• 한국염색가공학회지
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• 제9권6호
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• pp.26-32
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• 1997

In order to remove the pollutants effectively in the dye-processing wastewater by chemical precipitation, coagulation and flocculation test was carried out using several coagulants on various reaction conditions. It was found that the Ferric sulfate was best coagulant for the treatment of mixed dye-processing wastewater. When the Ferric sulfate dosage was 1,100mg/$\ell$, the COD removal rate was very high(50%), and the color was removed very effectively. The COD was decreased relatively well up to 40%, when Alum was dosed as coagulant. But it was difficult to remove the color effectively. Test results about COD removal for the Ferrous sulfate and the Ferric chloride used were mostly same as those of the Alum used. However, the color removal by the Ferrous sulfate was much better than the case of the Alum or the Ferric chloride. It was found that the COD removal was increased and the sludge yield was decreased by pH control before polymer flocculant addition, during the jar test for the Ferrous sulfate and the Ferric sulfate as a coagulant.

• 한국환경과학회지
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• 제28권11호
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• pp.927-933
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• 2019

A lipid-enriched strain of Botryococcus braunii (UTEX 572) was cultivated in a semi-batch aeration tank to enhance biomass as well as to develop intracellular lipids and fatty acids. A 30 day period of incubation produced 1.39 g/L of biomass and 0.31 g/L of total lipids in the biomass. The grown biomass was pre-treated using several methods to extract the total lipid content efficiently: ultrasonication was found to yield the highest percentage of lipids-namely 19.8% per biomass. Direct heating of biomass in an autoclave also showed better performance than when using only conventional solvent extraction. To enhance the biomass harvest and lipid extraction efficiency, coagulation and flocculation steps were added to the extraction process. It is noteworthy that not only the solvent type but also the solvent/biomass ratio greatly affected efficiency. In addition, the moisture content of the harvested(wet) biomass affected the efficiency significantly. This study elucidated the need for future research on optimizing this extraction process.

• 대한환경공학회지
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• 제32권3호
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• pp.248-255
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• 2010

본 연구는 연안해역에서 발생하는 적조의 현장 제어기술로 전자빔을 이용하고자 적조사멸에 대한 전자빔 조사의 효율성을 평가하였다. Prorocentrum minimum, Prorocentrum micans, Cochlodinium polykrikoides, Heterosigma akashiwo, Alexnadrium catenella의 5종을 실험대상 적조로 선정하여 배양하였으며, 실제 경남 통영(2007. 8. 15)에서 발생한 적조에 대해서도 동일한 실험을 수행하였다. 전자빔 조사선량은 1 kGy, 2 kGy, 4 kGy, 8 kGy로 1 kGy의 전자빔 조사로 50~65%의 적조사멸율을 보였으며, 1일 경과 시 86~97% 사멸하였다. Chlorophyll-a의 경우 조사 즉시 50~64% 감소하고, 1일 경과한 뒤 72~93%의 감소율을 보였다. 또한 전자빔 조사 즉시 S-protein은 28~47%, S-carbohydrate는 16~45% 가 증가하였으며, 1일의 시간 경과 후에는 S-protein이 77~138%, S-carbohydrate가 77~212%까지 증가하였다. 또한 투과 전자현미경을 통해 전자빔 조사 전후의 적조세포 관측을 통하여 세포의 파괴 및 세포내 구성물질의 용출을 확인할 수 있었다. 이렇듯 적조에 전자빔을 조사함으로써 Extracellular Biopolymer에 의한 Flocculation을 유도하여 적조를 침강 제어할 수 있다. 또한 전자빔 조사 전 후 Alexandrium catenella의 PSP(Paralytic Shellfish Poisoning) 패독 분석 결과 1 kGy의 전자빔을 조사함으로써 전자빔을 조사하지 않은 적조 대비 PSP 독성 함량이 48% 감소하여 전자빔조사가 유독적조의 사멸 뿐만 아니라 제독에도 효과가 있음을 알 수 있었다.

• 펄프종이기술
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• 제30권3호
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• pp.74-83
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• 1998

The phenomenon of decrease in sizing efficiency when the stock temperature is increased is well recognized as summer sizing, and this is believed to be caused by uneven distribution of sizing agents on paper surface most often incurred by coagulation of sizing agents. When unevenly sized paper is used as coating base stock, nonuniform consolidation of the coating layer may result, which, in turn, causes uneven distribution of binder on coating surface. This causes nonuniform ink absorption to produce print mottle. In this study the effects of simple or polymeric electrolytes, storage temperature and time on the coagulation of cationic dispersed rosin size were investigated using a turbidity measurement method which was verified to correlate well with the particle size of rosin emulsion or its coagulates. Handsheets sized with rosin dispersions coagulated under various conditions were prepared and their sizing degree and coated paper properties including gloss and ink density were examined. The relationship between the sizing nonuniformity of coated papers and its ink absorption property was evaluated. Turbidity of rosin emulsion increased as the storage temperature and time were increased. Addition of simple or polymeric electrolytes caused reduction in $zeta$ -potential of the rosin dispersion and accelerated the coagulation tendency substantially. Reversion of the $zeta$ -potential of rosin dispersion, however, did not occur when coagulation was induced with simple electrolytes. On the other hand, addition of an anionic polyelectrolyte reversed the $zeta$ -potential of the flocculated rosin dispersion. This indicated that electrical double layer compaction and bridging flocculation were coagulation mechanisms for simple and polymeric electrolytes, respectively. Sizing degree decreased as coagulation of rosin was increased. Paper gloss, ink gloss and ink density were increased when sizing degree of base stock was increased most probably due to prevention of base paper swelling and increased binder migration to coating surface. This suggested that uneven printing ink density occurred when uneven sizing development was induced by coagulation of rosin particles.

• 폴리머
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• 제36권1호
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• pp.104-110
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• 2012

LCD 컬러필터에서 안료의 분산은 컬러 강도를 증가시키는 중요한 요소이므로, 안료를 분산시키기 위한 안료 분산제의 첨가는 필수적이라 할 수 있다. 안료 분산제로서의 고분자는 안료와의 친화성을 가지는 anchoring group과 매체와의 혼화성을 가지는 stabilizing group을 포함하고 있다. 원자 이동 라디칼 중합은 잘 규정된 고분자 합성을 가능하게 하는 중합법으로, 이러한 구조를 포함하는 고분자형 안료 분산제를 얻기 위한 적절한 수단이 될 수 있다. Anchor로서 (2-dimethylamino)ethyl methacrylate를, stabilizer로서 oligo(ethylene oxide)methyl ether methacrylate를 각각 선택해 고분자 분산제를 합성하였다. 고분자의 구조 및 조성이 안료 분산에 미치는 영향을 연구하기 위해 다양한 길이의 stabilizing group을 가지는 diblock copolymer를 합성하여 비교하였다.

• 대한환경공학회지
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• 제30권7호
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• pp.721-728
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• 2008

정수처리과정 중 염소처리로 발생되는 소독부산물(DBPs) 발생현황을 파악하고 저감방안을 제시하기 위해 대표적인 염소소독부산물인 트리할로메탄(THMs)의 공정별 발생현황을 조사하였다. 또한, 계절별 수질별 영향인자와의 상관관계를 분석하고, 공정에서 전 염소 다단투입을 통하여 THMs 생성현황을 파악하고, 원수 수질에 따라 THMs을 저감시킬 수 있는 최적의 운영방안을 고찰하고자 하였다. Y 정수센터는 취수장과 착수정간의 도수시간이 평균 10시간이 소요되어 취수장에서 전염소 처리 시 염소와 THMs 전구물질간의 충분한 반응시간을 제공함으로써, THMs 발생을 억제하는데 한계를 가지고 있다. 따라서, 도수관로상의 THMs 생성을 억제하고 염소 과잉투입을 방지하기 위하여 전염소를 취수장과 착수정에 동시에 투입하여 정수중 THMs 발생을 저감시키고자 하였다. 계절별 정수의 THMs 발생량은 저수온기(겨울철)에 0.015 mg/L 이하로 적게 생성되었고, 고수온기(여름철)에는 평균 0.021 mg/L 이상 생성되어 수온상승에 따라 증가하였다. 공정별 THMs 발생량은 전염소 처리 후 착수정 원수에서 평균 0.013 mg/L, 응집/침전/여과 공정에서 0.014 mg/L, 후염소 처리 후 정수에서 평균 0.016 mg/L로 정수처리공정 시 착수정원수에서 대부분의 THMs이 발생하였다. 정수처리 공정에서 트리할로메탄생성능(THMFP)은 응집 침전공정 후 42.7%가 제거되었고, 여과공정 후 약 50%가 제거되어 공정에서 TOC 제거율과 비슷한 추세를 보였다. 전염소 다단투입은 취수장과 착수정에 염소를 분할하여 주입함으로써 유기물질과 염소와의 접촉시간(T) 및 농도(C)를 감소시키고, 염소주입량을 최적화하여 도수관로에서 생성되는 THMs을 억제시키고 염소사용량을 저감시킬 수 있었다. 수온이 높은 하절기에 전염소 다단 투입을 실시한 결과, 정수에서 THMs 농도는 평균 0.013 mg/L이 생성되어 취수장 단독 전염소 처리 시기에 발생된 정수 THMs 농도 대비 약 50%를 저감시킬 수 있었다.

• 한국지반환경공학회 논문집
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• 제8권3호
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• pp.5-10
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• 2007

본 연구는 도시하수와 응집, 오존처리, UV와 같은 물리화학적 방법으로 처리된 하수 속에 함유되어 있는 비 규제 유기오염물의 GC/MS를 통한 정성적 분석결과를 나타내었다. 하수 속에 함유된 주요 유기오염물질로는 식품 또는 가정, 공업적 사용으로부터 배출된 물질이 주류를 이루었다. 하수처리장의 생물학적 공정으로부터 몇몇 유기오염물질들의 처리효율은 효과적이었지만 일부의 유기오염물질의 제거는 그리 효과적이지 못하였다. 그러므로 생물학적 방법으로 처리가 효과적이지 못한 물질들의 처리를 위한 고도처리방법의 적용과 가정에서의 이러한 물질이 함유된 제품의 사용에 좀 더 적극적인 조절이 필요 할 것이다. 본 연구에서 얻은 결과는 하천유역에서 이들 오염물질의 특성 및 생태계에 대한 오염물질의 배출 평가에 기여를 할 수 있을 것이다.

• 한국물환경학회지
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• 제23권6호
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• pp.843-849
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• 2007

Monitoring of NOM characteristics is important for improving removal efficiency of natural organic matter (NOM) in water treatment processes. In this study, several NOM characteristics, which include specific UV absorbance (SUVA), total carbonate content, molecular weight distribution, and fluorescence properties, were measured using samples collected from a pilot-scale water treatment plant consisting of coagulation/flocculation (C/F), filtration, ozonation and granular activated carbon (GAC) processes. The highest removal of NOM was observed in C/F and filtration processes as demonstrated by the reduction of dissolved organic carbon (DOC) by 25% and 21%, respectively. Despite nearly no change in DOC, however, the lowest SUVA value and the highest total carbohydrate content were observed in the sample from ozonation process. This indicates that non-degradable aromatic compounds become depleted and biodegradable organic compounds are enriched during the process. Comparison of synchronous fluorescence spectra of the samples showed that ozoation process increased protein-like fluorescence while it decreased fulvic-like and terrestrial humic-like fluorescence. Consistently, a slight peak of protein-like fluorescence was observed in the sample from ozonation process. The greatest change in molecular weight distributions of the samples was observed in C/F process. Comparison of size exclusion chromatogram of the samples revealed that NOM fractions with the molecular weight greater than 2000 Da were reduced by over 90% after C/F process. SUVA values and total carbohydrate content of the samples were well correlated with a ratio of protein-like fluorescence and terrestrial humic-like fluorescence intensities with the correlation coefficients of 0.99 and 0.91, respectively. This suggests that synchronous fluorescence properties of NOM could be used as useful tolls for monitoring changes of some NOM characteristics during water treatment processes.

• 한국펄프종이공학회:학술대회논문집
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• 한국펄프종이공학회 2000년도 제26회 펄프종이기술 국제세미나
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• pp.1-10
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• 2000

The development of paper machines, increasing machine speeds with new, mostly low basis weight and/or high ash content paper grades, as well as the fact that several trends regarding process items have increased the sensitivity of papermaking. At the same time, papermakers are looking for flexibility in the production line. We can say that with all PMs the biggest benefits with the lowest capital spending can be achieved by focusing on improved wet end management. In order to manage wet end chemistry on a paper machine, our goal is to control sub-process through which we can influence the operation of the entire wet end with maximum effect. Key measurements and controls are-white water consistency control which is the most effective way to control retention - charge demand measurement and control which takes care of concentration of the anionic material entering to PM -ash measurements and controls which are deeply related to retention and paper quality This paper presents and concentrates to two of these key controls ; retention and charge. The purpose of charge control is to give the process control the tools to react to changes caused by amount of dissolved and colloida material incoming to wet end system. It is called coagulation or fixing control. Retention control is then taking care of retention aid flow to the process by responding any changes seen in white water consistency. It is called flocculation control. Each of these solutions separately , and even more effectively all together, stabilize the wet end operations and so greatly improve the produced paper quality and machine runnability. Practical results will be presented and they are referring to the latest mill cases. We have developed the first wet end measuring system in the late 1980s and control solutions based on this modern measuring technology were completely updated in 1990s. This paper introduces the principle, operation , and results of our unique wet end analyzers (retention and charge ) which are at the level of automation solutions as a part of paper machine quality control Especially our newest member of the platform , on-line charge analyzer has reached and set new standards to the on-line charge monitoring.

• 펄프종이기술
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• 제32권5호
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• pp.44-53
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• 2000

The development of paper machines, increasing machine speeds with new, mostly low basis weight and/or high ash content paper grades, as well as the fact that several trends regarding process items have increased the sensitivity of papermaking. At the same time, papermakers are looking for flexibility in the production line. We can say that with all PMs, the biggest benefits with the lowest capital spending can be achieved by focusing on improved wet end management. In order to manage wet end chemistry on a paper machine, our goal is to control subprocesses through which we can influence the operation of the entire wet end with maximum effect. Key measurements and controls are - white water consistency control which is the most effective way to control retention. - charge demand measurement and control which takes care of concentration of the anionic material entering to PM. - ash measurements and controls which are deeply related to retention and paper quality. This paper presents and concentrates to two of these key controls: retention and charge. The purpose of charge control is to give the process control the tools to react to changes caused by amount of dissolved and colloidal material incoming to wet end system. It is called coagulation or fixing control. Retention control is then taking care of retention aid flow to the process by responding any changes seen in white water consistency. It is called flocculation control. Each of these solutions separately, and even more effectively all together, stabilize the wet end operations and so greatly improve the produced paper quality and machine runnability. Practical results will be presented and they are referring to the latest mill cases. We have developed the first wet end measuring system in the late 1980s and control solutions based on this modern measuring technology were completely updated in 1990s. This paper introduces the principle, operation, and results of our unique wet end analyzers (retention and charge) which are at the level of automation solutions as a part of paper machine quality control. Especially our newest member of the platform, on-line charge analyzer has reached and set new standards to the on-line charge monitoring.