• Title/Summary/Keyword: 나트륨 이온 제거

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Ion-Pair Extraction of Cs Radionuclides by Dicyclohexyl-24-crown-8 and Tetraphenylborate for Their Determination in Reactor Coolant (Dicyclohexyl-24-crown-8과 Tetraphenylborate에 의한 원자로 냉각수로부터 세슘 핵종의 이온쌍 용매추출)

  • Ihn-Chong Lee;Si-Joong Kim;Chul Lee
    • Journal of the Korean Chemical Society
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    • v.27 no.4
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    • pp.262-267
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    • 1983
  • A study has been carried out for a scheme of the selective extraction and determination of cesium, sodium and nuclides by the ion association with dicyclohexyl-24-crown-8 and sodium tetraphenylborate from primary coolant of a pressurized water reactor. For that purpose, the effects of hydrogen, cesium and borate ions on the extraction have been investigated. Interferences of iodine and xenon nuclides were found but could be removed by reducing with sodium thiosulfate and back extraction with 1 N hydrochloric acid solution, respectively.

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Removal of Ca2+ and Fe3+ in Acid Mine Drainage by Tripolyphosphates (트리폴리인산염을 이용한 산성광산배수 내 칼슘 및 철이온 제거)

  • Hyun, Jaehyuk;Jeon, Hyungjoong;Kim, Jihoon
    • Journal of the Korean GEO-environmental Society
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    • v.10 no.5
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    • pp.27-32
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    • 2009
  • This study evaluates tripolyphosphate's ability to treat AMD (Acid Mine Drainage). Based on the batch test results for reaction between tripolyphosphate and AMD obtained from Munkyung coal mine, $4.7{\times}10^{-3}$ mole is the optimum dosage of tripolyphosphate for AMD treatment. $Ca^{2+}$ concentration is decreased from $16.4mg/{\ell}$ to $5.6mg/{\ell}$, in other words, the removal rate of $Ca^{2+}$ is 65.9%. $Fe^{3+}$ concentration is decreased from $3.7mg/{\ell}$ to $0.02mg/{\ell}$, that is, the removal rate of $Fe^{3+}$ is 99.5%. $SO{_4}^{2-}$ concentration ranges from $526.8mg/{\ell}$ to $566.5mg/{\ell}$, which shows no obvious decrease. After dosing up tripolyphosphate, $Na^+$ concentration in AMD ranges from $549.8mg/{\ell}$ to $599.3mg/{\ell}$ and orthophosphate concentration in AMD ranges from $6.82mg/{\ell}$ to $7.60mg/{\ell}$. It was found that the precipitate in the order of amount is Apatite${\gg}{\beta}$-tricalcium phosphate > $Fe(OH)_3$ from SEM, XRF, XRD analyses. Consequently, the treatment by tripolyphosphate is effective in pH buffering and in the removal of $Ca^{2+}$ and $Fe^{3+}$.

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Antimicrobial Activity and Stability of Tetrasodium Pyrophosphate Peroxidate (과산화피로인산나트륨의 항균성 및 안정성)

  • Lee, Jong-Hoon;Kim, Il-Hwan
    • Korean Journal of Food Science and Technology
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    • v.30 no.5
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    • pp.1040-1044
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    • 1998
  • Tetrasodium pyrophosphate peroxidate can be crystallized as a hydrogen-peroxide-bound salt from the solution of tetrasodium pyrophosphate and hydrogen peroxide. The antimicrobial activity and stability of the compound were tested for the use as a food preservative. It showed antimicrobial activities against several food spoilage microorganisms at the concentration of 0.1% (w/v), and was stable for 80 days in room temperature as a form of 70% hydrogen-peroxide-bound tetrasodium pyrophosphate peroxidate. It was also stable at the boiling temperature but decomposed significantly in the presence of metal ions. The compound can be an effective food preservative at the 0.2% (w/v) concentration, which contains 0.03% (v/v) hydrogen peroxide. The compound could be commercialized if the application area and usage direction as well as the removal method of hydrogen peroxide were developed.

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Production of Hard Water From Seawater Using Electrodialysis (해수로부터 전기투석 장치를 이용한 고경도 수 제조)

  • Ji, Ho;Kim, Kwang Soo;Moon, Deok Soo;Kim, Hyeon Ju;Lee, Ho Saeng
    • Journal of the Korean Society for Marine Environment & Energy
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    • v.18 no.1
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    • pp.9-14
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    • 2015
  • There are various ions in seawater. In order to use seawater as the drinking water, some elements are to be concentrated and other elements are to be removed. To obtain these characteristics using seawater, it is necessary to adjust seawater quality. Because calcium and magnesium are especially healthful to human bodies, it is required to concentrate these elements. In this study, the technology to obtain the hard water from seawater by electerodialysis was investigated. After concentrated water was produced using nanofiltration membranes, sodium chloride was eliminated from the concentrated water by electrodialysis. The hard water production from seawater was successfully achieved using electrodialysis in this study.

High-purity Lithium Carbonate Manufacturing Technology from the Secondary Battery Recycling Waste using D2EHPA + TBP Solvent (이차전지 폐액으로부터 D2EHPA + TBP solvent를 활용한 탄산리튬 제조기술)

  • Dipak Sen;Hee-Yul Yang;Se-Chul Hong
    • Resources Recycling
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    • v.32 no.1
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    • pp.21-32
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    • 2023
  • Because the application of lithium has gradually increased for the production of lithium ion batteries (LIBs), more research studies about recycling using solvent extraction (SX) should focus on Li+ recovery from the waste solution obtained after the removal of the valuable metals nickel, cobalt and manganese (NCM). The raffinate obtained after the removal of NCM metal contains lithium ions and other impurities such as Na ions. In this study, we optimized a selective SX system using di-(2-ethylhexyl) phosphoric acid (D2EHPA) as the extractant and tri-n-butyl phosphate (TBP) as a modifier in kerosene for the recovery of lithium from a waste solution containing lithium and a high concentration of sodium (Li+ = 0.5 ~ 1 wt%, Na+ = 3 ~6.5 wt%). The extraction of lithium was tested in different solvent compositions and the most effective extraction occurred in the solution composed of 20% D2EHPA + 20% TBP + and 60% kerosene. In this SX system with added NaOH for saponification, more than 95% lithium was selectively extracted in four extraction steps using an organic to aqueous ratio of 5:1 and an equilibrium pH of 4 ~ 4.5. Additionally, most of the Na+ (92% by weight) remained in the raffinate. The extracted lithium is stripped using 8 wt% HCl to yield pure lithium chloride with negligible Na content. The lithium chloride is subsequently treated with high purity ammonium bicarbonate to afford lithium carbonate powder. Finally the lithium carbonate is washed with an adequate amount of water to remove trace amounts of sodium resulting in highly pure lithium carbonate powder (purity > 99.2%).

A Study on the Sol-Gel Reaction Kinetics of Sodium Silicate Solution (규산(硅酸)나트륨 수용액(水溶液)의 솔-젤 반응속도론적(反應速度論的) 고찰(考察))

  • Kim, Chul-Joo;Yoon, Ho-Sung;Jang, Hee-Dong
    • Resources Recycling
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    • v.17 no.6
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    • pp.34-42
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    • 2008
  • The properties of sodium silicate solution were surveyed by using the yellow silicomolybdic method, and the formation of silica sol from sodium silicate solution and the growth of silica sol were investigated in this study. The $SiO_2$ content of 2 wt% in sodium silicate solution was proper to oxidize sodium silicate with sulfuric acid. After the removal of sodium ions in sodium silicate solution, the pH of silicate solution had to be controlled above 9 for the stabilization of silicate solution. The condensation between silicic acid species and silica nuclei surfaces has been studied at $20{\sim}80^{\circ}C$ and pH 10 in silicate solutions with silica nuclei. The reaction falls into two kinetics regimes, limited at high silicic acid species concentration by polymerization, but at lower concentration by a process whereby deposited silicic acid species condenses further to silica. The overall condensation is first-order in silicic acid species concentration, proceeded toward to pseudo equilibrium concentration, $C_x$, rather than the solubility of amorphous silica. The heat of solution of amorphous silica was 3.34 kcal/mol and exhibits an Arrhenius temperature dependence with an apparent activation energy of 3.16 kcal/mol in the range of $20{\sim}80^{\circ}C$.

Examination of Wet Process Comnibation and Thermal Reclamation Condition in Sand Reclamation of Inorganic Binder Process (무기 공정 모래 재생 처리에서의 습식 처리 조합과 배소 조건 검토)

  • Ryuya Ogusu;Yoshiki Tanaka;Hayato Tomochika
    • Journal of Korea Foundry Society
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    • v.43 no.5
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    • pp.260-263
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    • 2023
  • 이 보고서에서는 무기 공정에서의 무기 인공 재생 모래의 특성을 중심으로 다음과 같이 정리할 수 있다. 1) ICP 발광 분광 분석을 통한 재생 모래의 Na+ 용출량, TP 휨강도 및 충전 밀동에는 높은 상관 관계가 확인되었다. 2) 현행 재생 방법 대비, 습식 연마 처리를 첨가함으로써 잔류 점결재가 제거되고 Na+ 용출량이 저감된 결과, 재생 모래의 TP 휨강도를 보다 개선 가능한 것이 확인되었다. 3) 재생 처리 공정 순서를 건식 연마 → 습식 연마 → 배소 처리로 함으로써, 가장 Na+ 용출량이 낮고, 높은 휨강도를 얻을 수 있는 것이 확인되었다. 4) 습식 연마 단계를 거치지 않고 배소 처리 온도와 처리 시간을 궁리함으로써 충분한 품질의 재생 모래를 얻을 수 있는 가능성이 시사되었다. 마지막으로, 무기 공정은 유기 공정에 비해 압도적으로 냄새가 적고 생산성이 높으며 인공 모래와의 병용을 통한 재생 처리시의 폐기물량 저감, 주조품의 고품질화 등 이점이 기대되는 공정이다.

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Preparation of Cellular Liquid from Brown Seaweeds for Functional Tonic Products (기능성 음료의 개발을 위한 갈조류 생세포액의 제조)

  • 강영주;류근태;김효선
    • Journal of the Korean Society of Food Science and Nutrition
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    • v.25 no.1
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    • pp.94-103
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    • 1996
  • 기능성 해조음료를 개발하기 위하여 미역, 톳 및 다시마를 저온하에서 마쇄, 원심분리, 한회여과를 거쳐 생해조 세포액을 얻었으며, 각 해조 생세포액의 성분 분석과 색차 측정 및 관능검사를 통하여 품질평한 결과 다음과 같았다. 원심분리 후 한외 여과에 의한 생세포액의 수율은 생해조에 대하여 6.8~56.5% 였으며, 톳과 미역의 수율은 높았으나 다시마는 수율이 낮았다. 해조액을 한회여과한 다음 동결건조한 시료의 회분 합량은 28~60%였으며, 조단백 함량은 12.7%~6.7%정도 였는데 미역과 톳은 다시마 보다 각 성분의 함량이 많았다. 알긴산과 chlrophyll 및 carotenoid 은 한회여과막에 의하여 대부분 제거되었으나 톳의 polyphenol은 30K 한외여과막에 의해서도 효과적으로 제거되지 않았다. 다시마와 톳 생세포액의 주요 아미노산은 glutamic acid와 aspartic acid 였으며, 미역의 경우는 alanine, aspartic acid, valine이었다. 해조 생세포액중의 무기 질은 칼륨의 함량이 특히 높았으며 양이온의 경우 나트륨, 마그네슘, 칼슘, 철, 아연, 망간, 구리순으로 함유 되어있었다. 음이온으로는 $Cl^{-}$,$SO_{4}^{2-}$,$HPO_{4}^{2-}$,$NO_{3}^{-}$의 함량이 높았으며, I와 Br의 함량은 다시마가 톳과 미역에 비하여 높았다.

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The Effect of pH on Citric Acid Leaching of Soil Contaminated with Heavy Metals (중금속(重金屬) 오염토양(汚染土壤)의 구산(枸酸) 침출(浸出)에 대한 pH의 영향(影響))

  • Jung, Kyungbae;Park, Hongki;Yoo, Kyoungkeun;Park, Jay Hyun;Choi, Ui Kyu
    • Resources Recycling
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    • v.22 no.5
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    • pp.13-19
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    • 2013
  • The effect of pH on the citrate leaching behavior of heavy metal ion was investigated to develop an eco-friendly process for removing heavy metals from soil contaminated with copper, zinc, and lead. The leaching tests were performed using citrate solution with pH adjusted by mixing citric acid and sodium citrate under the following leaching conditions: particle size, under $75{\mu}m$; temperature, $50^{\circ}C$; citrate concentration, $1kmol/m^3$; pulp density, 5%; shaking speed, 100 rpm; leaching time, 1 hour. The difference of pH before and after the leaching test was not observed, and this result indicates the direct effect of hydrogen ion concentration on the leaching of metals was insignificant. The removal ratios of copper, zinc, and lead from the contaminated soil decreased with increasing pH. The thermodynamic calculation suggests that the leaching behaviors of metal ions were determined by two reactions; one is the reaction to form complex ions between heavy metal ions and citrate ion species, and the other is the reaction to form metal hydroxide between heavy metal ions and hydroxide ion.

Characterization of Silica Sol Particle Prepared by Sol-Gel Reaction from Sodium Silicate Solution (소디움실리케이트 수용액(水溶液)으로부터 솔-젤 반응(反應)에 의해 제조(製造)된 실리카 솔 입자특성(粒子特性) 고찰(考察))

  • Kim, Chul-Joo;Kim, Sung-Don;Jang, Hee-Dong;Yoon, Ho-Sung
    • Resources Recycling
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    • v.18 no.6
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    • pp.30-37
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    • 2009
  • Silica sol was prepared from the mixture of sodium silicate solution and oxidized silicate solution in which sodium had been removed by sol-gel process. The properties of sodium silicate solution and silicate solution thus prepared were characterized by yellow silicomolydate method. Moreover, the formation and growth of silica sol from sodium silicate solution was investigated. Sodium silicate solution with 2% of $SiO_2$ contains 95% of reactive silicate, and 50% of reactive silicate participates sol-gel reaction. From the results of FT-IR analysis, it was found that the intensity of silanol bond decreased and the intensity of siloxane bond increased with increasing reaction temperature. Zeta potential of silica sol prepared at each condition was -40~-60 mV and it could be known that silica sol in this study was well dispersed. The silica sol with 5~10 nm size could be prepared by heating the mixed solution of sodium silicate and silicate solution. And the silica sol grew into about 20 nm as silicate solution was added to silica sol solution.