• 제목/요약/키워드: Pitzer

검색결과 9건 처리시간 0.021초

25℃에서 ZnSO4-Fe2(SO4)3-Na2SO4-H2SO4-NaOH-H2O계에 대해 Pitzer식과 Vasil'ev식에 의한 이온평형해석 비교 (Comparison of Ionic Equilibria Analysis of ZnSO4-Fe2(SO4)3-Na2SO4-H2SO4-NaOH-H2O System at 25℃ between Pitzer and Vasil'ev Equation)

  • 이만승;이경주;남상호
    • 분석과학
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    • 제16권2호
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    • pp.159-165
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    • 2003
  • 아연산화광 황산침출액에 적용가능한 이온평형모델을 개발하기 위해 Vasil'ev식과 Pitzer식에 의한 해석방법을 비교하였다. 이온강도가 9 m정도로 증가할수록 Vasil'ev식보다는 Pitzer식에 의한 용액의 이온평형결과가 정확하였다. 아연산화광 황산침출액을 모사하기위해 $25^{\circ}C$에서 $ZnSO_4-Fe_2(SO_4)_3-Na_2SO_4-H_2SO_4-NaOH-H_2O$계에 대해 전해질의 농도를 변화시키며 혼합한 용액의 pH 측정값과 본 연구에서 계산한 pH값은 서로 잘 일치하였다.

$ZnSO_4-Na_2SO_4-H_2SO_4-NaOH-H_2O$계의 이온 평형 (Ionic Equilibria in $ZnSO_4-Na_2SO_4-H_2SO_4-NaOH-H_2O$ System)

  • 이만승;박현주;나춘기
    • 자원리싸이클링
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    • 제11권1호
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    • pp.19-25
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    • 2002
  • $ZnSO_4$- $Na_2$$SO_4$-$H_2$$SO_4$-$NaOH-H_2$O계에 대해 전해질의 농도를 변화시키며 $25^{\circ}C$에서 용액의 pH를 측정하고, K-value방법을 이용하여 이온평형을 해석하였다. 물의 활동도와 용질의 활동도계수는 Pitzer식으로 계산하였다. 평형상태에서 존재하는 용질들의 농도와 활동도계를 전해질의 초기농도로부터 이온평형을 해석하여 구할 수 있었다 이온강도가 4 m정도로 진한 용액에서 pH측정값과 이온평형 해석으로 구한 pH 이론 값은 서로 잘 일치하였다. 액의 이온강도가 3.5에서 4.3사이의 실험조건에서 Pitzer식으로 구한 $ZnSO_4$의 평균이온 활동도계수는 문헌에 발표된 값과 잘 일치하였다.

NaCl + CaCl2 + H2O 및 KCl + CaCl2 + H2O 삼성분계에 대한 50℃에서의 용해도 측정 (Measurement of Solubilities in the Ternary System NaCl + CaCl2 + H2O and KCl + CaCl2 + H2O at 50℃)

  • Yang, Ji-Min;Hou, Guang-Yue;Ding, Tian-Rong;Kou, Peng
    • 대한화학회지
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    • 제54권3호
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    • pp.269-274
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    • 2010
  • NaCl-$CaCl_2$-$H_2O$와 KCl-$CaCl_2$-$H_2O$계의 용해도와 물리화학적 성질(굴절률)을 $50^{\circ}C$에서 측정하였으며, 그 결과를 상평형 그림과 조성에 따른 물리화학적 성질에 대한 도표로 나타내었다. 삼성분계의 상 평형 그림은 불변점이 하나, 일변수 곡선이 둘, NaCl (또는 KCl) 및 $CaCl_2{\cdot}2H_2O$에 대응되는 결정화 지역이 두 개가 있음을 보여주었다. 이들 계에 대하여 혼합 파라미터인 ${\theta}_{M,Ca}$${\Psi}_{M,Ca,Cl}$ (M = Na or K), 평형상수 $K_{sp}$를 최소제곱법을 이용하여 결정하였으며, 이때, NaCl, KCl 및 $CaCl_2$의 단일-염 Pitzer 파라미터 ${\beta}^{(0)}$, ${\beta}^{(1)}$, ${\beta}^{(2)}$ and $C^{\Phi}$는 참고문헌을 통하여 직접 계산하였다. 이 결과들은 실험결과와 잘 일치하였다.

암모니아수 흡수제를 이용한 이산화탄소 제거 공정에서 침전생성이 조업영역에 미치는 영향 (Effect of Precipitation on Operation Range of the CO2 Capture Process using Ammonia Water Absorbent)

  • 유정균;박호석;홍원희;박종기;김종남
    • Korean Chemical Engineering Research
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    • 제45권3호
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    • pp.258-263
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    • 2007
  • 배가스 이산화탄소 처리를 위한 화학적 흡수공정의 새로운 흡수제로서 암모니아수의 적용 가능성을 고찰하였다. 이산화탄소 흡수용량과 침전 발생의 관점에서 적합한 암모니아수 흡수제 농도와 $CO_2$ 부하(loading, $molCO_2/molNH_3$)를 결정하였다. 이를 위하여 전해액에 대한 Pitzer 모델을 이용하여 암모니아 흡수제 농도에 따른 흡수용량과 침전 발생여부를 계산하였다. $5\;molNH_3/kgH_2O$ 이상의 암모니아수 흡수제를 사용하여 기존 아민류 흡수제 이상의 흡수용량은 얻을 수 있었다. 각 암모니아 흡수제 농도에서 $NH_4HCO_3$ 침전의 발생으로 인하여 조업이 제약되는 $CO_2$ 부하를 구하였다. $5{\sim}14\;molNH_3/kgH_2O$의 암모니아 흡수제는 293, 313 K에서 $CO_2$ 부하 0.5 이상에서 침전이 발행하였다. 침전 생성 $CO_2$ 부하값 이하로 흡수탑을 조업함으로써 고농도 암모니아 흡수제가 배가스 $CO_2$ 처리 공정에 사용될 수 있음을 알 수 있었다. 흡수용량과 침전발생을 고려하여 배가스 이산화탄소 처리를 위한 흡수제 최적온도는 암모니아수 농도에 따라 297~312 K이었다.

Scaling predictions in seawater reverse osmosis desalination

  • Hchaichi, Houda;Siwar, Saanoun;Elfil, Hamza;Hannachi, Ahmed
    • Membrane and Water Treatment
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    • 제5권3호
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    • pp.221-233
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    • 2014
  • Simulations were conducted to predict supersaturation along Reverse Osmosis (RO) modules for seawater desalination. The modeling approach is based on the use of conservation principles and chemical equilibria equations along RO modules. Full Pitzer ion interactive forces model for concentrated solutions was implement to calculate activity coefficients. An average rejection rate for all ionic species was considered. Supersaturation has been used to assess scaling. Supersaturations with respect to all calcium carbonate forms and calcium sulfate were calculated up to 50% recovery rate in seawater RO desalination. The results for four different seawater qualities are shown. The predictions were in a good agreement with the experimental results.

Marine macroalgae of the Aleutian Islands: I. Bangiales

  • Lindstrom, Sandra C.;Lindeberg, Mandy R.;Guthrie, Daniel A.
    • ALGAE
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    • 제30권4호
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    • pp.247-263
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    • 2015
  • We sequenced the rbcL gene in more than 100 collections of foliose Bangiales made in the Aleutian Islands and western Alaska Peninsula during the past 25 years. This work allows us to recognize four previously undescribed species, two in the genus Boreophyllum and two in Pyropia. Boreophyllum aleuticum appears to be endemic to the Aleutian Islands, whereas B. ambiguum is known to occur from the Yakutat area to the tip of the Alaska Peninsula. The two previously undescribed species of Pyropia are more broadly distributed. Pyropia taeniata, which was previously identified under the name Py. pseudolinearis, occurs from northern Southeast Alaska through the Aleutian Islands. Pyropia unabbottiae, which is sister to Py. abbottiae, occurs from southern Vancouver Island to Attu Island. Collections throughout the Aleutian Islands allow us to document the distribution of another dozen species of foliose Bangiales in this region, including Boreophyllum aestivale, Fuscifolium tasa, Pyropia fallax, Py. fucicola, Py. gardneri, Py. kurogii, Py. nereocystis, Py. pseudolanceolata, Py. torta, Wildemania amplissima, W. norrisii, and W. variegata. We were unable to confirm the occurrence of the following species previously recorded from the Aleutian Islands: Porphya ochotensis, Pyropia abbottiae, Py. perforata, Py. pseudolinearis, P. purpurea, P. umbilicalis, Py. yezoensis and Wildemania schizophylla. At least two undescribed filamentous Bangiales also occur in the Aleutian Islands.

염산용액에서 Alamine336에 의한 염화 제1, 2구리의 용매추출 (Solvent Extraction of Cuprous and Cupric Chloride from Hydrochloric Acid Solutions by Alamine336)

  • 이만승;이진영
    • 대한금속재료학회지
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    • 제47권5호
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    • pp.297-303
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    • 2009
  • Solvent extraction experiments of cupric and cuprous chloride with Alamine336 have been performed from HCl solution. In order to identify the solvent extraction reaction, distribution diagram of cupric and cuprous species with HCl concentration was obtained by considering complex formation reaction and the activity coefficient of solutes with Pitzer equation. Analysis of the solvent extraction data by graphical method together with the distribution diagram of copper indicated that solvent extraction reaction of copper with Alamine336 depends on HCl concentration. In strong HCl solution of 3 and 5 M, ${CuCl_4}^{2-}$ and ${CuCl_3}^{2-}$ took part in the solvent extraction reaction as Cu(II) and Cu(I), respectively. When HCl concentration was 1 M, ${CuCl_2}^-$ was extracted into the organic phase in the case of Cu(I) while adduct formation between $Cu^{2+}$ and Alamine336 was responsible for the solvent extraction reaction of Cu(II).

Equilibrium calculations for HyBRID decontamination of magnetite: Effect of raw amount of CuSO4 on Cu2O formation

  • Lee, Byung-Chul;Kim, Seon-Byeong;Moon, Jei-Kwon
    • Nuclear Engineering and Technology
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    • 제52권11호
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    • pp.2543-2551
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    • 2020
  • Calculations of chemical equilibrium for multicomponent aqueous systems of the HyBRID dissolution of magnetite were performed by using the HSC Chemistry. They were done by using a Pitzer-based aqueous solution model with the recipe of raw materials in experiments conducted at KAERI. The change in the amounts of species and ions and the pH values of the solution at equilibrium was observed as functions of temperature and raw amount of CuSO4. Precipitation of Cu2O occurred at a large amount of CuSO4 added to the solution, while no precipitation of Cu(OH)2 was found at any amounts of CuSO4. The E-pH diagrams for Cu were constructed at various Cu concentrations to provide the effect of the Cu concentration on the pH values at boundaries where the coexistence of Cu+ ion and Cu2O solid occurred. To prevent Cu+ ions from being precipitated to Cu2O, the raw amount of CuSO4 should be adjusted so that the pH value of the solution from the equilibrium calculation is less than that from the E-pH diagram. We provided guidelines for the raw amount of CuSO4 and the pH value of the solution, which prevent the formation of Cu2O precipitates in the HyBRID dissolution experiments for magnetite.

Temperature and Concentration Dependencies of Chemical Equilibrium for Reductive Dissolution of Magnetite Using Oxalic Acid

  • Lee, Byung-Chul;Oh, Wonzin
    • 방사성폐기물학회지
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    • 제19권2호
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    • pp.187-196
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    • 2021
  • Chemical equilibrium calculations for multicomponent aqueous systems involving the reductive dissolution of magnetite (Fe3O4) with oxalic acid (H2C2O4) were performed using the HSC Chemistry® version 9. They were conducted with an aqueous solution model based on the Pitzer's approach of one molality aqueous solution. The change in the amounts and activity coefficients of species and ions involved in the reactions as well as the solution pH at equilibrium was calculated while changing the amounts of raw materials (Fe3O4 and H2C2O4) and the system temperature from 25℃ to 125℃. In particular, the conditions under which Fe3O4 is completely dissolved at high temperatures were determined by varying the raw amount of H2C2O4 and the temperature for a given raw amount of Fe3O4 fed into the aqueous solution. When the raw amount of H2C2O4 added was small for a given raw amount of Fe3O4, no undissolved Fe3O4 was present in the solution and the pH of the solution increased significantly. The formation of ferrous oxalate complex (FeC2O4) was observed. The equilibrium amount of FeC2O4 decreased as the raw amount of H2C2O4 increased.