본 연구는 AgX (Ag-함침 X zeolite)에 의해 고방사성해수폐액 (HSW)의 발생초기에 함유되어 있는 고방사성 요오드(131I)의 흡착, 제거를 목표로 수행하였다. AgX에 의한 I의 흡착 (AgX-I 흡착)은 AgX 내 Ag-함침농도가 증가할수록 증가하며, 함침농 도 30wt% 정도가 적당하였다. AgX (Ag-함침 약 30~35wt%)로부터 Ag의 침출농도는 해수폐액에 함유되어 있는 chloride 이 온에 의한 AgCl 침전 등으로 증류수보다 덜 침출 (<1 mg/L) 되었다. AgX-I 흡착은 초기 I 농도 0.01~10 mg/L의 경우 m/V (흡착제량/용액부피의 비)=2.5 g/L에서 99% 이상 흡착제거 되어 I의 효율적 제거가 가능함을 알 수 있다. AgX-I 흡착제거 는 해수폐액 보다는 증류수에서 수행하는 것이 효과적이고, 온도의 영향은 미미한 것 같으며, 흡착평형등온선은 Languir 보 다는 Freundlich 등온선으로 표현하는 것이 양호하였다. 한편 AgX-I 흡착속도는 유사 2차 속도식을 만족하고 있으며, 속도 상수 (k2)는 Ci 증가에 따라 감소하고 있지만, m/V 비 및 온도 증가에 따라서는 증가하고 있다. 이때 흡착 활성화에너지는 약 6.3 kJ/mol 로 AgX-I 흡착은 약한 결합형태의 물리적흡착이 지배적일 것으로 보인다. 그리고 열역학적 매개변수를 평가 (음수 값의 Gibbs 자유에너지 및 양수 값의 엔탈피)에 의해 AgX-I 흡착이 자발반응(정반응)의 흡열반응이며, 고온에서 반응 이 양호함을 나타내었다.

분리층 두께가 5 μm이며 Si/Al 몰비가 1.5인 Na형 faujasite 제올라이트 분리막을 이차성장 공정에 의하여 제조하였고, 투과부에 13X 제올라이트 흡착제 충진 전후의 진공모드에서의 CO2/N2 분리거동을 CO2/N2 몰비가 1인 혼합기체에 대하여 30℃에서 평가하였다. 충진된 13X 제올라이트 흡착제는 CO2 투과도와 CO2/N2 선택도를 동시에 증진시켰다. 이 현상은 13X 제올라이트 흡착제 충진이 다공성 α-알루미나 지지체의 기공채널을 통한 CO2 탈출을 증진시킴으로써 faujasite 제올라이트/α-알루미나 상계면에서의 CO2 탈착을 증진시켰기 때문으로 설명되었다. 본 논문으로부터 흡착제와 분리막의 혼성화는 일반적으로 보여지는 선택도와 투과도의 역비례 관계를 획기적으로 개선할 방법임이 확인되었다.

The structure of nitrogen adsorption complex of fully dehydrated Cd2+ ion exchanged zeolite-X, |Cd46(N)18|[Si100Al92O384], was determined in the cubic space group Fd3 at 21(1) ℃ [a = 24.863(4) ] by single crystal X-ray diffraction analysis. The crystal was prepared by ion exchange in a flowing steam of 0.05 M aqueous solution Cd(NO3)2 : Cd(O2CCH3)2 = 1:1 for five days, followed by dehydration at 500℃ and 2×10-6 Tor. for two days, and exposured to 100 Tor. zeolitically dry nitrogen gas at 21(1) ℃. The structure was determined in atmosphere, and was refined within F0 〉 4Σ(F0) using reflection for which the final error can appear in indices R1 = 0.097 and wR2 = 0.150. In this structure, Cd2+ ions occupied four crystallographic sites. Nine Cd2+ ions filled the octahedral site I at the centers of hexagonal prisms (Cd-O = 2.452(16) a). Eight Cd2+ ions filled site I' (Cd-O = 2.324(19) a). The remaining 29 Cd2+ ions are found at two nonequivalent sites II (in the supercages) with occupancy of 11 and 18 ions. Each of these Cd2+ ions coordinated to three framework oxygens, either at 2.159(15) or 2.147(14) a, respectively. Eighteen nitrogen molecules were adsorbed per unit cell and three per supercage.

The structure of a carbon monoxide sorption complex of dehydrated fully Ca2+-exchanged zeolite X, |Ca46(CO)27|[Si100Al92O384]-FAU, has been determined in the cubic space group Fd 3 at 21℃ (a = 24.970(4) ) by single-crystal X-ray diffraction techniques. The crystal was prepared by ion exchange in a flowing stream of 0.05 M aqueous Ca(NO3)2 for three days, followed by dehydration at 400℃ and 2×10-6 Torr for two days, and exposure to 100 Torr of zeolitically dry carbon monoxide gas at 21℃. The structure was determined in this atmosphere and was refined, using the 356 reflections for which Fo 〉 4Σ(Fo), to the final error indices R1 = 0.059 and wR2 = 0.087. In this structure, Ca2+ ions occupy three crystallographic sites. Sixteen Ca2+ ions fill the octahedral site I at the centers of hexagonal prisms (Ca-O = 2.415(7) a). The remaining 30 Ca2+ ions are found at two nonequivalent sites II (in the supercages) with occupancies of 3 and 27 ions. Each of these Ca2+ ions coordinates to three framework oxygens, either at 2.276(10) or 2.298(8) a, respectively. Twenty-seven carbon monoxide molecules have been sorbed per unit cell, three per supercage. Each coordinates to one of the latter 16 site-II Ca2+ ions: C-Ca = 2.72(8) a. The imprecisely determined N-C bond length, 1.26(14) a, differs insignificantly from that in carbon monoxide(g), 1.13 a.

In order to investigate the adsorption characteristics for Sr ion using the Na-X zeolite synthesized from coal fly ash, batch tests and response surface analyses were carried out. The adsorption kinetic data for Sr ions, using Na-X zeolite, fitted well with the pseudo-second-order model. The uptake of Sr ions followed the Langmuir isotherm model, with a maximum adsorption capacity of 196.46 mg/g. Thermodynamic studies were conducted at different reaction temperatures, with the results indicating that Sr ion adsorption by Na-X zeolite was an endothermic (ΔHo>0) and spontaneous (ΔGo<0) process. Using the response surface methodology of the Box-Behnken method, initial Sr ion concentration (X1), initial temperature (X2), and initial pH (X3) were selected as the independent variables, while the adsorption of Sr ions by Na-X zeolite was selected as the dependent variable. The experimental data fitted well with a second-order polynomial equation by multiple regression analysis. The value of the determination coefficient (R2=0.9937) and the adjusted determination coefficient (adjusted R2=0.9823) was close to 1, indicating high significance of the model. Statistical results showed the order of Sr removal based on experimental factors to be initial pH > initial concentration > temperature.

This work is to compare the experiment results by a continuous fixed-bed adsorption of water vapor, acetone vapor, and toluene vapor on zeolite 13X (SAU) and silica-alumina (SAK). SAU and SAK have very different pore structure but similar composition as inorganic adsorbent. The relationship between the equilibrium adsorption capacity and specific pore size range were studied. Adsorption of water vapor was more suitable on SAU than SAK because SAU has relatively more developed pores around 5 Å than SAK in the pore range of 10 ~ 100 Å. Adsorption of acetone vapor was more suitable on SAK than SAU because SAK has relatively more developed pores around 5~10 Å than SAK in the pore range of less than 10 Å. Adsorption of toluene vapor was more suitable on SAK than SAU because SAK has relatively more developed pores in the pore range of 10~100 Å than SAK. Adsorption capacity of the adsorbent was closely related to the surface area generated in the specific pore size region. But it was difficult to distinguish the relationships between adsorption capacity and micro area, and the external surface area of adsorbent.

리트벨트 분석법과 저온에서 측정한 방사광 가속기 분말회절 자료를 이용하여 CFC-13 (CF3Cl; chlorotrifluoromethane) 분자체가 흡착된 제올라이트 Na,K-LSX (low-silica X or synthetic faujasite)의 구조분석을 수행하였으며, supercage 내의 6-ring주변에 CFC-13 분자체의 불소 원자와 LSX 제올라이트의 나트륨 양이온 간의 결합이 일어남을 확인하였다.