적조생물의 구제 -1. IOSP에 의한 적조생물의 응집제거-

김성재,조규대,KIM Sung-Jae,CHO Kyu-Dae 한국수산과학회 2000 한국수산과학회지 Vol.33 No.5

IOSP를 이용하여 적조생물입자에 대한 응집실험을 한 결과는 다음과 같다. 본 실험에 사용한 IOSP의 평균 지름은 $11.6{\mu}m$이고, 약$ 77{\%}$의 입자가 $5.0{\~}20.0{\mu}$의 범위에 속하며 변동계수는 $60.1{\%}$이었다. IOSP의 금속성분을 분석한 결과는 $98{\%}$가 칼슘으로서 생석회(CaO)와 같은 성분이었다. IOSP의 전자현미경 사진을 분석한 결과 표면이 매끈한 부정형의 입자로 되어 있었다. IOSP에 해수를 첨가하면 해수중의 $Mg^(+2)$ 이온과 급속하게 반응하여 입자의 표면 주위에 점질성의 $Mg(OH)_2$ 흡수층 (absorption layer)을 형성하여 응집 침전하고 해수의 pH를 10.0 정도까지 상승시켰다. IOSP는 $pH=6.2{\~}12.7$에서 $11.1{\~}50.1 mV$로서 IOSP의 입자가 완전히 용해될 때까지 positive zeta potential을 나타낸 반면 OSP는 pH=9.2, 11.9에서 각각 -42.5, -56.9mV로서 negative zeta potential을 나타내었다. $pNa=2.0{\~}4.0 (10^(-4){\~}10^(-2)M Na^+)$에서 IOSP, OSP의 zeta potential은 거의 일정한 값을 나타내었으나 $pNa=0.0 (1 M Na^+)$에서는 IOSP의 EDL이 매우 크게 압축되어 zeta potential은 거의 0.0mV를 나타내었고 OSP는 -25.4mV의 여전히 높은 negative zeta potential을 나타내었다. IOSP는 $Mg^(+2)$ 이온의 농도가 증가함에 따라 positive zeta potential이 증가하다가 $pMg=3.0 (10^(-3)M Mg^(+2))$에서 감소하는 결과를 나타내었다. 해수 중에서 IOSP는 4.8mV의 positive zeta potential을 나타내었고, OSP와 RTO는 각각 -30.7mV, -9.2mV의 negative zeta potential을 나타내었다. 해수중에서 IOSP의 $Mg(OH)_2$ 흡수층과 적조생물입자 사이에는 positive-negative EDL 반응이 일어나서 이들 둘 사이에는 항상 전기동력학적 인력이 작용하고, 동시에 $Mg(OH)_2$ 흡수층에 의한 전하중화로 인하여 입자 상호간의 응집반응은 극단적 인력이 작용하는 primary minimum에서 일어나고, DLVO 이론에 따라 응집반응은 비가역적아며 매우 신속하게 일어났다. 적조생물입자의 응집제거 효율은 IOSP의 농도 50mg/l까지 급격한 증가를 보이다가 IOSP의 농도가 계속 증가함에 따라서 점점 완만한 증가를 나타내었다. 즉 IOSP의 농도가 증가함에 따라서 지수함수적으로 증가하였다 ($Y=53.81{\times}X^(0.1); R^2=0.9868$).응집 침전은 IOSP 400mg/l 이상에서 거의 완전히 일어났다. IOSP $100mg/l$을 사용하고 G-value를 $1, 6, 29, 139 sec^(-1)$로 단계적으로 증가시키면서 응집 실험을 한 결과 적조생물입자의 응집제거 효율이 각각 $70.5, 70.5, 81.7, 85.3{\%}$로 증가하였다. 이는 응집 반응에서 입자간 충분한 충돌이 일어날 수 있도록 교반하는 것이 매우 중요함을 나타내 주는 것이다. This study was to examine the physicochemical characteristics of coagulation reaction between ignited oyster shell powder (IOSP) and red tide organisms (RTO), and its feasibility, in developing a technology for the removal of RTO bloom in coastal sea,IOSP was made from oyster shell and its physicochemical characteristics were examined for particle size distribution, surface characteristic by scanning electron microscope, zeta potential, and alkalinity and pH variations in sea water. Two kinds of RTO that were used in this study, Cylindrotheca closterium and Skeletonema costatum, were sampled in Masan bay and were cultured in laboratory. Coagulation experiments were conducted using various c(Incentrations of IOSP, RTO, and a jar tester. The supernatant and RTO culture solution were analyzed for pH, alkalinity, RTO cell number, IOSP showed positive zeta potentials of $11.1{\~}50.1\;mV\;at\;pH\;6.2{\~}12.7$, A positive zeta potential of IOSP slowly decreased with decreasing pNa 4,0 to 2,0. When pNa reached zero, the zeta potential approached zero, When a pMg value was decreased, the positive zeta potential of IOSP increased until pMg 3.0 and decreased below pMg 3.0. IOSP showed 4.8 mV of positive zeta potential while RTO showed -9.2 mV of negative zeta potential in sea water. A positive-negative EDL (electrical double-layer) interaction occurred between $Mg(OH)_2$ adsorption layer of IOSP and RTO in sea water so that EDL attractive force always worked between them. Hence, their coagulation reaction occurred at primary minimum on which an extreme attractive force acted because of charge neutralization by $Mg(OH)_2$ adsorption layer of IOSP. As a result, the coagulation reaction was rapidly processed and was irreversible according to DLVO (Deriaguin-Landau-Verwey-Overbeek) theory. Removal rates of RTO were exponentially increased with increasing both IOSP concentration and G-value. The removal rates were steeply increased until 50 mg/l of IOSP and reached $100{\%}\;at\;400\;mg/l$ of IOSP. Removal rates of RTO were $70.5,\;70.5,\;81.7,\;85.3{\%}$ for G-values of $1,\;6,\;29,\;139\;sec^(-1)$at IOSP 100 mg/l, respectively. This indicated that mixing (i.e., collision among particles) was very important for a coagulation reaction.

적조생물의 구제 -2. 황토에 의한 적조생물의 응집제거-

김성재,KIM Sung-Jae 한국수산과학회 2000 한국수산과학회지 Vol.33 No.5

점증하는 적조로부터 수산피해를 줄이는 것은 시급한 문제이다. 황토를 살포하여 적조생물입자를 응집 제거하는 것이 하나의 방법이 되고 있다. 황토를 이용하여 적조생물입자에 대한 응집실험을 한 결과는 다음과 같다. 본 실험에 사용한 황토입자의 입도 분포는 정규분포를 보여주는 하나의 peak로 나타났으며, 입자의 평균 지름은 $25.0 {\mu}m$이고, 약$84.5{\%}$의 황토입자가 $9.8-55.0{\mu}m$의 범위에 속하며 변동계수는 $65.1{\%}$이었다. 황토의 금속성분을 분석한 결과는 규소 (Si)가 $48{\%}$, 알루미늄 (Al)이 $35{\%}$, 철 (Fe)이 $11{\%}$로서 $94{\%}$를 차지하며 나머지 $48{\%}$는 칼릅 (K), 구리 (Cu), 아연 (Zn), 티타늄 (Ti) 등으로 구성되어 있었다. 전자현미경 사진에 나타난 황토입자의 표면은 거칠고 다공질이며 부정형의 입자로 되어 있었다. 황토입자는 $10^(-3)M$ NaCl의 수용액 중에서 pH가 증가함에 따라 negative zeta potential 값이 증가하여 pH 9.36에서 -71.3mV를 나타내고 이후 거의 일정한 값을 나타내었으며, pH 1.98에서 +1.8 mV를 나타내어 amphoteric surface charge를 가지는 물질의 성질을 나타내었다. 전하결정이온은 $H^+, OH^-$ 이온이고, pH 2 부근에서 PZPC를 나타내었다. 용액의 전해질이 NaCl일 경우 $10^(-2)M (pNa=2)$ 이상의 농도에서는 $Na^+$ 이온의 농도가 증가함에 따라서 황토입자의 negative zeta potential 값은 일률적으로 감소하다가 $Na^+$ 이온의 농도가 1M (pNa=0)이 되었을 때 zeta potential은 0에 근접하였다. 용액의 전해질이 2 :l electrolyte ($CaCl_2$와 $MgCl_2$)의 경우 $Ca^(+2)$ 이온의 농도가 증가함에 따라서 황토입자의 negative zeta potential 값이 일률적으로 감소하다가 약 $10^(-3)M (pCa=3)$의 농도에서 등전점을 나타내고 전하역전이 일어났다. 해수중의 황토와 적조생물 입자는 비슷한 negative zeta potential을 나타내었고, 점토 중에서 해사가 가장 큰 negative zeta potential을 나타내었다. 해수중에서 황토입자와 적조생물입자의 EDL은 해수에 포함된 고농도의 염류 농도로 인하여 극히 얇게 압축되고, 이런 상태에서 두 입자가 상호 접근할 경우 모든 간격에서 LVDW attractive force의 절대값이 EDL repulsive force의 절대값보다 항상 큰 값을 나타낸다. 해수중에서 황토입자와 적조생물입자는 모든 간격에서 negative total interaction energy 값 (attractive force)을 나타내어 항상 용이하게 floe을 형성할 수밖에 없는 조건에 있다. 적조생물입자의 응집제거 효율은 황토의 농도가 증가함에 따라서 지수함수적 ($Y=36.04{\times}X^(0.11); R^2=0.9906$)으로 증가하였으며, 황토의 농도 800mg/l까지 급격한 증가를 보이다가 황토의 농도가 계속 증가함에 따라서 완만한 증가를 나타내었다. 적조생물은 황토 6,400mg/l에서 거의 $100{\%}$ 응집제거 되었다. 황토 800 mg/l을 사용하고 G-value를 $1, 6, 29, 139 sec^(-1)$로 단계적으로 증가시킴에 따라 응집제거 효율은 지수함수적으로 증가하였다. 이는 응집반응의 효율을 높이기 위해서는 황토입자와 적조생물입자 사이에 충분한 충돌이 일어날 수 있도록 교반하는 것이 매우 중요함을 나타내 주는 것이다. $800mg/l$의 농도에서 황토는 철을 함유하지 않은 다른 점토보다 $28.8{\~}60.3{\%}$ 더 높은 처리효율을 나타내었다. 황토에는 >SiOH의 음전하단과 수중의 phenolphthalein alkalinity를 소모하 The objective of this study was to examine the physicochemical characteristics of coagulation reaction between loess and red tide organisms (RTO) and its feasibility, in developing a technology for the removal of RTO bloom in coastal sea. The physicochemical characteristics of loess were examined for a particle size distribution, surface characteristics by scanning electron microscope, zeta potential, and alkalinity and pH variations in sea water. Two kinds of RTO that were used in this study, Cylindrothen closterium and Skeietonema costatum, were sampled in Masan bay and were cultured in laboratory. Coagulation experiments were conducted using various concentrations of loess, RTO, and a jar tester. The supernatant and RTO culture solution were analyzed for pH, alkalinity, RTO cell number. A negative zeta potential of loess increased with increasing pH at $10^(-3)M$ NaCl solution and had -71.3 mV at pH 9.36. Loess had a positive zeta potential of +1,8 mV at pH 1.98, which resulted in a characteristic of material having an amphoteric surface charge. In NaCl and $CaCl_2$, solutions, loess had a decreasing negative zeta potential with increasing $Na^+\;and\;Ca^(+2)$ ion concentration and then didn't result in a charge reversal due to not occurring specific adsorption for $Na^+$ ion while resulted in a charge reversal due to occurring specific adsorption for $Ca^(+2)$ ion. In sea water, loess and RTO showed the similar zeta potential values of -112,1 and -9.2 mV, respectively and sea sand powder showed the highest zeta potential value of -25.7 mV in the clays. EDLs (electrical double-layers) of loess and RTO were extremely compressed due to high concentration of salts included in sea water, As a result, there didn't almost exist EDL repulsive force between loess and RTO approaching each other and then LVDW (London-yan der Waals) attractive force was always larger than EDL repulsive force to easily form a floe. Removal rates of RTO exponentially increased with increasing a loess concentration. The removal rates steeply increased until $800 mg/l$ of loess, and reached $100{\%}$ at 6,400 mg/l of loess. Removal rates of RTO exponentially increased with increasing a G-value. This indicated that mixing (i.e., collision among particles) was very important for a coagulation reaction. Loess showed the highest RTO removal rates in the clays.

The effects of microalgal cell disruption via FeCl₃-based synergistic effect between Fenton-like and Lewis acid reaction for lipid extraction

Kim, D.Y.,Park, J.Y.,Choi, S.A.,Oh, Y.K.,Lee, I.G.,Seo, Y.W.,Han, J.I. Elsevier B.V 2014 Algal research Vol.6 No.1

In this study, crude oil was extracted from Nannochloropsis salina for biodiesel production using FeCl<SUB>3</SUB> as a catalyst. Scanning electron microscopy (SEM) analysis revealed that microalgae cells became wrinkled or burst after reaction. An optimal extraction condition, via the response surface methodology (RSM), was evaluated with respect to FeCl<SUB>3</SUB> concentration (1-3mM), reaction time (30-90min) and temperature (60-100<SUP>o</SUP>C). At a condition of FeCl<SUB>3</SUB> of 2mM, 90min, and 87<SUP>o</SUP>C, a maximum extraction yield of 213mg/g biomass and a FAME conversion rate of more than 80% were achieved. In light of FeCl<SUB>3</SUB> being a reference coagulant, even for microalgae harvesting, its use for lipid extraction is expected to conceivably reduce the overall cost of microalgae-derived biodiesel production.

전기응집/산화를 이용한 축산폐수 처리에 관한 연구

정호진 ( Ho Jin Chung ),성현석 ( Hyun Seok Sung ) 한국수처리학회 2008 한국수처리학회지 Vol.16 No.2

Roles of Oxidation and Coagulation in Fenton Process for the Removal of Organics in Landfill Leachate

Yoon, Jeyong,Kim, Yoonki,Huh, Jin,Lee, Yunho,Lee, Dongsoo 한국공업화학회 2002 Journal of Industrial and Engineering Chemistry Vol.8 No.5

High potential of coagulation to remove organics has not been fully recognized in Fenton process and coagulation has been used as an auxiliary process removing iron in effluent. This study evaluates the relative role of oxidation and coagulation step of Fenton process in the removing of biologically treated leachate organics of Metropolitan Landfill in Korea. This study showed that to the maximum, 30% of DOC and 40% of COD removal efficiencies were achieved by the Fenton oxidation step alone, whereas, 60% of DOC and 75% of COD removal efficiencies were achieved by the combined Fenton oxidation and subsequent Fenton coagulation step, as the same Fenton's reagent condition ([Fe^2+]_0 = 1250 or 2500 mg/L, and [H_20_2]_0 = 0~3000 mg/L) was applied in laboratory experiments. In addition, it was observed that the rapid decomposition of H_20_2 with time did not lead to the corresponding removal of leachate organics. This means that OH radical generated from the H_2O_2 decompostion is not effectively invoved in degrading the leachate organics, pointing out the possibility of uneconomical use of H_20_2 and unwarranted retention time of Fenton oxidatiom chamber in Fenton leachate treatment plant. Furthermore, the investigation of field Fenton process confirmed the observation of laboratory scale study, revealing that the DOC and COD removal effciencies in the Fenton oxidation step were less than 10~20% prior to the Fenton coagulation step, and major removals of DOC and COD (60~70%) were achieved after the finial Fenton coagulation step. These findings demonstrate the significance of the coagulation in Fenton process and raise a need for individual assessments of both oxidation and coagulation for the optimal design and evaluation of a whole Fenton processes. The individual assessments, however, should be conducted in an integrative manner because the preceding process (oxidation) may affect the performance the next process (coagulation).

전기응집산화를 이용한 하수처리장의 고도처리방안 연구

임진환 한국환경기술학회 2018 한국환경기술학회지 Vol.19 No.6

Due to the enforcement of effluent water regulation the advance sewage treatment system is needed to retrofit and remodelling. In this case the most important issue is the effluent concentrations of TP and there are a lot of system to reduce its concentration. But biological treatment processes have many restrictions to enhance the removal efficiency of TP. In this study the efficient ECO operating condition to improve and retrofit biological sewage wastewater treatment system is as follow; 1) The treatment efficiency of BOD, TN and TP at the current density of 15 ㎃/㎠ was higher than the treatment efficiency at 5 ㎃/㎠ in the electrodes arranged with Al-SUS(Stainless Steel) regardless of the reaction time, The TP concentration was 0.1 mg/L or less. Especially, when the reaction time was maintained at 10 min, the TP concentration was 0.06 mg/L or less irrespective of the current density. 2) The change of TP concentration is not influenced by the change of current density and rather the concentration of treated water changes according to the reaction time. In the case of electro coagulation reaction, a few seconds to several minutes are required. However, the reaction time of electro coagulation and oxidation was studied to be more than 10 minutes. 3) As a result, it has been studied that the economical current density of the electro coagulation oxidation process for TN and TP treatment of domestic wastewater is 15 ㎃/㎠ or less and the reaction time is 10 minutes. 현재 하수종말처리장은 질소와 인의 방류수 수질기준 강화로 생물학적 처리 후 약품주입으로 잔류 인의 처리를 하고 있는 실정에서 방류수 수질기준은 확보가 가능하나, 약품주입량의 과다와 발생되는 슬러지의 증대 및 발생슬러지의 탈수효율 저하로 슬러지처리과정에서 또 다른 문제가 발생하여 처리에 대한 신뢰성이 결여되어 있는 실정이다. 그러므로 본 연구는 기존 하수종말처리장에서 발생하고 있는 문제에 대하여 최소의 반응시간과 슬러지 발생량의 최소화를 토대로 생물학적 고도처리를 적용한 하수처리장에서 방류수 수질기준의 강화에 따라 생물학적 처리로 확보하기 어려운 안정적 처리방식과 처리수질변동에 대한 적응 및 질소와 인의 처리기준을 맞추기 위하여 기존 하수처리 방식에 Electro Coagulation and Oxidation system을 적용한 결과 다음과 같다. 1) Al-SUS(stainless steel)로 배치한 전극에서 반응시간대와 상관없이 15 mA/㎠의 전류밀도에서 BOD, TN 및 TP의 처리효율이 5 mA/㎠에서의 처리효율보다 높게 나타났으나, 전류밀도 10 mA/㎠ 이상만을 유지하여도 TP의 경우 대부분 0.1 mg/L 정도로 처리가 가능하며, 특히, 반응시간을 10 min으로 유지할 경우 TP농도는 전류밀도와 상관없이 0.06 mg/L 이하로 방류수 수질기준 0.1 mg/L 이하를 유지할 수 있었다. 2) TP농도의 변화는 전류밀도의 변화에 영향을 크게 받지 않으며, 오히려 반응시간에 따라 처리수의 농도가 변화하는 것으로 전기응집반응의 경우 수초~수분이 요구되나 전기산화와 동시에 반응이 일어나야 하므로 적절한 전기응집산화의 반응시간은 10 min 이상이 요구되는 것으로 연구되었다. 3) 결과적으로 본 연구에서 생활하수의 TN 및 TP처리를 위한 전기응집산화공정의 경제적인 전류밀도는 15 ㎃/㎠이하, 반응시간은 10 min을 유지하는 것이 적절한 것으로 연구되었다.

ECH 유도체와 수지성 폴리머를 함유한 Brine 폐수의 전처리를 위한 응집 및 침전 반응의 최적화 연구

조욱상 수원대학교 산업기술연구소 2005 산업기술연구소논문집 Vol.20 No.-

Epoxy resins are produced by the dehydro condensated reaction with ECH (Epichlorohydrin) and BPA(Bisphenoi-A) as raw reactants under sodium hydroxide(NaOH) as a catalyst, and from this reaction, salted water named of brine, which contains ECH derivatives in condition of emulsion as likely as glycidol and polymer resins, is produced as an undesired side product. This brire water is alkaline wastewater and causes process fouling problems by plugging and chemically depositing polymer particles on the surface of inner wall of reactors and pipes. and decreases the biodegradable efficiency in the wastewater process. In this study, the optimization of coagulation and sediment reactions, using inorganic and organic polymer coagulants, were performed to remove the causes occurring the process fouling phenomena. And also, based on this study, the methodologies applicable to the commercial processes including economical analysis were presented.

소성굴패각분말과 황토의 동시 사용에 의한 적조생물에 응집

김성재 ( Kim Seong Jae ) 한국수산과학회 2003 한국수산과학회지 Vol.36 No.6

N/A This study determined the optimum dosage for coagulation reactions of red tide organisms (RTO) using a combination of ignited oyster shell powder (IOSP) and loess and examined the electrokinetic and rheological characteristics of their flocs. Two kinds of RTO, Cylindrotheca clostevium and Skeletonema costatum, were sampled in Masan Bay and cultured in the laboratory. Coagulation experiments were conducted using various concentrations of IOSP, loess, IOSP+loess, RTO, and a jar tester. RTO cell numbers were counted for both the supernatant and RTO culture solution. The removal rates increased rapidly with increasing IOSP concentrations up to 50 mg/L and loess concentrations up to 800 mg/L. A removal rate of 100% was reached at 400 mg/L of IOSP and 6,400 mg/L of loess. The highest increment (16.7%) of the rates of coagulation reaction occurred using both IOSP and loess (50+200 mg/L) in comparison with IOSP alone. The rate of coagulation reaction using both IOSP and loess (50+200 mg/L), 90.6%, was similar to employing either IOSP of 150 mg/L or loess of 3,200 mg/L. All of the coagulation liquids for RTO, IOSP (200 mg/L), loess (200 mg/L), and IOSP+loess (200+200 mg/L) revealed non-Newtonian fluid properties and therefore their shear rate vs. shear stress curves were non-linear. The coagulation liquids revealed elastic body properties at a lower shear rate increasing in the following order: RTO, IOSP (200 mg/L), loess (200 mg/L), and IOSP+loess (200+200 mg/L. IOSP+loess (200+200 mg/L) especially demonstrated plastic flow properties at a lower shear rate.

전기응집사환 시스템을 이용한 유기성 폐수처리에 관한 연구

이태관 ( Tae Gwan Lee ),구봉헌 ( Bong Hun Ku ) 한국수처리학회 2010 한국수처리학회지 Vol.18 No.3

Pozzolanic reaction of the waste glass sludge incorporating precipitation additives

유일환,최지선,David A. Lange,지광습 사단법인 한국계산역학회 2016 Computers and Concrete, An International Journal Vol.17 No.2

The waste glass sludge is a waste produced in the glass industry. It is in a dust form and disposed with water. In the disposal process, various cohesive agents are incorporated in order to precipitate the glass particles efficiently. In this paper, we investigate the pozzolanic reaction of the waste glass sludge incorporating precipitation additives experimentally. The consumption of calcium hydroxide, the setting time and the compressive strength and the pore structure were tested for two different types of the waste glass sludge depending on whether precipitation additives were used. It was found that the waste glass sludge incorporating the precipitation additives had a higher pozzolanic potential than the reference waste glass sludge without precipitation additives.