• 대한화학회지
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• 제45권6호
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• pp.520-523
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• 2001

산성조건에서 $H_2O_2$가 HCr$O^-_4$ 이온과 반응하여 진한 청색의 $CrO(O_2)_2$를 형성하는 반응에 흐름 주입 분석을 도입하여 수용액시료 중 $H_2O_2$의 양을 정량할 수 있는 흡수분광분석법을 개발하였다. 이 분석법에 의한 $H_2O_2$의 정량범의는 2.00${\times}10^{-6}$M∼0.020M이며, 측정한계는 약 1.5${\times}10^{-6}$M이다. 또한, 이 분석법은 실제 강우와 강설 중에 존재하는 과산화수소의 농도결정에도 사용할 수 있음이 밝혀졌다.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.337-341
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• 2001

A new method to extract gold from pyrite roster cinder, which combines ultra-fine-grinding with resin-in-pulp, has been studied in this paper. Compared with traditional leaching technology, it can short leaching time, avoid complex filter process, lower sodium cyanide consumption and increase gold recovery by 35%. During leaching, aluminium oxide ball was used as stirred medium, hydrogen peroxide as leaching aid and sodium hexametaphosphate as grinding aid. With the high efficiency and chemistry effect of ultra-fine-grinding, the leaching process was developed and the gold leaching rate may reach 88%. With AM-2 Б resin as abosorber and sulfocarbamide (TU) as eluent, gold was recovered from cyanide pulp by resin-in-pulp. AM-2 Б resin has good adsorbability in cyanide solution(pH=10). It was easy to elude gold from the loaded resin with 0.1㏖/L cholhydric acid and 1㏖/L sulfocabamide. The effect of contact time, temperature and acidity etc. on the gold absorption had been examined with static methods. The results showed that the adsorption and desorption of gold could both reach over 98%. The effects of flow rate of solution on dynamic adsorption and elution of gold had been examined with dynamic methods. Breakthrough curve and elution curve had been drawn in this paper. A mild condition was determined through a number of experiments: leaching time 2 hours, liquid solid ratio 4:1, sodium cyanide 3kg/t, hydrogen peroxide 0.05%, sodium hexametaphosphate 0.05%; adsorption time 30 minutes, temperature 10-3$0^{\circ}C$, resin($m\ell$) solid(g) ratio 1:10, eluent resin ratio 10-20:1, velocity of eluent $1.5m\ell$/min. Under the mild condition, the gold recovery may reach 85%.

• 한국진공학회지
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• 제9권4호
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• pp.382-388
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• 2000

ECR-PECVD 방법을 이용하여 ECR power, $CH_4/H2$ 가스 혼합비와 유량, 증착시간, negative DC self bias 전압 등을 변화 시켜가면서 수소가 함유된 비정질 탄소 박막을 제조하고, 증착조건에 따른 박막의 결합구조 변화를 FTIR로 분석하였다. a-C:H 박막에 대한 FTIR 스팩트럼의 흡수 peak들은 2800~3000 $\textrm{cm}^{-1}$ 영역에서 관측되었으며, 대부분 $sp^3$ 결합을 하고있고 일부 $sp^2$ 결합구조가 존재함을 알 수 있었다. $CH_4/H_2$ 가스 혼합비와 유량의 미소 변화는 a-C:H 박막의 탄소와 수소의 결합구조에 큰 영향을 미치지 않았으며, 증착 시간이 증가할수록 탄소와 수소 원자들의 결합구조가 $CH_3$ 구조로부터 $CH_2$ 나 CH 구조로 변하고 있음을 확인하였다. 또한, bias 전압을 증가시킬수록 플라즈마에 의한 이온충돌 현상이 두드러져 탄소와 결합하고 있던 수소원자들이 떨어져 나가는 탈수소화 현상도 확인할 수 있었으며, 증착조건에 따른 a-C:H 박막의 결합구조 분석을 토대로 산업에 응용할 수 있는 높은 경도와 밀착성을 갖는 박막을 ECR-PECVD 방법으로 제조할 수 있음을 확인하였다.

• 한국물환경학회지
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• 제36권1호
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• pp.48-54
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• 2020

This paper presents a screening protocol for the selection of solvents available for the solvent extraction desalination process. The desalination solvents hypothetically and theoretically require the capability of (1) Forming hydrogen bonds with water, (2) Absorbing some water molecules into its non-polar solvent layer, (3) Changing solubility for water-solvent separation, and (4) Rejecting salt ions during absorption. Similar to carboxylic acids, amine solvents are solvent chemicals applicable for desalination. The key parameter for selecting the potential solvent was the octanol-water partitioning coefficient (Kow) of which preferable value for desalination was in the range of 1-3. Six of the 30 amine solvents can absorb water and have a variable, i.e., temperature swing solubility with water molecule for water-solvent separation. Also, the hydrogen bonding interaction between solvent and water must be stronger than the ion-dipole interaction between water and salt, which means that the salt ions must be broken from the water and only water molecules absorbed for the desalination. In the final step, three solvents were selected as desalination solvents to remove salt ions and recover water. The water recovery of these three solvents were 15.4 %, 2.8 %, 10.5 %, and salt rejection were 76 %, 98 %, 95 %, respectively. This study suggests a new screening protocol comprising the theoretical and experimental approaches for the selection of solvents for the desalination method which is a new and challenges the desalination process in the future.

• Korean Chemical Engineering Research
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• 제49권4호
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• pp.485-490
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• 2011

사불화탄소($CF_4$)는 반도체 제조공정에서 에칭과 반응기 세척에서 사용되어온 가스이다. $CF_4$는 적외선을 강하게 흡수하고 대기 중 잔류시간이 길어서 지구온난화에 영향을 미치기 때문에 고효율의 분해가 필요하다. 본 연구에서는 플라즈마와 워터젯을 결합하여 워터젯 글라이딩 아크 플라즈마 시스템을 개발하고, 이를 이용하여 $CF_4$를 고효율로 분해할 수 있도록 방전영역을 증가시키고 다량의 OH 라디칼을 생성시킬 수 있는 최적의 조업 조건을 결정하였다. 공정 실험 변수로는 워터젯 주입량, $CF_4$ 초기 농도, 전체 가스량과 주입에너지량(SEI : Specific energy input)을 선정하였다. 변수실험을 통하여 워터젯 주입량이 25.5 mL/min, $CF_4$ 초기 농도 2.2%, 전체 가스량 9.2 L/min, SEI 7.2 kJ/L일 때 $CF_4$ 분해율은 최고 97%까지 도달하였다.

• 한국수소및신에너지학회논문집
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• 제27권3호
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• pp.290-297
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• 2016

The absorbent loss due to degradation in $CO_2$ capture process using aqueous alkanol amine solution has adverse effect on the economics of overall process. The degradation causes absorbent loss, equipment corrosion, foaming, adhesive material producing and viscosity increase in operation. In this study, the degradation characteristics of $CO_2$ capture process using MEA (monoehtanolamine) under various conditions such as $O_2$ partial pressure, $CO_2$ loading and absorbent temperature. The effects of iron, which generated from the equipment corrosion, on absorbent degradation were studied using $Fe_2SO_4$ containing MEA solution. The produced gases were analyzed by FT-IR(Fourier Transform Infrared Spectrophotometer) and the specifically measured $NH_3$ concentration was used as a degradation degree of aqueous MEA solution. The experiments showed that the higher $CO_2$ loadings (${\alpha}$), $O_2$ fraction ($y_{O2}$) and reaction temperature enhanced the more degradation of aqueous MEA solution. Comparing other operation parameters, the reaction temperature most affected on the degradation. Therefore, it could be concluded that the above parameters affects on degradation should be considered for the selections of $CO_2$ absorbent and operating conditions.

• 한국수소및신에너지학회논문집
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• 제27권1호
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• pp.83-94
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• 2016

Performance of absorbent for post-combustion $CO_2$ capture was measured and discussed. Fully saturated fresh absorbent (P2-15F) and absorbents sampled from absorption and regeneration reactor of continuous $CO_2$ capture process, P2-15A, P2-15R, respectively, were used as representative absorbents. Small scale fluidized bed reactor (0.05 m I.D., 0.8 m high) which can measure exhaust gas concentration and weight change simultaneously was used to analyze regeneration characteristics for those absorbents. Exhausted moles of $CO_2$ and $H_2O$ were measured with increasing temperature. $H_2O/CO$ ratio and working capacity were determined and discussed to confirm reason of reactivity decay after continuous operation. Moreover, possibility of side reaction was checked based on the $H_2O/CO_2$ mole ratio. Finally, suitable regeneration temperature range was confirmed based on the trend of working capacity with temperature.

• 한국수소및신에너지학회논문집
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• 제27권3호
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• pp.318-327
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• 2016

In order to improve the performance of temperature field measurements by CT-TDLAS (Computer Tomography Tunable Diode Laser Absorption Spectroscopy), a new reconstruction algorithm, named two-ratios-of-three-peaks method is proposed in this paper. Further, two methods for selecting appropriate initial values of the iterative calculation of CT-TDLAS are proposed. One is MLOS (multiplicative line of sight) method and the other one is ALOS (additive line of sight) method. Two-ratios-of-three-peaks (2R3P) algorithm combined with MART (multiplicative algebraic reconstruction technique) is finally developed for the enhancements of reconstructive calculations. The results have been compared with those obtained by the conventional one-ratio-of-two-peaks (1R2P) algorithm. In order to evaluate the performance of this algorithm, numerical test has been performed using phantom Gaussian temperature distributions with $11{\times}11$ square mesh. The performance of the constructed algorithm has been demonstrated by comparing the results obtained in actual burner experiments with those obtained by thermocouples. It has been verified that 2R3P algorithm with MART and MLOS showed best performance than that of 1R2P algorithm.

• 한국수소및신에너지학회논문집
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• 제21권5호
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• pp.375-382
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• 2010

A layered perovskite photocatalysts, $SrBi_2Nb_2O_9$ (SBN), was synthesized by the conventional solid-state reaction method and characterized by X-ray diffraction (XRD) and UV-visble spectrophotometry. The results showed that the structure of $SrBi_2Nb_2O_9$ is orthorhombic. Diffuse reflectance spectra for calcined and attrition-milled SBN showed the main absorption edges were less 400 nm, that is ultraviolet region. SBN under micron-sized powder was deposited on the $Al_2O_3$ by room temperature powder spray in vacuum process, so called aerosol deposition (AD), and nano-grained $SrBi_2Nb_2O_9$ photocatalytic thick film was fabricated. AD-deposited SBN thick films were characterized by XRD, scanning electron microscopy (SEM) and UV-visable spectrophotometry, Moreover, it was found that several nano-sized SBN film by AD process can improve the photocatalytic activity under visable reflectance.

• 공업화학
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• 제29권6호
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• pp.765-771
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• 2018

본 연구에서는 각종 환경기초시설에서 발생하는 악취 유발물질 중 $H_2S$를 처리하기 위한 하수슬러지 기반 흡착제의 흡착성능 증진을 위해 제조조건 중 탄화조건 최적화에 대한 연구를 수행하였다. 적용되는 흡착제는 하수처리장에서 발생하는 슬러지를 온도 및 승온속도와 같은 탄화조건을 달리하여 제조하였으며, 흡착제의 물리적 특성과 흡착성능과의 상관관계를 확인하였다. 실험결과 $10^{\circ}C/min$의 승온속도로 $900^{\circ}C$의 온도에서 탄화과정을 거친 슬러지의 흡착성능이 가장 우수하였으며, SEM, BET 분석을 통해 비표면적 및 기공특성(기공크기, 부피)이 흡착성능의 주요 인자임을 확인하였다. 최적 탄화조건 흡착제의 흡착성능을 증진시키기 위해 K 이온을 담지하였으나, 하수슬러지 기반 흡착제의 경우 큰 영향이 없는 것으로 확인하였다.