• Title/Summary/Keyword: Hydroxide ion

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PERIAPICAL TISSUE REACTION AND ROOT RESORPTION FOLLOWING REPLANTATION WITH DIFFERENT CALCIUM HYDROXIDE PASTES IN RAT (치아재식술 시 근관충전재로 사용된 수산화칼슘 제재의 치근단 조직 반응 및 치근 흡수의 평가)

  • 송상채;이승종;정일영;이찬영;금기연
    • Restorative Dentistry and Endodontics
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    • v.26 no.2
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    • pp.111-120
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    • 2001
  • Calcium hydroxide pastes is widely used in conventional endodontics. Along with the expanded clinical use of calcium hydroxide, literatures suggest mixing calcium hydroxide with other substance. Among added substances the vehicle plays the most importance role in the overall process because it is directly related with the velocity of ionic dissociation of $Ca^{2+}$ and OH ion. In this study, we evalutated and compared periapical tissue response and root resorption after canal was filled with mixture of saline and calcium hydroxide(Junsei Chemical Co.. Japan) as a aqueous vehicle, Metapaste(Meta Co., Korea) as a viscous vehicle paste, Vitapex(Neo Dental, Japan) as a oily vehicle paste and IRM(Caulk Dentsply, USA) in replantation of rat molar. A total of 31 maxillary first molars of Sprague-Dawley female rats, 30 days old were used. The upper 1st molar was extracted and the mesiobuccal canal was filled with mixture of saline and calcium hydroxide, Metapaste, Vitapex. IRM and then replanted. Rats were sacrificed 3 weeks after replantation. the maxillae were removed. section of 4 micron were cut and stained with hematoxylin-eosin, Apical tissue response were observed under light microscope. The results were as follows: 1. Saline mixing group and Metapaste group were significant different in fibrous capsule width compared to Vitapex group and IRM group(P<0.05). 2. Saline mixing group. Metapaste group. Vitapex group and IRM group did not prevent root resorption and there were no statistical difference. 3. In saline mixing group and Metapaste group. loss of pastes were observed in all samples. From the results of our study. we observed loss of pastes in saline mixing group and Metapaste group because of water soluble property and assumed it was related to inflammation in apical area and sealing ability of material. So, we should study and develop calcium hydroxide vehicle which is easily removed and more stable and because of only 3 weeks observation we need more evaluation in long period.

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A Basic Study on the Removal of Iron Ion in Waste Water by the Precipitation Method (침전법에 의한 폐수중의 철이온 제거에 관한 기초 연구)

  • 강동현;김형석;조동성
    • Resources Recycling
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    • v.2 no.2
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    • pp.16-21
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    • 1993
  • This study was carried out to investigate the settling characteristics of Fe(II) and Fe(III) hydroxide precipitates formed by pH adjustment of aqueous solution to remove ferrous and ferric ion in waste water. The results obstained in this study are as fellows : The settling rate was effectively increased with increasing the pH values of aqueous solution regulated by CaO and with increasing the amount of flocculant, on the other hand, application of excess flocculants decreased the settling rate. It is desirable that the concentration of iron ion is kept under $10^{-2}$ mol/ㅣ because the settling rate was decreased with increasing the concentration of iron hydroxide precipitates.

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Recovery of Valuable Lithium Hydroxide by Ion Exchange Process: A Review (이온 교환 공정에 의한 귀중한 수산화 리튬의 회수: 리뷰)

  • Sarsenbek, Assel;Rajkumar, Patel
    • Membrane Journal
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    • v.32 no.6
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    • pp.401-410
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    • 2022
  • Demand for lithium hydroxide (LiOH) is annually increasing due to its efficiency and safety for the environment in comparison to its current alternatives. Lithium can be found in different salty and brine lakes which later synthesized to produce LiOH for various applications. Different methods are used to separate and recover lithium ions, the most common of which is electrodialysis (ED). ED is a membrane-based separation technique which works on potential difference of its layers as a driving force to push ions from one side to another. The ion exchange membrane (IEM) in ED makes the process efficient because of the perm selectivity of different ions vary depending on their hydrodynamic volume. In this review, the different alteration strategies of both ED and IEM, to enhance the recovery of lithium ions are discussed.

Evaluation of Chloride Ion Binding Capacity of Hardened Portland Cement Paste Containing Hydrotalcite (경화된 하이드로탈사이트 혼입 포틀랜드 시멘트 페이스트의 염소이온 고정능력 평가)

  • Han, Jae-Do;Lee, Yun-Su;Lee, Han-Seung
    • Proceedings of the Korean Institute of Building Construction Conference
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    • 2018.05a
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    • pp.27-28
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    • 2018
  • Deterioration of reinforced concrete structures due to salt corrosion is a phenomenon that can be easily seen, and the main reason for deterioration is chloride ion. Therefore, researches are actively conducted to control chlorine ion penetration worldwide. The purpose of this study is to evaluate the chloride ion fixation capacity of Portland cement paste containing Hydrotalcite. For this purpose, cement paste containing 0%, 2.5%, and 5% of Hydrotalcite was sealed and cured for 28 days, and the cured cement paste was crushed. Chloride ion solution was prepared at a concentration of 0.5M using NaCl, and the powdered cement paste was reacted for a specific time in aqueous chloride ion solution. After the reaction, the concentration of the chloride ion aqueous solution was measured using a silver nitrate potentiometric titrator, and the reacted cement paste was analyzed using XRD and FT-IR.

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2, 4, 6-Trinitrotoluene(TNT) Treatment by the Alkaline Hydrolysis (가수분해에 의한 2, 4, 6-Trinitrotoluene(TNT) 처리)

  • Kwon, Bumgun;Kim, Jongoh
    • Journal of the Korean GEO-environmental Society
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    • v.13 no.9
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    • pp.69-74
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    • 2012
  • This study investigated the TNT decomposition by the treatment of alkaline hydrolysis. To obtain this objecitive, spectrum shift characteristics, pH effect, kinetics, and product analysis were examined during the alkaline hydrolysis by means of hydroxide ions. At pH = 12, an aqueous solution of TNT was changed into yellow-brown coloring, in which its absorbances were newly increased in a range of wavelength 400-600 nm. From the kinetic data, pseudo-first-order rate constant in a excess of hydroxide ion, in contrast to TNT concentration, was $0.0022min^{-1}$, which means that the reaction rate between TNT and hydroxide ion can be very slow, and that 1,047 min is necessary to achieve a 90% reduction of the initial TNT. In products analyses, nitrite ions and formic acid were mainly produced by the alkaline hydrolysis, nitrate ions and oxalic acid as minor products were generated.

Synthesis of its Tautomeric Forms and New 6-Substituted Pyridazin-3(2H)-one Analogs (새로운 6-Substituted Pyridazin-3(2H)-one 유도체 및 토토머형의 합성)

  • Kim, Chaewon;Park, Myung-Sook
    • YAKHAK HOEJI
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    • v.57 no.5
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    • pp.316-322
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    • 2013
  • The new pyridazinone analogs were synthesized for development of candidates to retain anticancer activity. Various 6-substituted pyridazin-3(2H)-ones were prepared from the pyridazinyl chloride 3a~d via endothermic nucleophilic substitution with hydroxide ion as nucleophile for 2~48 h. Pyridazinyl chloride 3a~d could be converted to hydroxypyridazines (or pyridazin-3(2H)ones) using 1~5 equivalents of water (or 1 equivalent of sodium hydroxide) at reflux in DMF. The tautomerism of lactim form to lactam form was also accomplished in pyridazine derivatives. Formation of pyridazinones 10 was undertaken with stirring using sodium hydroxide at reflux in DMF for 2 h. Synthetic compounds were identified using NMR spectrum.

Chemical characteristics of mineral trioxide aggregate and its hydration reaction

  • Chang, Seok-Woo
    • Restorative Dentistry and Endodontics
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    • v.37 no.4
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    • pp.188-193
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    • 2012
  • Mineral trioxide aggregate (MTA) was developed in early 1990s and has been successfully used for root perforation repair, root end filling, and one-visit apexification. MTA is composed mainly of tricalcium silicate and dicalcium silicate. When MTA is hydrated, calcium silicate hydrate (CSH) and calcium hydroxide is formed. Formed calcium hydroxide interacts with the phosphate ion in body fluid and form amorphous calcium phosphate (ACP) which finally transforms into calcium deficient hydroxyapatite (CDHA). These mineral precipitate were reported to form the MTA-dentin interfacial layer which enhances the sealing ability of MTA. Clinically, the use of zinc oxide euginol (ZOE) based materials may retard the setting of MTA. Also, the use of acids or contact with excessive blood should be avoided before complete set of MTA, because these conditions could adversely affect the hydration reaction of MTA. Further studies on the chemical nature of MTA hydration reaction are needed.

Arsenic Removal from Water Using Various Adsorbents: Magnetic Ion Exchange Resins, Hydrous Ion Oxide Particles, Granular Ferric Hydroxide, Activated Alumina, Sulfur Modified Iron, and Iron Oxide-Coated Microsand

  • Sinha, Shahnawaz;Amy, Gary;Yoon, Yeo-Min;Her, Nam-Guk
    • Environmental Engineering Research
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    • v.16 no.3
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    • pp.165-173
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    • 2011
  • The equilibrium and kinetic adsorption of arsenic on six different adsorbents were investigated with one synthetic and four natural types (two surface and two ground) of water. The adsorbents tested included magnetic ion exchange resins (MIEX), hydrous ion oxide particles (HIOPs), granular ferric hydroxide (GFH), activated alumina (AA), sulfur modified iron (SMI), and iron oxide-coated microsand (IOC-M), which have different physicochemical properties (shape, charge, surface area, size, and metal content). The results showed that adsorption equilibriums were achieved within a contact period of 20 min. The optimal doses of adsorbents determined for a given equilibrium concentration of $C_{eq}=10\;{\mu}g/L$ were 500 mg/L for AA and GFH, 520-1,300 mg/L for MIEX, 1,200 mg/L for HIOPs, 2,500 mg/L for SMI, and 7,500 mg/L for IOC-M at a contact time of 60 min. At these optimal doses, the rate constants of the adsorbents were 3.9, 2.6, 2.5, 1.9, 1.8, and 1.6 1/hr for HIOPs, AA, GFH, MIEX, SMI, and IOC-M, respectively. The presence of silicate significantly reduced the arsenic removal efficiency of HIOPs, AA, and GFH, presumably due to the decrease in chemical binding affinity of arsenic in the presence of silicate. Additional experiments with natural types of water showed that, with the exception of IOC-M, the adsorbents had lower adsorption capacities in ground water than with surface and deionized water, in which the adsorption capacities decreased by approximately 60-95%.

Treatment Features of Ni Wastewater by using Coffee Grounds as the Adsorbent (커피 찌꺼기를 흡착제로 한 니켈 폐수 처리 특성)

  • Seo, Myung-Soon;Kim, Dong-Su
    • Journal of Korean Society on Water Environment
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    • v.21 no.1
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    • pp.14-20
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    • 2005
  • A feasibility study has been conducted regarding the application of waste coffee grounds as an adsorbent for the treatment of nickel ion containing wastewater. The major variables which considered to influence the adsorbability of nickel ion were its initial concentration, reaction temperature, pH, and coexisting ion. The specific surface area of coffee grounds used in the experiment was found to be ca. $39.67m^2/g$, which suggesting its potential applicability as an adsorbent due to its relatively high surface area. In the experimental conditions, more than 90% of the initial amount of nickel ion was shown to adsorb within 15 minutes and equilibrium in adsorption was attained after 3 hours. The adsorption behavior of nickel ion was well explained by Freundlich model and kinetics study showed that the adsorption reaction was second-order. Adsorption was reduced with temperature and its change of enthalpy in standard state was estimated to be -807.05 kJ/mol. Arrhenius equation was employed for the calculation of the activation energy of adsorption and nickel ion was observed to adsorb on coffee grounds exoentropically based on thermodynamic estimations. As pH rose, the adsorption of nickel ion was diminished presumably due to the formation of cuboidal complex with hydroxide ion and the coexistence of cadmium ion was found to decrease the amount of nickel ion adsorption, which was proportional to the concentration of cadmium ion.

Visualization of Ion Transport and pH Change in Ion Concentration Polarization (농도 분극 현상에서의 이온의 흐름과 pH 변화의 가시화)

  • Ko, Sung-Hee;Kang, Kwan-Hyoung
    • Journal of the Korean Society of Visualization
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    • v.8 no.4
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    • pp.38-42
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    • 2010
  • Ion concentration polarization is an electrokinetic phenomenon which occurs in membrane systems, such as in an electrodialysis and fuel-cell system. But the phenomenon is not fully understood because hydrodynamics, electrokinetics and electrochemistry are coupled with each other. Here, we report that there occurs a change of pH value of buffer solution in concentration polarization phenomenon. To visualize the change of pH, the litmus solution which is one of the pH indicators was used. It is conjectured that the pH of solution changes because hydrogen ions were concentrated in cathodic side and hydroxide ions were concentrated in anodic side. We anticipate that this work may contribute to the fundamental understanding on the ion concentration polarization phenomenon.