates, influent concentrations, permeability co-efficients, the particular shapes of suspended solids and potential clogging, and also evaluated TSS removal efficiency when applied to filtration facility in a pilot-scale. In low filtration flux condition, the removal efficiency of suspended solids was more than 95 %, while decreased to 83% in high filtration flux. Regarding the clogging aspect of the experiment, total cumulative solids were loaded up to $19.15kg/m^2$, and TSS removal efficiency was noted to commence to decrease when the loaded solids exceeded $9.0kg/m^2$. It was also noted, however, that superior efficiency was maintained for six hours. In addition, for pilot-scale experiment, the removal efficiency was still high enough (83.4 %) for the solid concentration of 140 ~ 343 mg SS/L and after backwashing, head loss was recovered to 92 ~ 95 % during two hour filtration. With these results, It was confirmed that lifetime of the filter applied to the test was prolonged due to the high treatment efficiency and good backwashing efficiency for the cumulative solids load.

• Membrane and Water Treatment
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• 제10권3호
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• pp.201-206
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• 2019

In this study, we performed an electrowinning process for effective removal of metals (Cu and Ni) in solution and their recovery as solid forms. A complete removal of Cu and Ni (1,000 mg/L) was observed during four times recycling test, indicating that our electrowinning system can ensure the efficient metal removal with high stability and durability. In addition, we investigated effect of operation parameters (i.e., concentration of boric acid only for Ni, variation of pH, concentration of electrolyte ($H_2SO_4$), and cell voltage) on the efficiency of metal removal (Cu and Ni) during the electrowinning. The addition of boric acid significantly enhanced removal efficiency of Ni as the concentration of boric acid increased up to 10 g/L. Compared to negligible pH effect (pH 1, 2, and 4) on the Cu removal, we observed the increase in removal efficiency of Ni as the pH increased from 1 to 4. The electrolyte concentration did not significantly influence the removal of Cu and Ni in this study. We also obtained great removal rates of Cu and Ni at 2.5 V and 4.0 V, which were much faster than those at lower voltages. Finally, almost 99% of each Cu and Ni (1,000 mg/L) was selectively removed from the mixture of metals by adjusting pH and addition of boric acid after the completion of Cu removal. The findings in this study can provide a fundamental knowledge about effect of important parameters on the efficiency of metal recovery during the electrowinning.