• 상하수도학회지
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• 제25권3호
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• pp.367-373
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• 2011

Mechanism of rapid mixing effect on chemical phosphorus removal is evaluated in this study. Assuming that chemical phosphorus removal is unaffected by mixing time, only rapid mixing intensity is evaluated. In order to find out the mechanism, it is hypothesized that rapid mixing affects the Al hydrolysis speciation, and that formation of more monomeric species ($Al^a$) results in better removal of phosphorus. According to a ferron assay, more $Al^a$ formed at higher mixing intensity than at lower intensity. Subsequent experiments revealed that better phosphorus removal was obtained at higher intensity than at lower intensity, in terms of the molar ratio of $Al_{added}/P_{removed}$. The proposed hypothesis was proved in this study. Chemical phosphorus removal is affected by rapid mixing intensity due to its effect on the Al hydrolysis speciation.

• 한국재료학회지
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• 제25권3호
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• pp.132-137
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• 2015

The effects of the mixing of an active material and a conductive additive on the electrochemical performance of an electric double layer capacitor (EDLC) electrode were investigated. Coin-type EDLC cells with an organic electrolyte were fabricated using the electrode samples with different ball-milling times for the mixing of an active material and a conductive additive. The ball-milling time had a strong influence on the electrochemical performance of the EDLC electrode. The homogeneous mixing of the active material and the conductive additive by ball-milling was very important to obtain an efficient EDLC electrode. However, an EDLC electrode with an excessive ball-milling time displayed low electrical conductivity due to the characteristic change of a conductive additive, leading to poor electrochemical performance. The mixing of an active material and a conductive additive played a crucial role in determining the electrochemical performance of EDLC electrode. The optimal ball-milling time contributed to a homogeneous mixing of an active material and a conductive additive, leading to good electrochemical performance of the EDLC electrode.

• Korean Chemical Engineering Research
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• 제44권2호
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• pp.207-215
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• 2006

본 연구의 목적은 응집공정에서 생성되는 플럭의 성상을 가시화하여 PACC의 응집 특성을 고찰하였다. 인공 원수내탁질 입자의 제타전위는 pH 8~9에서 영으로 수렴하였고 이 영역에서 TDS와 전기전도도가 최소값을 나타내 주었다. 급속 및 완속 교반의 최적 혼화강도가 관측되었으며, 특히 탁도의 제거에 있어서는 급속교반의 속도경사가 가장 낮은 $95.1sec^{-1}$에서 최대의 제거율을 나타내었다. 급속교반 후에는 $3{\sim}5{\mu}m$의 작은 입자가 급격히 생성되었으며 교반강도가 클수록 더 많은 수의 입자가 생성되었다. 완속교반이 진행될수록 $3{\sim}5{\mu}m$의 작은 입자의 수는 급격히 감소하였고 $7{\sim}21{\mu}m$의 중간 크기의 입자는 증가하는 경향을 나타내주었다. $23{\mu}m$ 보다 큰 입자의 경우는 급속교반의 속도경사가 $95.1sec^{-1}$에서 가장 많은 수가 생성되었고, $3{\sim}5{\mu}m$의 작은 입자의 경우에는 급속교반의 속도경사가 $760.7sec^{-1}$에서 가장 많이 생성되었다.

• Bulletin of the Korean Chemical Society
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• 제28권2호
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• pp.181-182
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• 2007

• Korean Chemical Engineering Research
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• 제50권3호
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• pp.588-593
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• 2012

불포화 폴리에스터(unsaturated polyester, UP)와 저수축제(low profile agent, LPA), 폴리스틸렌(polystyrene, PS)과의 compatibility가 불포화 폴리에스터와 저수축제의 비율, 혼합시간, 혼합온도 그리고 추가로 투입되는 불포화 폴리에스터 수지량과 같은 다양한 조건하에서 확인되었다. 1단계로 1700 rpm의 교반속도에서 제조된 수지 혼합액의 경우, 불포화 폴리에스터 수지(unsaturated polyester resin, UPR) 투입량 25 g, 약 $30^{\circ}C$의 반응온도에서 상대적으로 작은 입자 크기 및 상분리율을 나타내었다. 2단계 수지 혼합액의 경우, 2차로 투입된 45 g의 불포화 폴리에스터 수지 혼합액에서 향상된 compatibility를 보였다. 이러한 결과는 혼합조건이 불포화 폴리에스터 수지와 저수축제 혼합액의 compatibility에 중요한 역할을 한다는 것을 의미한다. 또한, 상기조건을 통해 제조된 sheet molding compound (SMC)를 사용해서 만든 샘플은 흡수율, 수축율 및 광택도에서 향상된 결과를 나타내었다.

• 한국물환경학회지
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• 제23권1호
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• pp.111-121
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• 2007

The experimental design and response surface methodologies haven been applied to the investigation of the chemical coagulation of livestock wastewater. The chemical coagulation reactions were mathematically described as a function of parameters raping mixing (rpm) of chemical coagulation ($X_1$), slow mixing (rpm) of chemical coagulation ($X_2$), $FeCl_3 $ concentration (mg/L) ($X_3$) and pH ($X_4$) being modeled by use of the central composite design. Empirical models were developed to describe relationship between the experimental variables and response. Statistical analysis indicates that three factors ($X_1$: raping mixing (rpm), $X_2$: slow mixing (rpm), $X_3$: $FeCl_3 $ concentration (mg/L) on the linear term (main effect), slow mixing (rpm) (${X_2}^2$) on the non-linear term (quadratic), and two factors ($X_1-X_3$, $X_2-X_3$) on the non-linear term (cross-product) had significant effects, respectively. The estimated ridge of maximum responses and optimal conditions for CODcr using canonical analysis was 87.44% ($X_1$: 229 rpm, $X_2$: 51 rpm, $X_3$: 877 mg/L, $X_4$: 4.3). To confirm this optimum condition, three additional experiments were performed and the mean CODcr removal (%) and concentration (mg/L) with a standard deviation of $87{\pm}1.2%$ ($576{\pm}34ppm$) were obtained.

• Elastomers and Composites
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• 제51권2호
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• pp.81-92
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• 2016

1,3-Diphenylguanidine (DPG) is commonly used as a secondary accelerator which not only acts as booster of cure but also activating silanization reaction. The aim of this study is to increase the interaction between silica and rubber by using DPG. In this study, mixing was proceeded in two steps. The T-1 compound is mixed DPG with silica and silane coupling agent in the kneader at high temperature which is named as $1^{st}$ mixing step. T-3 compound is mixed DPG with curatives in the two-roll mill at low temperature which is named as $2^{nd}$ mixing step. The T-2 compound is mixed a half of DPG in $1^{st}$ mixing step and the remainder is mixed in $2^{nd}$ mixing step. Total DPG content was equal for all compounds. When DPG is mixed with silica, silane coupling agent during the $1^{st}$ mixing step, a decrease in cure rate and an increase in scorch time can be seen. This indicates that DPG is adsorbed on the surface of silica. during rubber processing. However, bound rubber content is increased and dynamic properties are improved. These results are due to the highly accelerated silanization reaction. However, there are no significant difference in 100%, 300% modulus.

• 대한환경공학회지
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• 제27권1호
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• pp.52-58
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• 2005

국내 정수장의 약품공정을 향상시켜 저비용 고효율의 정수처리 공정을 확립할 목적으로 약품 분사용 초음파 분사 노즐의 적용가능성을 평가하였다. 초음파 분사노즐은 압전세라믹스를 이용하여 제작하였으며, 이 장치를 사용하여 상수 원수를 처리한 결과와 현재 대부분의 정수장에서 사용되고 있는 기존의 약품 혼화방식에 의한 오염물질의 처리효율을 비교 평가하였다. 그 결과 혼화방식에 따른 혼화지 내 응집제 혼화특성은 초음파 노즐에 의한 혼화방식이 기계식(back-mixing) 혼화방식보다 응집제의 확산속도가 빠른 것으로 조사되었다. 오염물질 별 제거효율 역시 기계식(back-mixing) 혼화방식보다 초음파 노즐에 의한 혼화방식의 제거효율이 높은 것으로 조사되어, 초음파 분사노즐을 이용한 약품 혼화방식을 실제 정수처리 공정에 적용할 경우 응집제의 과량 주입에 의한 처리효율의 저하를 방지할 수 있고, 후속 공정에 대한 부하량을 줄임으로서, 정수공정에 사용되는 약품을 절감시키고, 혼화지가 필요없게 되어 이로 인한 경제적 효과 뿐만 아니라 보다 순도가 높은 음용수를 생산 할 수 있을 것으로 기대된다.

• 대한화학회지
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• 제6권2호
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• pp.130-132
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• 1962

A new method of evaluating the mixing time in the continuous flow stirred tank is herein proposed. Experimental results to test the concept are also presented.The mixing time is defined as the time interval between the injection of a slug of an electrolyte solution into the tank and the moment at which an essentially straight line begins on a plot of the conductivity of effluent versus time.The proposed method of measuring the mixing time is valid even for the low mixing time (5 seconds) and the results obtained agree well with previous work, where the mixing time measurements were carried out by the injection of a dye into the feed stream.

• 한국응용과학기술학회지
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• 제24권3호
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• pp.219-232
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• 2007

In T-mixer crystallization, supersaturation is generated by mixing of another solvent or non-solvent in order to reduce the solubility of the compound. Also, T-mixer is a type of continuous crystallization. In order to induce micro-mixing, two solutions were mixed rapidly by T-mixer, which formed high supersaturation. As the results, mean size of HMX crystals decreased with increasing de-supersaturation rate $(R_s)$. Eventually, HMX particles ranging from 0.5 to $5{\mu}m$ can be obtained by T-mixer crystallization. Mixing efficiency in T-mixer increased with increasing $R_s$ values. In T-mixer crystallization without surfactants, homogeneous nucleation was formed when S and $R_s$ was over 54 and $1.6{\times}10^3/sec$. In T-mixer crystallization with surfactants, homogeneous nucleation was formed when S and $R_s$ was over 26 and 7.4/sec.