• Title/Summary/Keyword: $Ca(OH)_$2

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Rate Enhancement of Thermal Decomposition Reaction in the $Ca(OH)_2$ Packed Bed ($Ca(OH)_2$ 충전층의 열분해 반응 촉진)

  • Chung, Soo-Yull;Kim, Do-Wan;Kim, Jong-Shik
    • Solar Energy
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    • v.15 no.1
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    • pp.73-84
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    • 1995
  • The present paper is on the utilization of a thermal decomposition reaction $Ca(OH)_2=CaO+H_2O$, for thermal energy storage. One of the important problems in this case is how to heat up and decompose the particle of $Ca(OH)_2$ effectively where the thermal conduction is poor. In this study, the effects of Cu-plates which are placed in the $Ca(OH)_2$ packed bed as heat transfer fins are investigated experimentally. The results show that the Cu-plates are very effective for heat transfer and the thermal decomposition in the $Ca(OH)_2$ packed bed. The amount of time to dehydrate took less than a half than that without fins under the conditions of this study.

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Synthesis of Hydroxycalciumphosphate (수산화 인산칼슘의 합성)

  • Hwang, Young-Gil;Kim, Youn-Soo;Kim, Jae-Il
    • Resources Recycling
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    • v.5 no.3
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    • pp.50-55
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    • 1996
  • The synthesis of Ca,,(PO,),(OH), by adding (NFIa)J),HPO, to lhe solution of Ca(NO,), dlssolvad CaO in HNO, and contmlled pH with NH,OH was carried out for certain time at room temperahire and atmosphere. Ca,,(PO,),(OH), was rorrned at the range from pN 10 to pH 13. The particle s~zeof Ca,,(PO,),(OH)i was 0.1-0.5 &In. Thc optimum reaction lime was 30 min, and the temperature was 40-70$^{\circ}$C. the shape also was not changed in spite of heating to iDVC hr 1 hour the c~ystalliratian temperature was 90$^{\circ}$C Ca,,(PO,),(OH), was calcinatcd and the shape also was not changzd, in spile of hcaling to 500$^{\circ}$C for 1 hour. But Ca,,(PO,),(OH), calcinated for lhour al 800$^{\circ}$C was changed to the spheric particle of Ca,,,(PO,),(OH),, CaO and Ca,(PO,),.

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Hydration Properties of 3CaO.3A12O3.CaSO4.CaSO4ㆍ2H2O - Ca(OH)24 - 3CaO.Al2O3 System (3CaO.3A12O3.CaSO4.CaSO4.2H2O - Ca(OH)24 - 3CaO.Al2O3계의 수화 특성)

  • 배승훈;송종택
    • Journal of the Korean Ceramic Society
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    • v.40 no.9
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    • pp.859-866
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    • 2003
  • When calcium sulfoaluminate-based expansive cement was hydrated, ettringite and monosulfate were mainly formed. The crack of hardened cement was prevented by compensating drying shrinkage due to formation of the above hydrates. In order to study the hydration properties of calcium sulfoaluminate-based expanding cement, 3CaOㆍ3Al$_2$O$_3$ㆍCaSO$_4$(C$_4$A$_3$S) was prepared by chemical synthesis, and then the hydration of $C_4$A$_3$S-Ca(OH)$_2$-CaSO$_4$.$2H_2O$-C$_3$A system_was characterized. Good $C_4$A$_3$S phase was prepared at $1300^{\circ}C$ by chemical synthesis, and the main hydration product of $C_4$A$_3$S-Ca(OH)$_2$-CaSO$_4$.2$H_2O$ system was ettringite. In the case of hydration $C_4$A$_3$S-Ca(OH)$_2$-CaSO$_4$ㆍ 2$H_2O$-C$_3$A system, ettringite was formed in the early period and it was transformed into monosulfate while consumed gypsum.

The Hydration of Hardenced Flyash-$Ca(OH)_2-CaSO_4$.$2H_2O$ System (Flyash-$Ca(OH)_2-CaSO_4$.$2H_2O$계의 수화반응)

  • 김창은;이승헌;이상완;김원기
    • Journal of the Korean Ceramic Society
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    • v.23 no.3
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    • pp.27-34
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    • 1986
  • The hydration of flyash-$Ca(OH)_2-CaSO_4$.$2H_2O$ system was stuedied with varing mixing ratio of flyahs $Ca(OH)_2$ and caSO4.2H2O The samples were steam-cured for 1-7 days at 9$0^{\circ}C$. The optimum mixing composition was flyash : Ca (OH)2=65:35 with 15% $CaSO_4$.42H_2O$ added which produced the hardened material having the best compressive strength (300kg/$cm^2$) Also the low specific gravity(1, 2) of the hardened paste suggests the possibility that it can be used as a light-weight building material. The added $CaSO_4$.42H_2O$ constituted calcium-sulfo-aluminate hydrates which activates the formation of C-S-H hy-drates. Both hydrates developed the strength of hardened paste. The amount of calcium-sulfo-aluminate hydrates was increased when the $CaSO_4$.42H_2O$ was added over 15% however the increased amount did not help the development of strength because of the individually grown calcium-sulfo-aluminate hydrates.

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A Study on the Characteristics of Ca(OH)2 According to the Calcination Conditions of Oyster Shells and Its Application for Exterior Water Paints (굴 패각의 소성 조건에 따른 소석회의 특성과 외부용 수성 도료 적용 연구)

  • Hwang, Dae Ju;Yu, Young Hwan;Han, Chang Soo;Lee, Jong Dae
    • Korean Chemical Engineering Research
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    • v.60 no.4
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    • pp.594-605
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    • 2022
  • CaO was prepared by calcining for oyster shells using a microwave kiln. It was analyzed to Ca(OH)2 synthed on hydration reaction from prepared CaO. The synthesized Ca(OH)2 was formulated as an external water paint. Oyster shells (325 mesh, 43 ㎛) were decarbonized for (a) 950 ℃/1 hr and (b) 1,150 ℃/1 hr to prepare CaO. In the calcination condition of (a), CaO was 56.7 wt%, and in the calcination condition of (b), CaO was 100 wt%. To compare CaO by calcination of oyster shells with that of limestone, limestone (25~30 mm) was decarbonized at 950 ℃/1 hr to prepare CaO, and as a result of the analysis(XRD), it was analyzed as CaO 100 wt%. CaO was prepared under the calcining conditions of oyster shells (b) 1,150 ℃/1 hr, and Ca(OH)2 was synthesized through hydration. Hydration conditions of the prepared CaO were (a) CaO : H2O(100 g : 200 g) and (b) CaO : H2O(100 g : 400 g). As a result of the hydration reaction, it was confirmed as low reactivity. 100 wt% of Ca(OH)2 was synthesized. In particular, Ca(OH)2 synthesized under the hydration condition of (a) was analyzed in a plate shape. An external water paint was formulated with Ca(OH)2 synthesized from oyster shells as the main component. When 15 items of the external water paint standard specification (KS M 6010) were analyzed, it was confirmed that all other criteria were satisfied except for freezing stability.

Synthesis and Crystal Structure of Amorphous Calcium Carbonate by Gas-Liquid Reaction of System CaO-$C_2 H_5 OH$-$CO_2$ (CaO-$C_2 H_5 OH$-$CO_2$계의 기.액반응에 의한 비정질 탄산칼슘의 합성 및 결정구조)

  • Im, Jae-Seok;Im, Goeng
    • The Journal of Engineering Research
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    • v.6 no.1
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    • pp.97-109
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    • 2004
  • The synthesis and crystal structure of amorphous calcium carbonate obtained from gas-liquid reaction of CaO-$C_2 H_5 OH$-$CO_2$ system according to change of added amount of calcium oxide by blowing $CO_2$ gas and reaction time using ethanol and ethylene glycol were investigated by electric conductivity, X-ray diffraction, and scanning electron microscope. The powdery or gelatinous phases were prepared by passing $CO_2$ gas at a flow rate of 1$\ell$/min into the suspensions containing 10~40g of CaO in mixing solutions 900ml of $C_2 H_5 OH$- and 100ml of ethylene glycol. By rapid filtration and drying the both phases at $60^{\circ}C$ under reduced pressure, the phases converted to the spherical vaterite and amorphous phase. The stable phase of amorphous calcium carbonate(ACC) was formed in the region pH 7-9 but the formation regions of amorphous phase were remarkably affected by pH in the mother liquor. It seems that a part of ACC changed into chain calcite as an intermediate products. The initial reactants prior to the formation of precipitated calcium carbonate is ACC. And ACC is unstable in the aqueous solution and crystallizes finally to calcite by the through-solution reaction. Especially ACC was produced or gelatinous phase which precipitated from the reaction of CaO-$C_2 H_5 OH$-$CO_2$ system.

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The Prediction Model of Carbonation Process by CO2 Diffusion Using the Air Permeability Coefficient for Concrete (콘크리트의 투기계수를 이용한 CO2확산 탄산화진행 예측모델)

  • Kang, Suk-Pyo;Kim, Young-Sun;Song, Ha-Won;Kim, Gyu-Yong
    • Journal of the Korea Concrete Institute
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    • v.22 no.2
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    • pp.209-217
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    • 2010
  • Recently, some mathematical models for the prediction on progress of carbonation of concrete were reported. These models take account for $CO_2$ diffusion and chemical reaction between $Ca(OH)_2$ and $CO_2$. Based on the assumption that $CO_2$ diffuses in the carbonation zone and reacts with $Ca(OH)_2$ at the outer face of carbonation zone and non-carbonation zone. In this study, a mathematical model to predict the progress of carbonation of concrete has been established based on the reducing concentration of $Ca(OH)_2$ in the carbonation progress zone, where $Ca(OH)_2$ reacts with $CO_2$ and $Ca(OH)_2$ and $CaCO_3$ coexist. Also, the prediction model of carbonation progress rate of concrete using the air permeability coefficient regarding to $CO_2$ diffusion is developed. As a result of this study, an expression, the model equation is obtained for the prediction of carbonation based on the time and interaction velocity between $CO_2$ and Ca(OH)$_2$ dependent air permeability coefficient. The prediction by the model satisfied the experimental data of the accelerated carbonation for painted concrete. Consequently, the model can predict the rate of carbonation and the potential service life of concrete structure exposed to atmosphere.

Ca-Alginate에 고정화된 Calcium Carbonate를 완충제로 사용한 Bifidobacterium longum의 배양 증대와 저장 안정성

  • Lee, Gi-Yong;Yu, Won-Gyu;Kim, Ji-Yeon;Heo, Tae-Ryeon
    • 한국생물공학회:학술대회논문집
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    • 2000.04a
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    • pp.203-206
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    • 2000
  • Calcium carbonate $(CaCO_3)$ bead immobilized with alginate were developed as buffer system to enhance the cultivation efficiency of bifidobacteria. When Bifidobacteriuim longum KCTC 3128 and HLC 3742 were independently cultivated in 2.5-liter fermenter buffered the $CaCO_3$ bead, NaOH, $Na_2CO_3$, and $NH_4OH$. The proliferation of bifidobacteria and their storage stability were higher in culture broth buffered $CaCO_3$ beads than in culture broth buffered with NaOH, $Na_2CO_3$, and $NH_4OH$. Therefore, $CaCO_3$ bead may be useful as a buffer to enhance of the cultivation efficiency and viability of bifidobacteria.

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Photocatalytic Oxidation of NOx onCaO/TiO2 (CaO/TiO2에서 NOx의 광촉매 산화반응에 대한 연구)

  • Shin Joong-Hyeok;Lim Woong-Mook;Jun Jin
    • Journal of Environmental Science International
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    • v.15 no.6
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    • pp.533-538
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    • 2006
  • Removal of $NO_x$ on $CaO/TiO_2$ photocatalyst manufactured by the addition of $Ca(OH)_2$ was measured in relation with the amount of $Ca(OH)_2$ and calcination temperature. In case of pure $TiO_2$, the $NO_x$ removal decreased greatly with the increase of calcination temperature from $500^{\circ}C\;to\;700^{\circ}C$, whereas in the photocatalyst added with $Ca(OH)_2$, the removed amount of $NO_x$ was high and constant regardless of calcination temperature. Considering $NO_x$ removal patterns depending on the amount of $Ca(OH)_2$ added(50, 30, 10wt%), high removal rate showed at the photocatalysts containing less than 30wt% of $Ca(OH)_2$, and it was about 30% higher than that of pure $TiO_2$. From the XRD patterns, it is seen that the addition of $Ca(OH)_2$ contributes to maintaining the anatase structure that is favourable to photocatalysis. It also indicates that the possibility of the formation of calcium titanate($CaTiO_3$) by reacting with $TiO_2$ above $700^{\circ}C$. Apart from the favourable crystalline structure, the addition of $Ca(OH)_2$ helped increase the alkalinity of photocatalyst surface, thus promoting the photooxidation reaction of $NO_x$.