Ca2＋交换的几种分子筛的氮氩分离性能

采用水溶液离子交换法制备了Ca2＋交换的4A、13X和LSX分子筛，并在25 ℃下测定了它们的静态吸附等温线和动态穿透曲线.研究发现， Ca2＋交换的4A、13X和LSX分子筛对氮的吸附性能都明显优于其相应的钠型分子筛，而它们对氩的吸附量变化不大，说明Ca2＋交换的这三种分子筛是较好的氮氩分离吸附剂.从动态吸附的结果来看，所研究的各种分子筛都有一个最优的吸附分离压力，在本论文研究的压力范围内，这个最优压力在0.6 MPa附近.由穿透曲线可推算出混合气体的吸附量，通过氮和氩在混合气体中的吸附量和相应纯气体吸附量的对比可以得出，对于氮氩吸附选择性较高的分子筛，氮的存在对氩的吸附量有较大的影响.     

Ca2+交换的几种分子筛的氮氩分离性能

采用水溶液离子交换法制备了Ca2+交换的4A,13X和LSX分子筛,并在25 ℃下测定了它们的静态吸附等温线和动态穿透曲线.研究发现, Ca2+交换的4A,13X和LSX分子筛对氮的吸附性能都明显优于其相应的钠型分子筛,而它们对氩的吸附量变化不大,说明Ca2+交换的这三种分子筛是较好的氮氩分离吸附剂.从动态吸附的结果来看,所研究的各种分子筛都有一个最优的吸附分离压力,在本论文研究的压力范围内,这个最优压力在0.6 MPa附近.由穿透曲线可推算出混合气体的吸附量,通过氮和氩在混合气体中的吸附量和相应纯气体吸附量的对比可以得出,对于氮氩吸附选择性较高的分子筛,氮的存在对氩的吸附量有较大的影响.     

不同分子筛的氮氩分离性能

采用水溶液离子交换法制备了不同离子交换的13X和4A分子筛,并在25℃下测 定了它们的静态吸附等温线和动态穿透曲线。研究发现,Ca~(2+)离子和Li~+离子 交换的13X和4A分子筛对氮的吸附性能都明显优于其相应的钠型分子筛,而它们对 氩的吸附量变化不大,说明这两种离子交换的分子筛是较好的氮氩分离吸附剂。从 动态吸附的结果来看,所研究的各种分子筛都有一个最优的吸附分离压力,在本论 文研究的压力范围内,这个最优压力在0.6MPa附近。通过穿透曲线推算出的混合气 体吸附量和纯气体吸附量的对比可以得出,对于氮氩吸附选择性较高的分子筛,氮 的存在对氩的吸附量有较大的影响。     

N2和Ar在改性的NaA分子筛上的吸附分离

采用水溶液离子交换法分别制备了不同Li^ 和Ca^2^ 交换度的A型分子筛,并在25℃下测定了各分子筛吸附剂的氮和氩的吸附等温线及穿透曲线．研究发现,锂交换和钙交换的两种分子筛的氮吸附量和氮氩分离选择性都随分子筛中阳离子交换度的增加而增大;在阳离子交换度较高时,锂离子和钙离子交换的A型分子筛的氮氩分离能力均优于NaA分子筛．穿透曲线的结果显示,所研究的各种吸附剂都存在一个最优的吸附分离压力,大约在0．6MPa．在0．6MPaT,接近100％阳离子交换度的CaNaA分子筛的动态氮氩分离性能优于相同交换度的LiNaA分子筛。     

几种二价阳离子的交换对13X分子筛氮氩分离性能的影响

采用水溶液离子交换法分别制备了不同二价阳离子(Mg²⁺、Zn²⁺和Ca²⁺)交换的13X型分子筛，并在25 ℃下测定了各分子筛吸附剂的氮和氩的吸附等温线。研究发现，13X分子筛经Mg²⁺和Zn²⁺交换后，吸附剂的吸氮能力及氮氩分离能力降低；13X分子筛经Ca²⁺交换后，吸附剂的吸氮能力及氮氩分离能力随分子筛中钙离子交换度的增加而增大。对常压氮氩分离性能较好的CaNaX系列分子     

低温变压分子筛动态分离CH_4/CO_2实验研究

在低温变压条件下测量了5A和13X沸石分子筛对CH_4/CO_2混合气体的分离能力。实验研究了CH_4/CO_2气体流量、吸附压力、填料高度和吸附温度对穿透曲线和分离能力的影响。研究结果表明,增大气体流量、增加吸附压力会降低分离效果,减小混合气体的分离系数;降低吸附温度、增加填料高度有利于CH_4/CO_2分离,提高混合气体的分离系数;在相同实验条件下,13X沸石分子筛对CH_4/CO_2混合气体吸附分离能力高于5A分子筛。     

4A沸石分子筛对氮、氧、氩的吸附分离特性

用PSA法的动态吸附装置,宏观地考察了在压力下、于NaA上氮、氧、氩单一组份的和在二元体系中的吸附分离特性,企图从这一角度解释4A沸石分子筛在PSA过程中能制取富氮气体的原因。     

氮、氩在5A^。分子筛上的低温吸附分离

测定了不同温度下氮、氩在5分子筛上的吸附等温线,其中三参数的Langmuir-Freundlich方程和Toth方程在不同温度下都能获得较好的拟合结果;计算了不同温度下氮、氩在5分子筛上吸附的亨利常数,获得了氮、氩选择性和温度的关系.测定了125K温度下氮、氩混合气体在5分子筛吸附柱上的穿透曲线.结果表明:最先流出的5L气体中含有约70%的氩,通过收集5L气体即可实现混合气体中氩的初步分离.     

氮、氩在5分子筛上的低温吸附分离

测定了不同温度下氮、氩在5分子筛上的吸附等温线,其中三参数的Langmuir-Freundlich方程和Toth方程在不同温度下都能获得较好的拟合结果;计算了不同温度下氮、氩在5分子筛上吸附的亨利常数,获得了氮、氩选择性和温度的关系。测定了125K温度下氮、氩混合气体在5分子筛吸附柱上的穿透曲线。结果表明:最先流出的5L气体中含有约70%的氩,通过收集5L气体即可实现混合气体中氩的初步分离。     

水溶液交换法制备的(Li,Na)-LSX沸石骨架中Li~+分布

采用水溶液交换法对Na-LSX沸石进行Li+交换,通过改变交换次数制备出不同交换度的低硅铝比X型[(Li,Na)-LSX]沸石分子筛,并对其进行XRD、FT-IR、TG-DSC、SEM和NMR等表征和分析,重点考察了Na-LSX分子筛在Li+交换前后的结构变化情况,以及不同交换度的(Li,Na)-LSX沸石分子筛骨架中Li+的分布。结果表明随着Li+交换度的增加,LSX分子筛的晶胞常数减小,热稳定性有所下降,Li+进入骨架中的顺序依次为S2>S3>S5。     

Hydrothermal Stability of the Novel Zeolite Type LSX in Comparison to the Traditional 13X Modification

Ion‐exchanged LSX (Si/Al = 1.02) and 13X (Si/Al = 1.18) zeolite series (Li, Na, K, Rb, Ca, Sr, Ba exchanged) were hydrothermally treated at temperatures between 423 K and 513 K in liquid water under autogeneous water vapour pressure. Beside X‐ray powder diffraction, the molybdate method and the water sorption uptake have been used to characterize the treated samples. The LSX and 13X zeolites show a similar hydrothermal behaviour in spite of their different framework Si/Al ratios depending only on the type of introduced cations. Significant destabilizing effects were observed especially in presence of K and Rb cations as well as the bivalent Sr and Ba cations. The LSX zeolites are hydrothermally more stable than LTA zeolites of same cations despite their same chemical framework composition.     

Hydrogen storage in low silica type X zeolites

Low silica type X zeolites (LSX, Si/Al = 1) fully exchanged by alkali-metal cations (Li(+), Na(+), and K(+)) were studied for their hydrogen storage capacities. Hydrogen adsorption isotherms were measured separately at 77 K and <1 atm, and at 298 K and <10 MPa. It was found that the hydrogen adsorption capacity of LSX zeolite depended strongly on the cationic radius and the density of the cations that are located on the exposed sites. The interaction energies between H(2) and the cations follow the order Li(+) > Na(+) > K(+), as predicted based on the ionic radii. Oxygen anions on zeolite framework were minor adsorption sites. Li-LSX had an H(2) capacity of 1.5 wt % at 77 K and 1 atm, and a capacity of 0.6 wt % at 298 K and 10 MPa, among the highest of known sorbents. The hydrogen capacity in LSX zeolite by bridged hydrogen spillover was also investigated. A simple and effective technique was employed to build carbon bridges between the H(2) dissociation catalyst and the zeolite to facilitate spillover of hydrogen atoms. Thus, the hydrogen storage capacity of Li-LSX zeolite was enhanced to 1.6 wt % (by a factor of 2.6) at 298 K and 10 MPa. This is by far the highest hydrogen storage capacity obtained on a zeolite material at room temperature. Furthermore, the adsorption rates were fast, and the storages were shown to be fully reversible and rechargeable. Further optimization of the bridge building technique would lead to an additional enhancement of hydrogen storage.     

自粘结低硅铝X型沸石的结构、吸附和N_2/O_2分离比

用原位合成方法直接将高岭土转化为所需形状的低硅X型沸石(PLSX),经X衍射,~(29)Si,~(27)AI MAS NMR谱证实PLSX的结构硅铝比接近1,它含LSX的组成为40.40%,含4A的组成为17.92%,其余为无定形硅、铝氧化物.LSX的骨架硅铝比接近1,是骨架负电荷分配最均匀的X型沸石,293K时静态法测定和推算ISX的饱和吸附水达39.80wt%,LSX的组成为Na(96-x)K_x(Al_(96)S_i(96)O_(384))·310H_2O,是吸附量高、价廉的吸水剂.PLSX对空气中氮氧的分离系数为α(N_2/O_2)=3.15,高于用于PSA的商品5A的α(N_2/O_2)=2.33和已报道的13X的α(N_2/O_2)=2.36.PLSX也是一种极好的吸附分离剂.     

Theoretical study of the adsorption of ethylene on alkali‐exchanged zeolites

The structures of alkali‐exchanged faujasite (X–FAU, X = Li⁺ or Na⁺ ion) and ZSM‐5 (Li–ZSM‐5) zeolites and their interactions with ethylene have been investigated by means of quantum cluster and embedded cluster approaches at the B3LYP/6‐31G(d, p) level of theory. Inclusion of the Madelung potential from the zeolite framework has a significant effect on the structure and interaction energies of the adsorption complexes and leads to differentiation of different types of zeolites (ZSM‐5 and FAU) that cannot be drawn from a typical quantum cluster model, H₃SiO(X)Al(OH)₂OSiH₃. The Li–ZSM‐5 zeolite is predicted to have a higher Lewis acidity and thus higher ethylene adsorption energy than the Li–FAU zeolites (16.4 vs. 14.4 kcal/mol), in good agreement with the known acidity trend of these two zeolites. On the other hand, the cluster models give virtually the same adsorption energies for both zeolite complexes (8.9 vs. 9.1 kcal/mol). For the larger cation‐exchanged Na–FAU complex, the adsorption energy (11.6 kcal/mol) is predicted to be lower than that of Li–FAU zeolites, which compares well with the experimental estimate of about 9.6 kcal/mol for ethylene adsorption on a less acidic Na–X zeolite. © 2003 Wiley Periodicals, Inc. Int J Quantum Chem 94: 333–340, 2003     

吸附法脱除乙烯中少量氮气的研究

采用重量法在电子天平上，研究了C2H4和N2单组分在5A、13X、丝光沸石和炭分子筛不同吸附剂上的吸附平衡性质和扩散动力学性质。单柱模拟变压吸附评价了炭分子筛吸附脱除C2H4-N2（N2为4．7％）混合组分中N2的性能，并对流速和压力的影响进行了考察。研究表明，该炭分子筛是吸附脱除C2H4中少量N2的理想吸附剂。     

High-rate and high-density gas separation adsorbents and manufacturing method

High-rate and high-density gas separation adsorbents used in vacuum pressure swing adsorption (VPSA) processes are described. Agglomerated zeolite Li–LSX compositions made using colloidal silica binding agents and having improved nitrogen pore diffusivity compared to like compositions prepared with traditional clay binders, are also described. Preparation methods for the colloidal silica-bound adsorbents are described together with their characterization by mercury (Hg) porosimetry, scanning electron microscopy (SEM) and low dead-volume breakthrough testing, from which the pore diffusivity is obtained. In this article, we show how the location and dispersion of the colloidal silica binding agent within the agglomerated zeolite particle yields pore-architectures that resemble “state-of-the-art” binderless adsorbents. In addition, we use VPSA process simulations to show that the best process performance is achieved by the combination of high-rate and high-density adsorbent properties.     

Li-LSX沸石中阳离子分布与空分性能的研究

利用静态交换与动态柱交换的方法对低硅KNaX沸石进行Li~+交换．用XRD， ICP测定样品的晶相及化学红外光谱对LSX在Li~+交换中的骨架振动进行了研究．结 果表明：在Li~+交换过程中，谱峰的位移与本身性质有关，而且与LSX骨架中的离 子位置有关．还探讨了在高交换度的Li-LSX样品上的空分性能布的关系．     

Adsorption of Nitrogen, Oxygen and Argon on Na-CeX Zeolites

Commercial type X zeolites (Linde 13X) are nitrogen selective. Oxygen is the less abundant component in air; hence oxygen selective sorbents are desired for air separation. Mixed Na-Ce type X zeolites containing different ratios of Ce³⁺/Na⁺ ions are prepared by partial ion exchange of commercial X zeolite. The adsorption isotherms of nitrogen, oxygen and argon are measured and the pure-component selectivity ratios are compared and analyzed against commercial zeolites (13X) for air separation. Oxygen selectivity over nitrogen (1.5) and argon (4.0) are seen for mixed Na-Ce type X zeolite (Si/Al = 1.25; Ce³⁺/Na⁺ < 4.0) from Henry's constant determined from low pressure adsorption measurements. The oxygen and nitrogen isotherms cross over for mixed Na-Ce type X zeolite (Si/Al = 1.25; Ce³⁺/Na⁺ < 4.0), and the pressure at which cross they over increases as Ce³⁺/Na⁺ approaches 1. The oxygen selectivity as claimed in the patent by N.V. Choudary, R.V. Jasra, and S.G.T. Bhat (US Patent no. 6,087,289, 2000) is seen only at very low pressures in the volumetric adsorption measurement and the hydrogen treatment of the Ce-exchanged samples have no effect on the adsorption characteristics.