• 제목/요약/키워드: Zeolite-Structure

검색결과 217건 처리시간 0.026초

디젤엔진 배출가스 저감을 위한 CO, $C_3H_6$의 산화반응에서 Y-제올라이트 담체의 영향 (Effects of Y-Zeolite as a Support on CO, $CC_3H_6$ Oxidation for Diesel Emission Control)

  • 김문찬
    • 한국대기환경학회지
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    • 제13권1호
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    • pp.91-98
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    • 1997
  • Y-zeolite and ${\gamma}$-Al$_2$O$_3$ were used as supports on CO and $C_3$H$_{6}$ oxidation for diesel emission control. The catalysts composed of Pd and Pt as active components were wash coated on honeycomb type ceramic substrate. The oxidation of CO and $C_3$H$_{6}$ was carried out over prepared honeycomb in a fixed bed continuous reactor in the temperature range of 20$0^{\circ}C$~50$0^{\circ}C$ and 20,000 GHSV (h$^{-1}$ ). Surface area of Y-zeolite was larger than that of ${\gamma}$-Al$_2$O$_3$ due to channel structure of Y-zeolite. Therefore, high conversion of CO and $C_3$H$_{6}$ could be obtained because of good dispersion of active metals over Y-zeolite. The honeycomb used Y-zeolite as a support showed higher $C_3$H$_{6}$ conversion than that of ${\gamma}$-Al$_2$O$_3$ due to better cracking and isomerization activity of Y-zeolite. PdPt catalyst showed high conversion of CO and $C_3$H$_{6}$ at low temperature region, 20$0^{\circ}C$~30$0^{\circ}C$, for their synergy effects. PdPt/Y-Zeolite catalyst could achieve more than 80% conversion of $C_3$H$_{6}$ at 30$0^{\circ}C$. The use of Y-zeolite as a support increased CO and $C_3$H$_{6}$ conversion, and decreased SO$_2$ conversion very effectively. Y-zeolite found to have a good adaptability as a support for the diesel emission after treatment system.

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제올라이트를 PVA로 고정화한 흡착제에 의한 Cs과 Sr 이온 제거 (Removal of Cs and Sr Ions by Absorbent Immobilized Zeolite with PVA)

  • 이창한;이민규
    • 대한환경공학회지
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    • 제37권8호
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    • pp.450-457
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    • 2015
  • 본 연구에서는 제올라이트를 PVA에 고정화시켜 새로운 흡착제인 PVA-Zeolite 비드를 제조하고, XRD 및 SEM 분석을 통해 제조한 PVA-Zeolite 비드는 내부에 제올라이트가 잘 고정화된 다공성 구조를 가지고 있는 것을 확인할 수 있었다. 제조한 흡착제에 의한 Cs 이온과 Sr 이온에 대한 흡착특성을 살펴보기 위하여 pH의 영향, 흡착속도, 흡착등온을 검토하였다. Sr 및 Cs 이온에 대한 평형흡착시간은 약 540 min으로 나타났으며, 흡착속도는 유사 1차 속도식 보다는 유사 2차 속도식에 더 잘 부합하였다. 흡착평형 실험결과는 Langmuir 등온식에 잘 적용되었으며, Langmuir 등온식으로부터 구한 Sr 이온과 Cs 이온의 최대 흡착량은 각각 52.08 mg/g와 58.14 mg/g이었다. PVA-Zeolite 비드에 의한 Sr 이온과 Cs 이온의 흡착공정은 외부물질전달단계는 매우 빠르게 이루어지며, 내부입자확산에 의한 흡착반응은 느리게 진행되어 내부입자확산 단계가 흡착속도 결정단계인 것으로 판단된다.

천연(天然) Zeolite의 입경별(粒徑別) 수증기(水蒸氣) 흡착량(吸着量)과 비표면적(比表面積) 계산상(計算上)의 문제점(問題點) (Water Vapor Retention and Specific Surface Area of Fractionated Natural Zeolite)

  • 강신정;최정
    • Applied Biological Chemistry
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    • 제31권1호
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    • pp.86-91
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    • 1988
  • 경북(慶北) 월성산(月城産) Zeolite광석으로 조제(調製)한 $1{\sim}0.5,\;0,5{\sim}0.25,\;0.25{\sim}0.1$ 및 <0. 1mm의 4종류의 Zeolite 획분(劃分)의 비표면적(比表面積)이 수증기(水蒸氣) 및 EGME흡착법(吸着法)에 의(依)해 측정(測定)되었다. 수증기(水蒸氣) 및 EGME에 의(依)한 Zeolite의 비표면적(比表面積)은 각각 평균(平均) 106 및 $161m^2/g$으로 측정물질(測定物質)에 따라 약간의 차이(差異)가 있었으나 두방법(方法) 공히 입경(粒徑)의 대소(大小)에 따른 비표면적(比表面積)의 차이(差異)는 거의 없었다. $H_2O$ 분자경(分子徑)과 Mordenite공경(孔徑)을 근거(根據)하여 비교검토(比較檢討)한 결과측정(結果測定)된 비표면적(比表面積)은 실제표면적(實際表面積)의 일부분(一部分)으로 추정(推定)되었다. 따라서 Zeolite의 표면적(表面積)을 정확(正確)히 측정(測定)하기 위해서는 새로운 측정법(測定法)의 개발(開發) 필요성(必要性)이 인정(認定)된다.

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Preparation and Characterization of Titanium Dioxide Embedded onto ZSM-5 Zeolite

  • A. Yu. Stakheev;Lee, C. W.;Chong, P. J.
    • Bulletin of the Korean Chemical Society
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    • 제19권5호
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    • pp.530-533
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    • 1998
  • Chemical vapor deposition of $TiCl_4$ followed by the hydrolysis thereof at elevated temperatures was employed for the formation of $TiO_2$ clusters inside ZSM-5 matrix. BET and XRD revealed that the zeolite structure remains intact. XPS, Raman, FTIR, and UV-VIS reflectance spectroscopy indicated that $TiO_2$ particles thus formed are extremely small and localized inside the zeolite matrix.

바나듐 함유 MFI형 제올라이트의 제조 및 촉매적 특성 (Preparation and Catalytic Properties of Vanadium-Containing MFI Type Zeolite)

  • 김건중;고완석;조병린
    • 공업화학
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    • 제5권2호
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    • pp.361-372
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    • 1994
  • 수열합성법 및 탈알루미늄 처리 이후 $NH_4VO_3$담지법으로 바나듐이 함유된 MFI형 제올라이트를 제조하였다. X선 회절분석, 시차 열분석, 적외선 분광분석 및 전자스핀공명분석을 수행하여 바나듐의 격자구조 내로의 도입을 검토하였다. 탈알루미늄된 ZSM-5에 $NH_4VO_3$를 담지시키고 소성한 경우에도 수열합성법으로 제조한 시료와 같이 바나듐이 구조 내로 도입될 수 있었다. 제올라이트 구조 중의 바나듐은 고온처리에 의해 산화-환원과정을 거칠 수 있으며, 이들은 원자단위로 분산되어 고정됨을 나타내었다. 벤젠 수산화반응과 hexane 및 알코올의 산화반응을 바나듐 함유 MFI형 제올라이트의 특성 검토를 위한 시험반응으로 이용하였다.

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A Study on the Structure and Thermal Property of $Co^{2+}$-Exchanged Zeolite A

  • Jong-Yul Park
    • Bulletin of the Korean Chemical Society
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    • 제12권3호
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    • pp.265-270
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    • 1991
  • Theoretical calculations on the stabilization energies of framework atoms in hydrolyses Co(Ⅱ )-exchanged zeolite A were made using some potential energy functions and optimization program. The protons which are produced by hydrolysis of $[Co(H_2O)_n]^{2+}$ ion in large cavity showed a tendency to attack the framework oxygen atom O(1) preferentially, and the oxygen atom O(4) within OH- ion was coordinated at Al atom. The weakness of bonds between T(Si, Al) and oxygen by attack of proton and too large coordination number around small aluminum atom will make the framework of Co(Ⅱ)-exchanged zeolite A more unstable. The stabilization energy of $Co_4Na_4$-A framework (- 361.57 kcal/mol) was less than that of thermally stable zeolite A($Na_{12-}$A: - 419.68 kcal/mol) and greater than that of extremely unstable Ba(Ⅱ)-exchanged zeolite A($Ba_{6-}$A: - 324.01 kcal/mol). All the data of powder X-ray diffraction, infrared and Raman spectroscopy of Co(Ⅱ)-exchanged zeolite A showed the evidence of instability of its framework in agreement with the theoretical calculation. Three different groups of water molecules are found in hydrated Co(Ⅱ )-exchanged zeolite A; W(Ⅰ) group of water molecules having only hydrogen-bonds, W(Ⅱ) group water coordinated to $Na^+$ ion, ans W(Ⅲ) group water coordinated to Co(Ⅱ) ion. The averaged interaction energy of each water group shows the decreasing order of W(Ⅲ)>W(Ⅱ)>W(Ⅰ).

Studies on the Production of Artificial Zeolite from Coal Fly Ash and Its Utilization in Agro-Environment

  • Lee, Deog-Bae;Henmi, Teruo;Lee, Kyung-Bo;Kim, Jae-Duk
    • 한국환경농학회지
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    • 제19권5호
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    • pp.401-418
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    • 2000
  • 1. Production of the artificial zeolite from coal ash Coal fly ash is mainly composed of several oxides including $SiO_2$ and $Al_2O_3$ derived from inorganic compounds remained after burning. As minor components, $Fe_2O_3$ and oxides of Mg, Ca, P, Ti (trace) are also contained in the ash. These components are presented as glass form resulting from fusion in the process of the combustion of coal. In other word, coal ash may refer to a kind of aluminosilicate glass that is known to easily change to zeolite-like materials by hydrothermal reaction. Lots of hot seawater is disposing near thermal power plants after cooling turbine generator periodically. Using seawater in the hydrothermal reaction caused to produce low price artificial zeolite by reduction of sodium hydroxide consumption, heating energy and water cost. As coal ash were reacted hydrothermally, peaks of quartz and mullite in the ash were weakened and disappeared, and new Na-Pl peaks were appeared strengthily. Si-O-Si bonding of the bituminous coal ash was changed to Si-O-Al (and $Fe^{3+}$) bonding by the reaction. Therefore the produced Na-Pl type zeolite had high CEC of 276.7 $cmol^+{\cdot}kg^{-1}$ and well developed molecular sieve structure with low concentration of heavy metals. 2. Utilization of the artificial zeolite in agro-environment The artificial zeolite(1g) could remove 123.5 mg of zinc, 164.7 mg copper, 184.4 mg cadmium and 350.6 mg lead in the synthetic wastewater. The removability is higher 2.8 times in zinc, 3.3 times in copper, 4.7 times in cadmium and 4.8 times in lead than natural zeolite and charcoal powder. When the heavy metals were treated at the ratio of 150 $kg{\cdot}ha^{-1}$ to the rice plant, various growth inhibition were observed; brownish discoloration and death of leaf sheath, growth inhibition in culm length, number of panicles and grains, grain ripening and rice yield. But these growth inhibition was greatly alleviated by the application of artificial zeolite, therefore, rice yield increased $1.1{\sim}3.2$ times according to the metal kind. In addition, the concentration of heavy metals in the brown rice also lowered by $27{\sim}75%$. Artificial Granular Zeolites (AGZ) was developed for the purification of wastewater. Canon exchange capacity was 126.8 $cmol^+{\cdot}kg^{-1}$. AGZ had Na-Pl peaks mainly with some minor $C_3S$ peaks in X-ray diffractogram. In addition, AGZs had various pore structure that may be adhere the suspended solid and offer microbiological niche to decompose organic pollutants. AGZ could remove ammonium, orthophosphate and heavy metals simultaneously. Mixing ratio of artificial zeolite in AGZs was related positively with removal efficiency of $NH_4\;^+$ and negatively with that of $PO_4\;^{3-}$. Root growth of rice seedling was inhibited severely in the mine wastewater because of strong acidity and high concentration of heavy metals. As AGZ(1 kg) stayed in the wastewater(100L) for 4days, water quality turned into safely for agricultural usage and rice seedlings grew normally.

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합성조건이 제올라이트 SUZ-4의 물성에 미치는 영향 (Effect of Synthesis Conditions on Physicochemical Properties of Zeolite SUZ-4)

  • 김덕규;김영호;황영규;장종산;박상언
    • 대한화학회지
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    • 제48권6호
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    • pp.623-628
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    • 2004
  • 빠른 교반 조건에서 구조주형화합물인 TEAOH(Tetraethyl ammonium hydroxide)를 이용하여 제올라이트 SUZ-4를 성공적으로 합성하였다. 교반속도 250 rpm 이상에서 결정성의 제올라이트 SUZ-4를 얻을 수 있었다. 이것은 교반이 재현성있는 합성에 결정적인 역할을 한다는 것을 의미한다. 사용한 물의 양$(H_2O/Al_2O_3)$의 차이에 의하여 SUZ-4 결정형태 조절이 가능하였다. XRD, BET 및 암모니아 TPD에 의해 SUZ-4의 물리화학적 성질 및 증기처리에 의한 열적 안정성이 조사되었다.