• 자원리싸이클링
• /
• 제15권3호
• /
• pp.58-65
• /
• 2006

폐펄프를 흡착제로 $Ni^{2+}$가 함유된 폐수의 흡착 처리시 흡착제로 활용하는 방안을 검토하고자, 흡착질의 초기 농도, 온도, 흡착제인 폐펄프의 양, pH 등을 변화시키고, 공존물질의 농도 및 전처리의 영향 등의 요인을 고려하여 실험하였다. pH 에 따른 폐펄프의 Electrokinetic Potential pH 7.8 보다 낮은 영역에서는 양의 전하를 나타내고, 그 이상의 pH에서는 음의 전하를 나타내었다. 본 연구에서 폐펄프에 대한 $Ni^{2+}$의 흡착은 4시간 이내에 평형에 도달하였고, 흡착질인 $Ni^{2+}$의 초기 농도가 증가할수록 흡착량 역시 증가함을 보였다. 온도가 증가함에 따라 흡착량이 감소하여 흡착반응은 발열반응의 양상을 보였으며 이를 열역학적으로 고찰하였다. 또한 흡착제인 폐펄프의 양이 증가함에 따라 흡착량이 증가하였으며, pH $3{\sim}6$ 영역에서 pH 가 증가함에 따라 흡착량이 증가함을 보였는데 이는 폐펄프의 표면전위의 pH에 따른 변화양상과도 일치하는 결과였다. 공존물질인 $KNO_3$의 농도가 증가함에 따라 $Ni^{2+}$ 흡착량이 감소함을 보였고, NaOH 로 페펄프를 전처리한 후 흡착실험을 한 결과 전반적으로 NaOH 의 농도가 상승함에 따라 흡착률이 증가하는 것으로 관찰되었으나 그 값이 어느 한도 이상일 경우 오히려 흡착률이 감소하는 것으로 파악되었다.

• 한국재료학회:학술대회논문집
• /
• 한국재료학회 2001년도 춘계학술발표강연 및 논문개요집
• /
• pp.24-24
• /
• 2001

• 한국원자력학회:학술대회논문집
• /
• 한국원자력학회 1999년도 춘계학술발표회요약집
• /
• pp.100-100
• /
• 1999

• 공업화학
• /
• 제7권4호
• /
• pp.614-622
• /
• 1996

엣칭용 염화제2철 용액중의 효과적인 니켈제거에 관해 연구하였다. 전해철괴 또는 폐새도우마스크 철편을 사용하여 염화제2철을 염화제1철로 환원시킨후 용액중의 $Ni^{2+}$를 전해철 분말로 환원 석출시켰다. 최적의 실험조건하에서 초기 니켈의 농도가 1.0%일 때 니켈제거율은 99%이었고 초기 니켈의 농도가 0.1%일 때 니켈제거율은 98%이었다. 염화제2철의 환원반응 중에 생성된 수산화철의 종류 및 입자크기를 XRD와 SEM으로 분석하였다.

• 한국재료학회지
• /
• 제33권10호
• /
• pp.385-392
• /
• 2023

A solution combustion process for the synthesis of hollandite (BaAl₂Ti₆O₁₆) powders is described. SYNROC (synthetic rock) consists of four main titanate phases: perovskite, zirconolite, hollandite and rutile. Hollandite is one of the crystalline host matrices used for the disposal of high-level radioactive wastes because it immobilizes Sr and Lns elements by forming solid solutions. The solution combustion synthesis, which is a self-sustaining oxi-reduction reaction between a nitrate and organic fuel, generates an exothermic reaction and that heat converts the precursors into their corresponding oxide products in air. The process has high energy efficiency, fast heating rates, short reaction times, and high compositional homogeneity. To confirm the combustion synthesis reaction, FT-IR analysis was conducted using glycine with a carboxyl group and an amine as fuel to observe its bonding with metal element in the nitrate. TG-DTA, X-ray diffraction analysis, SEM and EDS were performed to confirm the formed phases and morphology. Powders with an uncontrolled shape were obtained through a general oxide-route process, confirming hollandite powders with micro-sized soft agglomerates consisting of nano-sized primary particles can be prepared using these methods.

• 한국방사성폐기물학회:학술대회논문집
• /
• 한국방사성폐기물학회 2004년도 Proceedings of the 4th Korea-China Joint Workshop on Nuclear Waste Management
• /
• pp.245-256
• /
• 2004

The extraction of three kinds of amido podands, N,N,N'N'-tetrabutyl-3-oxa-pentanedi- amide (TBDGA), N,N,N'N'-tetra-isobutyl-3-oxa-pentanediamide(TiBDGA) and N,N,N'N'-tetra- butyl-3,6-dioxa-oct-anediam- ide(TBDOODA) on U(VI),Pu(IV), Am(III), Eu(III) and other metal ions is studied in nitric acid solutions. 40%octanol-kerosene is chosen as diluents to eliminate third phase and emulsion. TBDGA and TiBDGA show extraction selectivity to An(III) and Ln(III) much higher than to U(VI) and Pu(IV). Fe, Ru and Mo is poorly extracted by the three kinds of amid podands in 2~3mol/L $HNO_3$ solutions. Aiming to eliminate interface crude when using simulated HLLW solution in the system of 0.2mol/L TBDGA/Octanol＋kerosene, acetohydroxyamic acid was adapted. Distribution ratio of zirconium was decreased when adding acetohydroxyamic acid in aqueous solution, and interface crude disappeared as mixing extractant with HLLW. The counter-current extraction test is carried out in a set of miniature mixer-settler, with 0.2mol/L TBDGA/ 40% octanol-kerosene as extractant to separate U(VI), Pu(IV), Am(III) and Eu(III) from simulated high level liquid waste(HLLW) solution. In battery A, lanthanides and actinides are coextracted into organic phase with the recovery of 99.98% for U(Ⅵ), >99.99% for Pu(IV), and >99.99% for Am(III) and Eu(III) respectively. In battery R1, 99.99% U, 86.2% Pu and a part of Am or Eu are stripped into aqueous phase by 0.2mol/L acetohydroxyamic acid (AHA) in 0.01mol/L $HNO_3$ solution. In battery $R_2$, Am, Eu and remained Pu are completely back-extracted by 0.2mol/L AHA. This separation process contains no salt reagent, and it is not necessary to dilute HLLW feed.

• 대한전자공학회:학술대회논문집
• /
• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
• /
• pp.259-263
• /
• 2001

There are several steps such as slicing, lapping, chemical etching and mechanical polishing in the silicon wafer production process. The chemical etching step is necessary to remove damaged layer caused In the slicing and lapping steps. The typical etching liquor is the acid mixture comprising nitric acid, acetic acid and hydrofluoric acid. At present, the waste acid is treated by a neutralization method with a high alkali cost and balky solid residue. A solvent extraction method is applicable to separate and recover each acid. Acetic acid is first separated from the waste liquor using 2-ethlyhexyl alcohols as an extractant. Then, nitric acid is recovered using TBP(Tri-butyl phosphate) as an extractant. Finally hydrofluoric acid is separated with the TBP solvent extraction. The expected recovered acids in this process are 2㏖/l acetic acid, 6㏖/1 nitric acid and 6㏖/l hydrofluoric acid. The yields of this process are almost 100% for acetic acid and nitric acid. On the other hand, it is important to recover and reuse the metal values contained in various industrial wastes in a viewpoint of environmental preservation. Most of industrial products are made through the processes to separate impurities in raw materials, solid and liquid wastes being necessarily discharged as industrial wastes. Chemical methods such as solvent extraction, ion exchange and membrane, and physical methods such as heavy media separation, magnetic separation and electrostatic separation are considered as the methods for separation and recovery of the metal values from the wastes. Some examples of the application of solvent extraction to the treatment of wastes such as Ni-Co alloy scrap, Sm-Co alloy scrap, fly ash and flue dust, and liquid wastes such as plating solution, the rinse solution, etching solution and pickling solution are introduced.

• Nuclear Engineering and Technology
• /
• 제46권6호
• /
• pp.847-856
• /
• 2014

Spent resin waste containing a high concentration of $^{14}C$ radionuclide cannot be disposed of directly. A fundamental study on selective $^{14}C$ stripping, especially from the IRN-150 mixed bed resin, was carried out. In single ion-exchange equilibrium isotherm experiments, the ion adsorption capacity of the fresh resin for non-radioactive $HCO_3{^-}$ ion, as the chemical form of $^{14}C$, was evaluated as 11mg-C/g-resin. Adsorption affinity of anions to the resin was derived in order of $NO_3{^-}$ > $HCO_3{^-}{\geq}H_2PO_4{^-}$. Thus the competitive adsorption affinity of $NO_3{^-}$ ion in binary systems appeared far higher than that of $HCO_3{^-}$ or $H_2PO_4{^-}$, and the selective desorption of $HCO_3{^-}$ from the resin was very effective. On one hand, the affinity of $Co^{2+}$ and $Cs^+$ for the resin remained relatively higher than that of other cations in the same stripping solution. Desorption of $Cs^+$ was minimized when the summation of the metal ions in the spent resin and the other cations in solution was near saturation and the pH value was maintained above 4.5. Among the various solutions tested, from the view-point of the simple second waste process, $NH_4H_2PO_4$ solution was preferable for the stripping of $^{14}C$ from the spent resin.

• 한국산업정보학회:학술대회논문집
• /
• 한국산업정보학회 2001년도 춘계학술대회논문집:21세기 신지식정보의 창출
• /
• pp.237-246
• /
• 2001

본 논문에서는 DQDB 시스템에서 불공정한 문제를 개선하고 대역의 낭비를 제거하기 위한 해결방안을 제안한다. 이 방법은 기존 프로토콜의 약간의 수정만으로, 불공정성 문제를 해결할 때 발생하는 대역의 낭비론 없앨 수 있다. DQDB 시스템에서는 각 노드가 메세지를 보낼 때의 공정성에 여러 문제가 있으며 이를 해결하기 위하여 대역폭 균형 기법과 비례할당 기법이 소개된 바 있다. 그러나 이 기법들에서는 공정성 문제는 크게 개선되었으나 대역의 낭비라는 문제가 새로 발생한다. 따라서 본 논문에서는 공정성 문제를 개선하면서 대역의 낭비문제를 제거할 수 있는 새로운 기법을 제안한다. 제안하는 기법에 대하여 수학적으로 해석하고 이의 검증을 위하여 모의실험을 수행하였다. 그 결과에서는 다른 기법들에 비해 공정한 정도가 더욱 뚜렷하며 과부하시에도 대역의 낭비가 거의 없는 것을 확인 할 수 있다.

• 한국환경보건학회지
• /
• 제31권4호
• /
• pp.332-339
• /
• 2005

The environmental regulations in the world has been reinforced and many nations has devoted themselves to the development of cost-effective technology. Selective catalyst reduction(SCR) and selective non-catalyst reduction (SNCR) processes are mainly used to treat nitrogen oxidants generated from fossil-fuel combustion. One of these typical technologies for reduction of do-NOx is SNCR process has increased continuously because of the low cost for building and maintenance. Nevertheless the researches on the application to real scale plant by the reductant like Urea are rarely studied. In this paper, an experimental investigations were performed on the SNCR process in the industrial waste incineration plant. With no reducing agent, the concentration of NOx stayed in around 180 ppm $(O_2\;12\%)$ with the exhausting temperature of $950^{\circ}C$ and changed within the range of 20 ppm to remain relatively consistent. When $10\;wt\%)$ of a solution was added, the efficiency of denitrification reached above $61.4\%$ with the NSR of 2.0 and the exhausting temperature of $950^{\circ}C.$ When the concentration of the urea solution was set to $10\;wt\%$ and the sprinkling to four nozzles, the reaction temperature was reduced to about $50~100^{\circ}C$ with a mixture of $10\;wt\%\;CH_3OH\;and\;5wt\%\;Na_2CO_3$ in $40\;wt\%$ of the solution. The NOx removal efficiency increased to $78.4\%,$ achieving a broader and expansive range of reaction temperatures than the addition of an unmixed pure solution.