Rare-earth-cation-exchanged Y zeolites (REHY) are important because they are fluid catalytic cracking catalysts with superior catalytic properties such as high stability and activity [1, 2, 3]. It has been reported that the stability of zeolite can be improved by the addition of RE cations, principally those from the light group (La, Ce, Nd, Sm, and Pr) [3, 4]. This effect has been attributed to the formation of hydroxy RE cationic species within zeolite channels. Another important role of RE cations is the modification of Y zeolite acidity. Richardson [5] investigated the high catalytic activity of a cation-exchanged zeolite and observed that the bond strength of Brönsted (B) OH groups was perturbed by the polarizing effect of neighboring cations. Ward [6] explained the generation of B acidity based on the dissociation of adsorbed water molecules by electrostatic fields around RE cations. It is therefore necessary to obtain detailed information on the types, strengths, concentrations, and locations of acid sites on REHY zeolites to understand the detailed reaction mechanisms and related catalytic features of the catalysts.
The acidity of REHY zeolites has been widely investigated using conventional methods such as temperature-programmed desorption (TPD), infrared spectroscopy (IR), and nuclear magnetic resonance (1H NMR) spectroscopy of adsorbed basic probe molecules [7, 8, 9]. Although these conventional methods are useful in providing qualitative and quantitative information (e.g., acid types and amounts) on acid sites, most techniques cannot provide detailed acidity information.
Recently, a novel solid-state 31P NMR technique was used for simultaneous qualitative and quantitative investigation of acidic properties using trimethylphosphine oxide (TMPO) and tributylphosphine oxide (TBPO) [10]. Unlike TBPO (kinetic diameter ca. 0.82 nm), which can only be adsorbed on the external surfaces of Y zeolite, TMPO (ca. 0.55 nm) can enter the zeolite channels, enabling simultaneous detection of internal and external acid sites. In addition, quantitative information on the acid sites (i.e., the acid concentration) can be obtained when 31P NMR experiments are performed in conjunction with elemental analysis by inductively coupled plasma-mass spectrometry (ICP-MS).
In this study, the properties of acid sites, namely their types, locations, concentrations, and strengths on a REHY zeolite, were investigated in detail using solid-state 31P magic-angle spinning (MAS) NMR spectroscopy of adsorbed TMPO and TBPO, in conjunction with elemental analysis.
The zeolite samples were prepared from a commercial NaY-type zeolite with a Si/Al ratio of 2.5 using an ion-exchange method. The NaY zeolite was converted to NH4Y with NH4Cl; NH4Y was treated in a chloride solution (RECl3, RE = La, Ce) at 90 °C for 2 h to give the NH4REY zeolite. The RE content in the zeolite was varied by changing the concentration of the chloride solution. The NH4REY zeolite was calcined at 500 °C for 5 h, thoroughly washed with demineralized water, dried overnight, and calcined at 400 °C for 2 h. The zeolite samples obtained were denoted by REHY-x, where x indicates the RE2O3 mass content (%).
All solid-state NMR experiments were carried out using a Bruker MSL-500P spectrometer at room temperature. 31P MAS NMR spectra were acquired at a Larmor frequency of 202.46 MHz using a single-pulse sequence with a pulse width of 1.8 μs, a recycle delay of 10 s, and a typical sample-spinning frequency of 12 kHz. A single-pulse sequence was also used for 27Al MAS NMR experiments, with a sample-spinning rate of 12 kHz, pulse-width of 1.0 µs, and recycling delay of 500 ms at a resonance frequency of 130.32 MHz. Aqueous 85% H3PO4 and Al(H2O)63+ solutions (1 mol/L) were used as external references for the 31P and 27Al NMR chemical shifts, respectively.
Prior to the 31P MAS NMR experiments, each sample was dehydrated at 350 °C for 24 h under vacuum (133.32 × 10−5 Pa). Details of the procedures for introducing the phosphine oxide (TMPO or TBPO) probe molecule into the sample can be found elsewhere [11]. In brief, a known amount of TMPO (100%, Alfa) or TBPO (98%, Acros) dissolved in anhydrous CH2Cl2 was added (using a gas-tight syringe) in a N2 glove box to a vessel containing a dehydrated sample; the loaded sample was agitated in an ultrasonic shaker for 30 min for thorough mixing, and then the CH2Cl2 solvent was removed by extraction (under liquid N2) and then evacuation for 12 h. To ensure uniform adsorption of the probe molecules on the sample, the sealed sample vessel was subjected to thermal treatment at 140 °C for 1 h. Finally, the sample vessel was placed in the N2 glove box, where the sample was transferred into a ZrO2 MAS rotor (4 mm o.d.), which was sealed with a gas-tight Kel-F cap.
For quantitative determination of the acid sites, each adsorbate-loaded sample was subjected to elemental analysis using ICP-MS (Jarrell-Ash, ICAP 9000). Typically, the adsorbate-loaded sample (ca. 0.1 g) was dissolved in a mixture of HF, HNO3, and HCl (10 mL), and the solution was added to a saturated boric acid solution (60 mL) at room temperature. The amounts of P, Al, and Si were then determined using the respective commercial standards.
Adsorbed pyridine Fourier transform infrared spectroscopy (Py-IR) was also used to determine the acidity. Prior to each Py-IR experiment (Thermo Nicolet NEXUS 750), a compressed sample (in the form of a self-supporting wafer, ca. 6 mg/cm2) was placed in the IR cell (with ZnSe windows) and evacuated at 450 °C for 2 h, followed by saturation adsorption of pyridine at room temperature and subsequent removal of the physisorbed pyridine under vacuum. Pyridine desorption took place at 200 °C. Each Py-IR spectrum was acquired by scanning from 4000 to 900 cm−1. The numbers of Brönsted (B) acid sites and Lewis (L) acid sites were determined from the IR absorption bands of pyridine at 1545 and 1450 cm−1, respectively [12].
The crystallinity of the zeolite samples was determined using a Philips X'Pert X-ray diffractometer with copper Kα radiation. Nitrogen physisorption measurements were performed at liquid-nitrogen temperature with a Micrometritics ASAP 2405N V1.01 apparatus. The surface area was determined by the BET method, and the micropore volum was determined from the intercept of the liner part of the t-plot.
The structural features of the samples were determined using powder X-ray diffraction (XRD). The crystallinity, cell parameter α0, molar Si/Al ratio, BET surface area, and pore volume were determined using XRD, 29Si MAS NMR spectroscopy, and N2 adsorption/desorption measurements. The characteristics of these samples are listed in Table 1.
The 31P MAS NMR spectra of TMPO and TBPO adsorbed on REHY-8 are shown in Figure 1. The 31P NMR spectra of the REHY zeolite samples with various RE contents were similar, so REHY-8 was taken as an example. The dashed curves represent the results of spectral simulation by Gaussian deconvolution. A Win-NMR software program (Bruker Biospin) enabled curve fitting through appropriate choice of 31P NMR peaks, based on the observed resonance line-shape. A simulated spectrum nearly identical to the observed spectrum was considered to be a good fit. The simulation results for REHY-8/TMPO had nine resonance peaks at δ = 78, 70, 65, 62, 58, 55, 53, 49, and 41. The two peaks at δ < 50 can be unambiguously assigned to physisorbed TMPO and are therefore irrelevant in terms of the acidic properties of the sample being examined [13]. The assignments of the peaks at higher chemical shifts remains controversial; for example, Zhao et al. [14] concluded that the 31P resonances at δ = 60-65 were associated with TMPO adsorbed on L acid sites, whereas Mueller's group [15] suggested that the peak at δ = 63 arose from interactions between TMPO and B acid sites.
Additional experiments were performed to confirm the resonance assignments. The TMPO-loaded sample was exposed to humidity, and the specific chemical shifts and corresponding integrated areas in each spectrum are given in Figure 2(a) and Table 2. It is known that L acid sites can react easily with water to form B acid sites [16]. However, the strong hydrogen bonds between the adsorbed TMPO molecules and B acid sites are unlikely to be dissociated in the presence of water. Consequently, only the 31P resonances associated with L acid sites will decrease when the sample is hydrated. The data in Table 2 and Figure 2 show that the peaks at δ = 78 and 55 can be ascribed to interactions of TMPO with L acid sites, and the peaks at δ = 70, 65, 62, 58, and 53 can be ascribed to interactions of TMPO with B acid sites.
In the case of adsorbed TBPO, only three peaks were observed for REHY-8/TBPO at δ = 86, 76, and 50 (Figure 1). The resonance with the lowest chemical shift (δ = 50) can be assigned to physisorbed TBPO. On exposure of the adsorbate sample to humidity, the peak intensity at δ = 86 decreased, and that of the peak at δ = 76 increased, with increasing water content (see Figure 2(b) and Table 3). The peaks at δ = 86 and 76 were therefore associated with L acid sites and B acid sites, respectively.
31P NMR results obtained for TMPO adsorbed on REHY zeolite provide information on both internal and external acid sites, whereas TBPO systems exclusively provided information on acid sites located on the external surface [11]. Before performing further experiments, it was therefore necessary to clarify the distributions and locations of the acid sites. It was important to combine the results obtained separately using the homologous probe molecules, TMPO and TBPO, to identify the internal and external acid sites.
An earlier study [16] showed that the respective 31P resonances observed for TMPO and TBPO adsorbed on acid sites with the same acid strength can be correlated based on the differences (∆δ ± 3) between the observed chemical shifts and those of their crystalline bulks, namely δ = 39 for TMPO and δ = 47 for TBPO. For example, for REHY-8, up to seven peaks can be resolved from the 31P NMR of adsorbed TMPO, at δ = 78, 70, 65, 62, 58, 55, and 53 (in order of decreasing acid strength), whereas only two resonances can be identified in the case of adsorbed TBPO (i.e., δ = 86 and 76). The resonances at δ = 86 and 76, with respective ∆δ values of 39 and 29, can therefore be correlated with the resonances at δ = 78 and 70, obtained from TMPO, which were found to have similar respective ∆δ values. It can therefore be concluded that the peaks at δ = 78 and 70 observed for the REHY-8/TMPO system represented internal and external acid sites. Furthermore, for the same system (REHY-8/TMPO), the other peaks at δ = 65, 62, 58, 55, and 53, which corresponded to respective ∆δ values of 26, 23, 19, 16, and 14, were not visible in the spectrum obtained from REHY-8/TBPO. These peaks can therefore be attributed to TMPO adsorbed on acid sites located in the internal channels of the REHY-8 sample.
Figure 3 shows the 31P MAS NMR spectra of TMPO and TBPO adsorbed on REHY zeolite. It was found that no new resonance peaks emerged as the RE content of the Y zeolite increased. However, the relative concentrations of acid sites with the same acid strength clearly changed.
To clarify the effects of RE cations on Y zeolite acidity further, additional quantitative information on the acid sites is needed; this can be obtained from ICP-MS analysis for Si, Al, and P; the results are listed in Tables 4 and 5. The amounts (mmol/g) of B acid and L acid sites can then be derived using the renormalized (i.e., after excluding contributions from physisorbed TMPO or TBPO) relative concentrations obtained from spectral simulation by Gaussian deconvolution, based on the assumption that each TMPO or TBPO molecule can only be adsorbed on either one B or L acid site [14], i.e., TMPO or TBPO was adsorbed on the acid sites on a 1:1 basis.
The conclusions drawn from a comparison of the results shown in Table 4 are summarized below and are clearly shown in Table 6.
In terms of the overall (internal and external) acidity, the total number of acid sites on REHY zeolite decreased with increasing RE2O3 content; for example, the number of acid sites on REHY-4, REHY-8, REHY-14, and REHY-28 were 2.09, 2.04, 1.93, and 0.99 mmol/g, respectively. In particular, the number of L acid sites decreased significantly when the RE2O3 content was increased from 4% to 28%, but a large decrease in the number of B acid sites was only observed when the RE2O3 content was very high (28%). The ratio of B to L acid sites therefore increased on incorporation of RE into Y zeolite.
In terms of acid strength, when the RE2O3 content was 14% or less, the incorporation of RE into the Y zeolite resulted in a clear increase in the number of medium strength (δ = 62 and 58) B acid sites, and significant decreases in the numbers of weak (δ = 55) L acid sites and strong (δ = 65) B acid sites. When the content of RE2O3 was very high (28%), the number of B acid sites decreased greatly.
In terms of the distribution of acid sites, the acid sites (B and L) were mainly located inside the Y zeolite cages, i.e., internal acid sites, and these consisted of B acid sites of various strength and weak L acid sites; only 5%-10% of the total acidity was contributed by acid sites located on the external surfaces of the Y zeolite.
To confirm the results from 31P MAS NMR, Py-IR was used to characterize the acidic properties of various samples. Py-IR is a useful technique and is commonly used for the identification of B acid and L acid sites. The adsorbed pyridine probe molecules couple with L acid and/or B acid sites through the nitrogen lone-pair electrons and can therefore be monitored using their ring vibrations. The numbers and distributions of acid sites (B and L) determined from IR spectra after the adsorption and desorption of pyridine at 200 °C are shown in Figure 4. In general, the total number of acid sites, particularly L acid sites, decreased with increasing RE2O3 content. The number of B acid sites did not change significantly when the RE2O3 content increased from 4% to 14%, but decreased greatly when the RE2O3 content was about 28%. These results were mostly in agreement with those obtained using 31P MAS NMR. However, acidity characterization using Py-IR was limited because it cannot provide information on the distributions of sites with different acid strengths and the locations of acid sites. In contrast, the combination of 31P MAS NMR and ICP-MS used in this study enabled detailed qualitative and quantitative information on acid sites to be obtained simultaneously, and also enabled monitoring of changes in the strengths and concentrations of acid sites on the samples.
The XRD and 29Si MAS NMR results show that the unit cell size (α0) increased with increasing RE content, as did the number of framework Al atoms; this indicates that the introduction of RE cations prevented shrinkage of the unit cell and formation of extra-framework Al. Previous theoretical research [17] showed, using density functional theory, that the RE species and Y zeolite clusters interact strongly, and this strengthens the interactions between framework Al and neighboring O atoms, inhibits framework dealumination and formation of extra-framework Al, and significantly enhances the Y zeolite stability.
The influences of framework and extra-framework Al species and RE cations on the Y zeolite acidity can be explained by the following model (Figure 5). (1) When the REHY zeolite is prepared from NaY using an ion-exchange method, the polarization effect of RE3+ on water results in the formation of RE(OH)2+ [18]. Under heat treatment conditions, RE(OH)2+ can move from the supercage to the sodalite cage I' sites of the Y zeolite, and then bond strongly with O3 and O2, leading to enhanced stability of the Y zeolite [17]. (2) With regard to B acid strength, it is accepted that heat treatment can cause the release of Al atoms from the Y zeolite framework, leading to the formation of extra-framework Al species. It has been shown that a decrease in the framework Al content [19] and the presence of extra-framework Al species [20] both lead to formation of strong B acid sites on dealuminated HY (USY) zeolite. The enhanced stability of the REHY zeolite suppresses the release of framework Al and the formation of extra-framework Al, leading to weaker B acid sites on REHY zeolite than on USY zeolite. RE(OH)2+ species located in the sodalite cage I' sites of Y zeolite result in stronger B acid sites on REHY zeolite than on HY zeolite. The order of the B acid site strength is therefore USY > REHY> HY. (3) In terms of the number of B acid sites, the HY zeolite, which is prepared from NaY by NH4+ exchange with Na+ and NH3 release, has the most B acid sites. The USY zeolite, which is obtained by dealumination of HY under heat treatment conditions, has the fewest B acid sites. REHY zeolites are obtained from NaY by RE(OH)2+ exchange with two Na+ ions in the sodalite cage, followed by NH4+ exchange with the remaining Na+; H+ is produced by hydrolysis exchange with Na+ in the supercage, so REHY zeolites have fewer B acid sites tha n HY zeolite [21]. The higher stability of REHY zeolite compared with HY zeolite suppresses zeolite dealumination, so REHY zeolite has larger numbers of B acid sites than USY zeolite. The order of the numbers of B acid sites is therefore HY > REHY > USY.
The number of medium strength B acid sites (with 31P NMR/TMPO at δ = 62 and 58) increases significantly with increasing RE content, whereas the numbers of strong B acid sites (with 31P NMR/TMPO at δ = 65) and weak L acid sites both decrease.
The acidic properties (i.e., types, locations, concentrations, and strengths of acid sites) of REHY zeolite were characterized using solid-state 31P MAS NMR of adsorbed phosphine oxide probe molecules (TMPO and TBPO). In particular, the distributions and concentrations of internal and external acid sites were differentiated using a combination of elemental analysis and 31P MAS NMR of adsorbed phosphorus probe molecules. Five B acid sites and two L acid sites of various acid strengths were identified for Y zeolite. Among these, four of the five B acid sites, with different acid strengths, and one of the L acid sites, which was weak, were found to be internal sites, and one B acid site and one L acid site were associated with external sites. The concentration of internal B acid sites of medium strength increased significantly with increasing RE2O3 content, and that of L acid sites decreased accordingly, when the RE2O3 content was 14% or less. The total number of acid sites on the REHY zeolite, especially the number of L acid sites, decreased with increasing RE2O3 content.
稀土改性Y型分子筛作为催化裂化催化剂的活性组分具有较高的活性和稳定性[1, 2, 3]. 普遍认为, 稀土(La, Ce, Nd, Sm, Pr)离子可通过表面修饰进入分子筛晶体内部, 增强了分子筛骨架结构的稳定性[3, 4]. 稀土离子的另一个重要作用是调变分子筛酸性, Richardson[5]阐述了稀土离子交换Y分子筛的高稳定性, 认为稀土离子的极化作用影响了Brönsted (B) OH的强度. Ward[6]认为稀土离子的高电价使水分子极化, 释放出氢质子, 从而提高了分子筛的酸性. 因此, 详细研究稀土改型Y分子筛的酸性(种类、数量、强度以及酸中心分布等)对于提高催化剂性能和指导合成新型催化剂具有重要意义.
虽然关于稀土改性Y型分子筛的酸性已有大量的研究, 但这些研究大多采用传统的酸性表征方法[7, 8, 9], 如程序升温脱附(TPD)、红外光谱(IR)以及1H核磁共振(1H NMR). 而这些传统的酸性表征方法都无法给出酸性的详细信息(如酸种类、酸数量、酸强度和不同强度酸中心的分布等).
近年来, 固体核磁共振技术在酸性表征方面得到应用[10], 结合探针分子的31P魔角旋转共振(31P MAS NMR)技术能够分析固体酸催化剂的酸类型、酸强度、酸量和酸位分布, 常用的探针分子有三甲基磷氧(TMPO)和三丁基磷氧化合物(TBPO). TMPO的分子直径约为0.55 nm, 能进入分子筛内部, 因此可探测分子筛内外表面的酸性; TBPO的分子直径约为0.82 nm, 无法进入分子筛内部, 只能测得分子筛外部的酸量. 另外, 结合ICP-MS元素分析可以给出酸中心的定量信息.
为了深入理解稀土改性Y型分子筛的酸性, 本文采用结合探针分子的31P MAS NMR技术, 对分子筛酸中心的数量、强度以及酸中心分布等进行了详细分析.
稀土改性Y分子筛采用离子交换法制备. 首先将NaY分子筛(Si/Al = 2.5)用NH4Cl交换得到NH4Y, 然后用不同浓度的RECl3 (RE = La, Ce)溶液在90 °C交换2 h得到NH4REY, 于500 °C焙烧5 h. 所得样品用去离子水洗涤, 干燥, 400 °C焙烧2 h, 得到稀土改性的Y分子筛样品, 记为REHY-x, 其中x代表RE2O3的质量分数(但不是其准确数值).
固体NMR实验于室温在Bruker MSL-500P仪器上进行. 31P MAS NMR采用4 mm双共振魔角旋转探头, 共振频率202.46 MHz, 单脉冲程序, 脉冲间延迟10 s, 脉冲宽度1.8 μs, 在12 kHz高速旋转下采集样品31P MAS NMR谱. 27Al MAS NMR实验共振频率为130.32 MHz, 脉冲间延迟500 ms, 脉冲宽度1.0 μs, 在12 kHz高速旋转下采集样品谱图. 为了得到良好的谱图信号比, 重复累加多次扫描, 以85% H3PO4水溶液作为化学位移参考点(δ = 0).
进行31P MAS NMR实验前, 样品需经预处理[11]. 首先在高真空状态(133.32 × 10−5 Pa) 350 °C下加热脱水处理24 h, 然后置于氮气袋中冷却至室温; 为了吸附磷氧化物, 在氮气袋中将一定量的磷氧化合物(TMPO或TBPO)溶解在无水的二氯甲烷溶液中, 透过密闭性注射器转移到除水后的样品中; 将上述步骤处理后的混合物置于超声波振荡槽中振荡30 min, 以确保系统达到均匀饱和吸附; 之后采用液态氮重复冷凝-抽除法, 将多余的二氯甲烷溶液除去, 再将样品加热至140 °C维持1 h, 使磷氧化合物分子充分扩散到分子筛样品孔洞中; 最后于氮气袋中, 将样品转移到ZrO2 MAS NMR转子中, 并 用Kel-F盖子紧密地封口, 进行31P MAS NMR实验.
为了确定样品中探针分子在酸性位上的吸附量, 本实验采用ICP(Jarrell-Ash, ICAP 9000)元素分析方法进行测定. 将大约0.1 g的已吸附探针分子样品, 溶解在10 mL含HF, NH3和HCl的混合溶液中, 然后将60 mL硼酸饱和溶液于室温下加入上述混合溶液中, 此混合溶液使用PET塑料瓶盛装避免外露, 由各自商业化标准测定样品中Si, Al和P含量.
吡啶-红外光谱(Py-IR)分析[12]利用Thermo Nicolet NEXUS 750型FT-IR仪测定样品的表面酸性, 将样品采用自支撑片法在1.5−2.0 MPa压力下压制成直径15 mm的圆形均匀薄片, 放置于石英原位池中, 加热到450 °C, 并抽真空到10−3 Pa下净化2 h. 将样品降至90 °C, 饱和吸附吡啶20 min. 然后程序升温, 分别在200和350 °C下高真空脱附20 min, 测定各温度点的红外吸附光谱, 波数范围4000−900 cm−1.
采用PHILIPS公司的X’Pert型X射线粉末衍射仪表征样品的晶体结构. 采用美国Micromeritics公司ASAP 2405N V1.01型自动吸附仪, 低温静态氮吸附容量法, 在−195.6 °C下测定样品的吸附-脱附等温线. 根据BET公式计算样品的比表面(SBET), 测定相对压力p/p0 = 0.98时样品吸附N2的体积, 将其换算为液氮体积, 即总孔体积. 根据t-plot法计算微孔表面积(SMicro)和微孔体积(VMicro).
图1为REHY-8样品分别吸附TMPO和TBPO探针分子的31P MAS NMR谱图. 由于各稀土改性Y分子筛样品的31P MAS NMR谱图相似, 本文以REHY-8样品为例进行谱图解析. 图中虚线为高斯线型模拟方法对重叠谱线进行分峰拟合的结果, 在谱峰形状的基础上, 采用Win-NMR软件程序(Bruker Biospin)进行分峰拟合, 使拟合光谱与实际观测光谱尽可能重合. 从图1可以看出, REHY-8/TMPO样品在δ = 78, 70, 65, 62, 58, 55, 53, 49和41处存在共振谱线, δ = 49和41处特征峰为物理吸附在分子筛表面的TMPO分子[13], 其它共振峰为TMPO吸附在不同酸性位的共振谱线. Zhao等[14]总结了TMPO在各种常见固体酸上的31P化学位移值, 吸附在L酸上的δ = 60−65. 而Mueller课题组等[15]将δ = 63处峰归属为TMPO吸附在分子筛B酸位上的信号.
为了进一步区分B酸中心和Lewis (L)酸中心, 本文将REHY-8/TMPO样品置于盛有饱和NaCl水溶液的密闭容器中, 进行不同时间的吸水实验, 所得样品的31P MAS NMR谱图和数据分别列于图2(a)和表2. 通常认为, L酸中心容易与水分子作用生成B酸中心[16]; 而B酸中心与TMPO分子之间存在较强的氢键作用, 在水分子作用下很难水解, 因此只有与L酸相关的31P谱峰随着水合时间的增长会显著减弱. 结合上述分析可见, δ = 55处谱峰由于随着吸水时间的增长而显著降低, δ = 78处谱峰随 着吸水时间增长也略有降低, 所以将δ = 55和78处谱峰归属于L酸中心与TMPO的作用, 而δ = 70, 65, 62, 58和53处谱峰归属于B酸中心与TMPO的作用.
当REHY-8样品吸附TBPO后, 其31P MAS NMR谱图在δ = 50, 76和86处存在3个明显的谱峰(图1), δ = 50处吸收峰为物理吸附在Y型分子筛表面的TBPO分子, 也可能含有部分结晶状TBPO吸收峰(δ = 47), δ = 76和86处吸收峰归属于TBPO分子吸附在样品不同酸性位的谱峰. 为了进一步确认TBPO探针分子与分子筛外表面B酸或L酸相互作用的化学位移, 本文将吸附TBPO分子的REHY-8样品进行不同时间的水合实验, 结果见图2(b)和表3. 可以看出, δ = 86处谱峰随着吸水时间的延长逐渐减弱, δ = 76处谱峰的相对含量没有降低, 反而略有增加. 由于L酸中心会和水生成B酸中心, 所以本文将δ = 86处谱峰归属于TBPO和L酸中心的相互作用, 而δ = 76处谱峰归属于TBPO与B酸中心的相互作用.
TMPO分子检测的是分子筛内部和外部酸中心的总和, 而TBPO只能检测分子筛外部酸中心, 二者的关联可以识别分子筛内部和外部酸中心的位置、强度、分布及数量[11].
已有研究表明, 相对于结晶分子特征峰的化学位移, 尽管所吸附的探针分子不同, 但在同一酸性中心上, 其特征峰位移的改变程度基本相同(∆δ ± 3)[16]: 即以结晶状TMPO (δ = 39)和TBPO (δ = 47)的化学位移作为参考, 化学位移差(Δδ)接近的谱峰反映了同一类型的酸位, 即具有相似的酸强度. 可以推断, REHY-8/TBPO中δ = 86和76处特征峰分别对应于REHY-8/TMPO中δ = 78和70处特征峰, 由于REHY-8/TBPO中特征峰对应分子筛外部酸中心, 所以REHY-8/TMPO中δ = 78和70处特征峰含有一部分外表面酸性中心, 酸性强, 可能位于分子筛孔口处, 因为此处结构的不规则或缺陷而存在一些静电作用. 同样, REHY-8/TMPO中δ = 65, 62, 58, 55和53处特征峰的∆δ值分别为26, 23, 19, 16和14, 在REHY-8/TBPO谱图中未发现, 所以这些特征峰归属于分子筛内部酸中心, 其中δ = 65, 62, 58和53处谱峰为分子筛内部B酸中心, δ = 55处谱峰为分子筛内部L酸中心.
图3给出了稀土改性Y分子筛分别吸附TMPO和TBPO探针分子的31P MAS NMR谱图. 可以看出, 随着稀土含量的增加, REHY分子筛吸附探针分子后的谱图相似, 没有出现新的特征峰, 但相同位移处谱峰的面积发生了变化(表4和表5).
分子筛酸性的定量信息需要配合ICP实验分析, 获得分子筛的总酸量(一个酸中心吸附一个TMPO分子), 再利用高斯拟合后的谱图计算各个峰面积, 可得每个峰的面积百分比(与酸中心相关的峰面积之和为100%), 将分子筛上的总酸量与每个峰的面积百分数相乘, 即得酸中心含量. 表4为REHY分子筛31P NMR/TMPO谱图各化学位移归属及酸中心分布数据, 表6为改性Y分子筛酸中心分布图.
随着稀土含量的增加, 分子筛的总酸量呈下降趋势, 当稀土含量较高时, 总酸量下降更显著. 例如, REHY-4, REHY-8, REHY-14和REHY-28的总酸量分别为2.09, 2.04, 1.93和0.99 mmol/g. 其中L酸中心数量随着稀土含量增加一直减少; 而B酸中心数量的变化不象L酸那样显著, 只有当稀土含量较高时B酸中心含量才显著降低.
酸强度分布方面, 当稀土含量低于14%时, 稀土有利于中等强度B酸中心(吸附TMPO时δ = 62和58)数量显著增加, 较弱L酸中心数量(吸附TMPO时δ = 55)显著下降, 强B酸中心(吸附TMPO时δ = 65)数量减少; 当稀土含量较高时(如REHY-28), B酸中心的数量显著减少.
酸位置分布方面, 分子筛外表面酸中心仅占分子筛总酸量的5%−10%, 且主要由强酸组成; 分子筛酸中心主要存在于分子筛孔洞内, 约占总酸量的90%以上, 且酸强度分布范围较广(从强酸到弱酸都有).
本文还利用吡啶吸附红外光谱(Py-IR)方法对分子筛酸中心种类及数量进行了表征. 吡啶是检测固体样品酸类型比较合适的探针分子, 易与B酸作用生成PyH+, 其C−C (N)键伸缩振动的红外特征吸收峰出现在1540 cm−1附近, 同时Py还可与L酸发生配位生成Py-L, 在1450 cm-1附近出现C−C (N)键伸缩振动吸收峰. 对于Y型分子筛而言, 由于Py的动力学直径较大, 只能进入分子筛大笼与羟基发生作用, 而不能进入较小的笼与羟基发生作用, 因此Py-IR法测得的酸性主要是Y型分子筛外表面和超笼中的酸性.
图4给出了分子筛酸量随稀土含量的变化趋势. 可以看出, 在总酸量方面, 随着稀土含量的增加, 分子筛的总酸量下降, 尤其是L酸中心数量随着稀土含量增加一直减少, 而B酸中心的数量只有当稀土含量较高时才显著降低. 这与探针分子的31P NMR分析结果一致. 然而, Py-IR分析不能给出不同强度酸中心的分布以及位置等详细信息, 存在一定的局限性.
通过XRD及29Si MAS NMR分析发现, 随着稀土含量增加, 分子筛晶胞常数增大, 骨架Si/Al比降低, 骨架Al数量增加, 表明稀土的引入能显著抑制分子筛晶胞常数收缩, 避免骨架铝脱除. 以前的研究借助于量子力学密度泛函理论进行了计算, 进入分子筛β笼中的稀土离子与分子筛骨架O2和O3原子较好地配位成键, 增加了骨架铝原子的稳定性, 抑制了非骨架铝物种的形成[17].
结合骨架Al、非骨架Al以及稀土离子对分子筛酸性的影性, 建立了以下机理模型(图5). (1) 采用液相离子交换法制备稀土改性Y型分子筛时, RE3+对其周围的H2O产生极化和诱导作用, 有效吸引H2O中OH-生成RE(OH)2+ [18], 在热处理条件下, RE(OH)2+可以由分子筛超笼迁移进β笼I'位; 进入分子筛β笼I'位的RE(OH)2+与O2和O3相互作用, 增强了Al-O作用力, 稳定了分子筛骨架结构, 提高了分子筛的水热稳定性. (2) 在酸中心强度方面, 在热或水热处理条件下, 分子筛骨架Al易脱除生成非骨架Al物种, 非骨架Al物种的生成和骨架Al数目的减少导致脱铝后Y分子筛(USY分子筛)的B酸强度显著增大[19, 20]; 由于以RE(OH)2+形式进入分子筛β笼I'位的稀土离子稳定了分子筛骨架结构, 抑制了骨架Al的脱除, 减少了非骨架Al物种的生成, 所以稀土改性Y型分子筛的B酸强度低于USY分子筛的; 同时, 稀土离子与分子筛骨架O2和O3的相互作用, 使分子筛骨架O1负电荷减弱, Al-O1键长变短, H+释放能力增强, 所以与HY分子筛相比, 稀土改性Y型分子筛的B酸强度增加, 即分子筛B酸中心强度顺序如下: USY > REHY > HY. (3) 在酸中心数量方面, 通过NH4+交换NaY中1个Na+并脱除NH3后生成的HY分子筛具有较多的B酸中心, 经过热或水热处理后生成USY分子筛, 骨架Al的脱除导致USY分子筛具有较少的B酸中心数量; 对于稀土改性Y型分子筛, RE3+水解产生的RE(OH)2+可以进入NaY分子筛β笼交换2个Na+, 同时水解产生的H+交换超笼中1个Na+, 进一步经过NH4+交换和脱除NH3后生成REHY分子筛, 所以REHY分子筛的B酸中心数量比HY分子筛的少[21]; 又由于β笼中RE(OH)2+对分子筛骨架结构的稳定作用, 避免了骨架Al的脱除, 所以REHY分子筛的B酸中心数量比USY分子筛的多, 即分子筛B酸中心数量顺序如下: HY > REHY > USY.
因此, 随着稀土含量的增加, 分子筛强B酸中心和较弱L酸中心的数量显著降低, 而中等强度B酸中心数量显著增加.
分别以TMPO和TBPO为探针分子的31P MAS NMR实验配合ICP元素分析探测了稀土改性Y型分子筛的酸性. 结果表明, Y型分子筛存在5种B酸中心和2种L酸中心, 其中4种强度不同的B酸中心和1种较弱的L酸中心位于分子筛内表面, 分子筛外表面存在2种较强的酸中心. 随着稀土含量的增加, Y型分子筛中的强B酸中心和较弱L酸中心数量显著降低, 而中等强度B酸中心数量显著增加, 当稀土含量过高时, 分子筛的总酸量显著降低.Q 97; 与传统酸性表征方法相比, 结合多种探针分子的固体核磁共振技术更能全面认识分子筛的酸性, 即酸类型、酸强度、酸量以及酸位分布.
致谢 本工作主要在台湾“中央”研究院原子与分子科学研究所完成, 得到刘尚斌教授的大量指导, 在此表示诚挚的感谢.