• Proceedings of the Korea Water Resources Association Conference
• /
• 2019.05a
• /
• pp.197-197
• /
• 2019

총인처리시설에서는 응집제를 주입하여 인이나 오염물질을 침전시켜 처리하고 있으며 PAC(poly aluminum chloride)나 $FeCl_3$, $Al_2(SO_4)_3$, 등 다양한 종류의 응집제가 사용되어지고 있다. 하지만 기존에 사용되어 지고 있는 알루미늄계열의 응집제는 처리수에 잔류이온이 존재하게 되어 인체에 축적돼 알츠하이머 병 등 신체질환을 유발할 수 있는 단점이 있다. 따라서 이러한 단점을 사전에 예방하기 위해 $TiCl_4$와 같은 티타늄계열 응집제에 대한 연구가 진행되고 있다. $TiCl_4$ 응집제는 인 제거에 효과적으로 적용할 수 있으며 수중에 잔류이온을 유발하지 않으며 Ti이온은 치과임플란트나 의료장비로 사용될 만큼 인체에 무해하다고 알려져 있다. 응집제 사용에 따라 생성된 응집슬러지의 처리방안에 있어서 기존 응집제의 경우 생성된 슬러지의 대부분은 하수슬러지 위탁처리업체를 통해 소각 및 매립, 재활용 되고 있으나, $TiCl_4$를 응집제로 사용할 경우 생성된 슬러지를 인발하여 건조 및 소성을 통해 이산화티타늄으로 재활용할 수 있어 슬러지를 친환경적으로 처리가 가능해 기존 슬러지 처리방안의 경제적, 환경적 부담을 줄일 수 있는 장점이 있다. 따라서 본 연구에서는 $TiCl_4$를 하수처리장 방류수에 주입하여 수중의 총인(T-P)을 처리한 후 생성된 슬러지를 인발하여 건조와 소성과정을 거쳐 이산화티타늄을 제조하였다. 방류수를 취수해 2.5mg/L의 초기 총인 농도를 가진 원수를 제조하였으며 제조된 원수에 $TiCl_4$를 0.6mL 주입하였을 때 99.93%의 총인제거효율을 얻을 수 있었다. 응집 실험 후 생성된 슬러지를 인발하여 건조 후 $300{\sim}1000^{\circ}C$의 각각 다른 온도조건에서 소성하여 이산화티타늄을 제조하였으며, SEM과 XRD를 통해 제조된 이산화티타늄의 표면특성과 결정성 분석을 실시하였다. 제조된 이산화티타늄은 $500{\sim}800^{\circ}C$에서는 아나타제, $900{\sim}1000^{\circ}C$에서는 루타일 결정구조가 나타났다. 또한, $TiCl_4$ 주입량에 따른 이산화티타늄의 최종 생산량과 제조 시 사용되는 건조로 및 소성로의 경제적 비용 등을 고려하여 이산화티타늄 1Ton을 제조하기 위해 필요한 단가를 산출하였다. 본 연구에서 제조된 이산화티타늄 1kg의 생산단가는 약 5,400원으로 나타났으며, 가장 많이 사용되는 P-25 광촉매 보다 저렴한 가격으로 제조 및 판매를 기대할 수 있다. 따라서 하수처리장에 적용 시 기존 응집제 보다 비싼 $TiCl_4$ 비용을 보완하고 친환경적인 슬러지 처리로 제조된 이산화티타늄의 유통 및 현장적용을 통해 경제적, 환경적으로 우수하다고 판단된다.

• Proceedings of the Korean Society of Applied Pharmacology
• /
• 1993.04a
• /
• pp.45-45
• /
• 1993

괄루근으로부터 분리된 다당류에 대하여 continuous gel electrophoresis, SDS-Polyacrylamide gel eletrophoresis, ion exchange column chromatography, Hydroxyapatite column chromatography 및 Gel filtration등의 방법을 이용하여 다음과 같은 결과를 얻었다. 1) 황산암모늄 분별침전법에 의한 렉틴의 정제도는 초추출물의 4.85배이며 DEAE Sephadex A-50 column chromatography법에 의한 정제도는 24.17배로 나타났고, 마지막 정제단계인 Sephacryl S-200 gel filtration에 의한 정제도는 47.34배로 나타났다. 2) 정제된 렉틴의 분자량은 60,000da1ton으로 나타났다. 3) 사람의 혈액형에 따른 응집효과는 90-100％로 특이성은 없었다.

• Journal of the Korea Organic Resources Recycling Association
• /
• v.7 no.1
• /
• pp.13-21
• /
• 1999

The purposes of this research were to evaluate the character of laboratory wastewater, and to examine the utilization of waste egg shells for neutralization and removal of heavy metals. Waste egg shells are excellent at neutralizing acidic wastewater, because they have alkaline minerals such as calcium. It must be seemed that removal rate of heavy metals were very influenced by adsobent dosage and adsorbate concentrations, because waste egg shells acted as precipitation and adsorption. If we reflected the adsorption capacity(k) and adsorption(1/n) of Freundlich isotherm, we couldn't consider waste egg shells as a good adsorbent. In view of these results, it showed that wastes containing the similar compositions as waste egg shells could utilize the neutralization, precipitation and adsorption of heavy metals in laboratory wastewater.

• Korean Chemical Engineering Research
• /
• v.55 no.6
• /
• pp.816-821
• /
• 2017

An integrated slow mixing/sedimentation and net fit fiber filtration system has been developed to reduce the high concentrations of suspended solid (SS) and total phosphorus (T-P) in the reject water from sewage/wastewater. A filtration device used in this experiment consists of coagulation, in-line mixing, air injection, slow mixing/sedimentation, and filtration processes. The performance test using this device was carried out with six operational modes for reject water from sewage treatment plant. Experimental conditions used were 16.7, 33.3, 41.7 and 50.0 ton/day of flow rate and 2~4 of Al/P molar ratio. By injection of coagulant in each operational mode, the high removal efficiencies of SS and T-P were obtained, but continuous operation time was decreased to 7.8~11.4 min in most modes. However, when the Mode 5 of the developed filtration device was applied, the continuous operation time was maintained up to 88.2 min. Also, it was found that the continuous operation time in the Mode 5 using the developed system was increased from 8 to 11.3 times longer than those in other modes. Backwashing flow rate was also very low at 5.4% of total filtered water. Therefore, it can be concluded that the Mode 5 of the developed filtration system was the most efficient treatment method for the removal of high concentrations of SS and T-P.

• Journal of Korean Society of Environmental Engineers
• /
• v.31 no.8
• /
• pp.673-678
• /
• 2009

High-rate phosphorous removal by PAC (poly aluminum chloride) coagulation of A2O effluent was investigate to meet the stringent requirement of wastewater discharge from municipal wastewater treatment plant. A series of jar tests were conducted to find optimum coagulation condition and to enhance removal efficiency. The optimum volumetric concentration of PAC was 30 ppm (2.81mol Al/mol P by mol ratio). Only 17.2% of soluble P was removed for 30 minutes' settling without PAC addition, while this increased to 30.3% by dosing 10ppm PAC. It even increased conspicuously from 49.3% to 88.4% by increasing PAC dose from 20 ppm to 30 ppm. 92.4% of total P was removed by 30 ppm PAC, and the effluent concentration (0.3 mg/L) was acceptable for discharge. The optimum value of coagulation time, settling time, and pH were 4minutes, 20 minutes, and 7.0, respectively. It was not necessary to control pH of raw sample whose pH was 7.0. Soluble P removal was remarkably enhanced at pH 7.0. This implied that sweep floc formation by $Al(OH)_3$ was the main mechanism of coagulation for soluble P removal. Influent and effluent of secondary clarifier were tested for coagulation, and the effluent was better for high-rate P removal. It resulted in 0.18 mg/L of P and 95.4% of P removal by coagulation. It was favorable to recycle the treated water to coagulation tank and the optimum recycle ratio was 0.3.

• Proceedings of the Korea Water Resources Association Conference
• /
• 2020.06a
• /
• pp.210-210
• /
• 2020

LID (Low Impact Development, 저영향개발)는 산업화 및 도시화 진행 지역에서 비점오염원으로부터 배출되는 오염물질을 제어해 개발지역 내 자연순화 기능을 최대한 유지하고, 물순환 기능증대를 통해 강우 유출수를 지역 내에서 관리하는 것을 목표로 한다. 비점오염원 저감 LID 시설에는 자연형과 장치형 시설이 있다. 자연형 시설에는 저류형, 침투, 식생형 시설 등이 있다. 특히, 침투시설에는 대표적으로 투수블럭이 있으며, 이는 투수성 포장재를 통해 강우 유출수를 지하로 침투시켜 여과나 흡착 등으로 비점오염물질을 제어하는 시설이다. 장치형 시설로는 여과재나 망을 이용해 비점오염물질을 분리하는 여과형 및 스크린형 시설, 응집과 침전을 통해 비점오염물질을 분리하는 응집·침전 시설 등이 있다. 이에 본 연구는 2016년부터 2018년 3년간 전주 서곡지구 지역 내 설치된 필터형 투수블럭, 틈새형 투수블럭에서 진행했다. 각각의 투수블럭에서 총 19회, 20회의 강우 모니터링을 실시했고, 오염물질 유입 및 유출 EMC 등의 분석을 통해 유출 및 오염물질 저감효과를 분석했다. 연구 대상 각 투수블럭의 주요 제원은 시설 용량 14.4㎥, 시설 면적은 14.4㎡이다. 모니터링 결과값을 분석한 결과 필터형 투수블럭의 경우 유출 저감율은 17.4 ~ 100%, 틈새형 투수블럭은 29.6 ~ 100%이었다. 필터형 투수블럭과 틈새형 투수블럭의 단위면적당 유량 저감량은 각각 0.014 ~ 0.583㎥/㎡, 0.035 ~ 0.588㎥/㎡이었다. 오염물질 저감효율을 분석한 결과 유기물 항목(BOD, TOC)의 경우 틈새형 투수블럭에서의 저감효율(BOD 93.59%, TOC 90.39%)이 필터형 투수블럭에서의 저감효율(BOD 89.99%, TOC 86.94%) 보다 다소 높게 나타났다. 영양염류 항목(T-N, T-P)의 경우 필터형, 틈새형 모두 비슷한 저감효율(필터형 T-N 89.02%, 필터형 T-P 98.12%, 틈새형 T-N 90.41%, 틈새형 T-P 98.04%)을 보였다.

• Proceedings of the Membrane Society of Korea Conference
• /
• 1991.10a
• /
• pp.49-50
• /
• 1991

최근 산업폐수의 수질오염에 대한 국민적 관심이 높아지면서 정부의 배출수 수질기준강화 및 배출부과금의 인상 등으로 기업의 폐수처리에 관한 인식이 상당히 달라졌다. 기존의 폐수처리는 각공정에서 발생되는 폐수는 종합적으로 수집하여 처리하는 소위 END OF PIPE 처리방법이 대부분이며 산화/환원, 응집/침전, 미생물분해, 여과 등이 주로 사용되고 있다. 그러나 END OF PIPE 처리방식에서는 소량이지만 처리가 어렵거나 독성이 강한 물질이 일부분의 공정에서 발생되어도 분리처리되지 않고 전체적으로 합쳐지므로 처리시설이 복잡하고 규모도 커진다. 따라서 최근의 폐수처리는 각 생산공정에서 발생되는 폐수를 소규모의 처리시설로 처리하기 어려운 소량의 오염물질을 제거하거나 유효성분일 경우 회수하여 재활용하는 방향으로 연구가 진행되고 있다.

• Journal of Korean Society of Environmental Engineers
• /
• v.39 no.12
• /
• pp.689-697
• /
• 2017

As a fundamental study to apply the new flocculation method using ballast in water treatment process, the optimal conditions for general and ballast coagulant dosage, and pH, which are known to have a significant influence, were derived by response surface methodology. Poly aluminum chloride (PAC) and magnetite ballast were used as a general coagulant and ballast, respectively. Coagulation experiments were performed by jar-tester using the kaolin based synthetic water. The effects of three independent variables (pH, PAC, and ballast) on response variables (turbidity removal rate and average settling velocity of flocs) and the optimum condition of independent variables to induce the optimum flocculation were obtained by 17 experimental conditions designed by Box-Behnken procedure. After performing experiments, the quadratic regression model was derived for each of response variables, and the response surface analysis was conducted to explore the correlation between independent variables and response variables. The $R^2$ values for the turbidity removal rate and the average settling velocity were 0.9909 and 0.8295, respectively. The optimal conditions of independent variables were 7.4 of pH, 38 mg/L of PAC and 1,000 mg/L of ballast. Under these conditions, the turbidity removal rate was more than 97% and the average settling velocity exceeded 35 m/h.

• Journal of the Korean Society for Environmental Technology
• /
• v.19 no.6
• /
• pp.570-575
• /
• 2018

The various of raw wastewater inflows to the industrial wastewater treatment plants everyday. This makes it difficult to operate the coagulation and flocculation efficiently as a pretreatment process for the industrial wastewater treatment. Additionally, it causes loads on evaporation and membrane facilities which are the posttreatment and alternative processes. For this reason, this study sampled raw wastewater before and after the NaOH injection. An experiment was conducted to compare the coagulation characteristics according to the methods of coagulant injection (single injection, simultaneous injection, consecutive injection, and inverse injection) aiming at efficient treatment of industrial wastewater. The coagulation experiment was conducted using a jar tester. The TDS removal efficiency by the coagulant injection methods increased in the order of consecutive injection (2.8 %) < single injection (3.9 %) < simultaneous injection(8.1 %) < inverse injection(9.6 %); the TOC removal efficiency grew in the order of single injection (84.3 %) < inverse injection (86.2 %) < consecutive injection (88.6 %) < simultaneous injection (89.1 %); the turbidity removal efficiency grew from single injection (99.7 %) < consecutive injection (99.8 %) ${\fallingdotseq}$ inverse injection (99.8 %) < simultaneous injection (99.9 %). These results show that the simultaneous inorganic coagulant-polymer coagulant injection method was more efficient than the consecutive injection method (inorganic coagulant ${\rightarrow}$ polymer coagulant).

• Journal of Korean Society of Environmental Engineers
• /
• v.27 no.5
• /
• pp.461-467
• /
• 2005

Phthalate esters is recently considered as an environmental pollutant. This study investigated removal methods of phthalate esters in water environment. On tap water treatment condition with batch test, removal efficiency of coagulation precipitation of one oxidation were $26.6{\sim}33.8%$ and $10{\sim}15%$, respectively. Phthalate esters was effectively removed by the activated carbon adsorption process on tap water treatment condition. The operation of raw water with EBCT of 10 minutes on continuous process satisfied the standard of drinking water by the WHO and US EPA when the concentration of phthalate esters was $100\;{\mu}g/L$. On pilot plant test, coagulation precipitation process got $32{\sim}44%$ of removal efficiency, sand filtration process $6{\sim}10%$ and ozone oxidation process $8{\sim}10%$, respectively. DEP, DBP, BBP and DEHP were not detected after the raw water was processed with activated carbon. The actual survey of phthalate esters removal by advanced water treatment showed that $29{\sim}76%$, $3{\sim}29%$ and $17{\sim}22%$ of phthalate esters were removed on coagulation precipitation process, sand filtration and ozone oxidation process, respectively. DEP, DBP, BBP and DEHP were not detected after the raw water was processed with activated carbon.