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Silicoaluminophosphate (SAPO) molecular sieves—particularly the SAPO‑34, SAPO‑11, and SAPO‑5 frameworks—are critical materials for the selective catalytic reduction of NOx, methanol‑to‑olefin (MTO) conversion, and novel gas separation processes. Their performance is exquisitely sensitive to framework Si distribution, crystallite size, acidity type and strength, pore architecture, and the nature of extra‑framework species. Clients seeking testing for SAPO materials are typically confronted with challenges in optimising synthesis protocols, distinguishing between framework and extra‑framework aluminium/phosphorus species, controlling Si enrichment in specific crystallographic sites, and correlating acidity with catalytic selectivity. Our laboratory has established a fully integrated, multi‑technique analytical platform that combines solid‑state NMR, high‑resolution X‑ray diffraction, electron microscopy, temperature‑programmed desorption, and advanced spectroscopic methods, delivering a quantitative, structure‑property‑performance fingerprint that enables precise tuning of synthesis parameters, rigorous quality assurance, and reliable performance prediction for industrial applications.

The location and concentration of silicon in the aluminophosphate framework directly determine the Brønsted acidity and shape‑selectivity of SAPO materials. We employ multi‑nuclear solid‑state magic‑angle spinning (MAS) NMR at high magnetic fields (≥14.1 T) to acquire 29Si, 27Al, and 31P MAS NMR spectra with spinning rates up to 15 kHz. For 29Si MAS NMR, we use single‑pulse excitation with high‑power proton decoupling to resolve the characteristic signals corresponding to Si(0Al), Si(1Al), Si(2Al), Si(3Al), and Si(4Al) environments, enabling the quantification of silicon islands, isolated Si domains, and Si‐Al ordering with a spectral resolution of < 0.5 ppm and an accuracy of ±2% for each local environment. 27Al MAS NMR at multiple flip angles (π/12, π/6, and π/2 pulses) is performed to differentiate tetrahedral (AlIV), penta‑coordinated (AlV), and octahedral (AlVI) aluminium species, providing the framework Al content and the fraction of extra‑framework aluminium with a precision of ±1%. 31P MAS NMR identifies phosphorus environments (P(OAl)4 and P(OAl)3(OSi) etc.) and reveals the degree of Si incorporation into the phosphate network. We also perform 1H‑29Si heteronuclear correlation (HETCOR) NMR to directly link silanol groups and bridging hydroxyls (Si‑OH‑Al) with specific silicon sites, providing definitive evidence of acid site genesis. All NMR data are processed with deconvolution and fitting routines that account for overlapping resonances, and the results are cross‑validated with XRF and ICP‑MS for bulk elemental ratios.
The integrity of the SAPO framework and the absence of competing phases (e.g., AlPO₄, dense silica, or quartz) are critical. We use high‑resolution powder X‑ray diffraction (HR‑XRD) with a synchrotron source (λ = 0.8–1.2 Å) or a high‑performance benchtop diffractometer (Cu Kα, λ = 1.5406 Å) with a step size of 0.005° 2θ. Rietveld refinement is performed to determine unit cell parameters (±0.0003 Å), crystallite size (via Scherrer and Williamson‑Hall analysis), and microstrain. We also quantify phase purity by detecting any impurity peaks down to 0.5 wt%. For intergrowth or stacking fault detection (common in SAPO‑34), we use DIFFaX modelling to simulate the diffraction pattern and to estimate the stacking disorder probability. To assess the long‑range order, we measure the crystallinity index (based on the integrated intensity of characteristic peaks relative to a highly crystalline reference) with repeatability < 0.5%. In addition, we perform in situ XRD at elevated temperatures (up to 600 °C) and under controlled humidity to evaluate framework stability and structural changes upon calcination or hydration, which are essential for predicting catalyst lifetime.
The catalytic performance of SAPO materials is governed by the number, strength, and nature (Brønsted vs. Lewis) of acid sites. We employ a combination of temperature‑programmed desorption (TPD) of ammonia (NH₃‑TPD) using a mass spectrometer or thermal conductivity detector, with a heating rate of 10 °C/min from 100 °C to 800 °C, to quantify total acidity (mmol NH₃/g) and to distinguish weak, medium, and strong acid sites based on desorption temperature ranges (e.g., 150–250 °C, 250–400 °C, >400 °C). For site‑specific characterisation, we use pyridine adsorption followed by FTIR spectroscopy (Py‑FTIR) in transmission mode, using self‑supported wafers and in situ evacuation at increasing temperatures (150 °C, 300 °C, 450 °C). The Brønsted (1545 cm⁻¹) and Lewis (1450 cm⁻¹) band intensities are measured with a resolution of 2 cm⁻¹, and the ratio of Brønsted to Lewis acid sites (B/L) is calculated with a precision of ±0.05. We further perform 1H MAS NMR to directly observe bridging hydroxyl protons (δ = 3.5–4.5 ppm), and we use deuterated acetonitrile (CD₃CN) as a probe molecule to differentiate hydrogen‑bonding interactions. For a more detailed acidity map, we apply 2D 1H‑27Al heteronuclear multiple‑quantum correlation (HMQC) NMR to correlate acid protons with specific aluminium sites.
The accessible pore volume and molecular sieving effect are fundamental to separation and shape‑selective catalysis. We measure argon (or nitrogen) physisorption at 87 K (or 77 K) over a relative pressure range from 10⁻⁶ to 0.995 using a high‑accuracy volumetric analyser. The data are reduced by BET theory for specific surface area (with reproducibility < 1%), t‑plot method for micropore volume, and DFT/NLDFT models with cylinder‑slit pore models to obtain the pore size distribution (0.3–2 nm). For mesopore characterisation (if present), we use BJH method on the desorption branch. We also perform helium pycnometry and mercury intrusion porosimetry (for macroporosity) to obtain the skeletal density and total pore volume. All isotherms are analysed for type of hysteresis (IUPAC classification) and micropore filling steps, which provide insight into framework flexibility and gate‑opening phenomena. The combined textural profile is essential for predicting adsorption capacity and diffusion coefficients for specific adsorbates.
The precise Si/Al/P ratio and the level of heteroatomic impurities (e.g., Fe, Ti, Ca, Na) are determined by X‑ray fluorescence (XRF) on fused beads for major elements (accuracy ±0.2% relative), and by inductively coupled plasma mass spectrometry (ICP‑MS/MS) for ultra‑trace elements (detection limits 0.01–0.5 ppb) after microwave digestion. We also quantify volatile and organic species (template residues, water, and carbon) by Thermogravimetric Analysis coupled with mass spectrometry (TGA‑EGA‑MS) from 30 °C to 1000 °C under air and nitrogen, with mass resolution of 1 amu. The framework Si/Al ratio is further validated by the NMR deconvolution results, providing a cross‑checked stoichiometric model. For quality control, we provide a complete oxide analysis (SiO₂, Al₂O₃, P₂O₅, and other oxides) with expanded uncertainties (k=2).
Extra‑framework aluminium or phosphorus species, as well as surface silanol nests, can block pores and poison active sites. We use X‑ray photoelectron spectroscopy (XPS) with monochromatic Al Kα source and depth profiling (Ar⁺ cluster sputtering) to obtain Si 2p, Al 2p, P 2p, and O 1s core‑level spectra, enabling the quantification of the surface atomic ratios (which may differ from bulk) and the identification of aluminium phosphate, siliceous, or aluminium‑oxide overlayers. We complement this with transmission electron microscopy (TEM) coupled with energy‑filtered imaging (EFTEM) to map the spatial distribution of Si, Al, P, and O at sub‑nanometre resolution. For defect detection, we perform positron annihilation lifetime spectroscopy (PALS) to quantify vacancy‑type defects and open volume within the framework, which directly influences adsorption kinetics. The combined surface and defect profile ensures a comprehensive understanding of both bulk and surface heterogeneity.
For clients who need to directly correlate material properties with reactivity, we offer micro‑reactor tests for the MTO reaction, NOx‑SCR, or isomerisation of n‑butene. We use a fixed‑bed stainless steel reactor (internal diameter 4 mm) with online GC‑FID and GC‑TCD analysis, operating at temperatures up to 550 °C and pressures up to 10 bar. We measure conversion, selectivity (to light olefins, paraffins, aromatics), and catalyst deactivation profile over time. The coke content on spent catalysts is quantified by TGA‑EGA‑MS and elemental analysis. These catalytic data are then correlated with the acidity, porosity, and crystallinity parameters to establish a predictive performance model for your specific application.
Our service is uniquely distinguished by the orthogonal integration of solid‑state NMR, HR‑XRD, physisorption, chemisorption, XPS, TEM, and catalytic testing—all performed on the same representative batch to eliminate cross‑batch variability and to enable direct multivariate correlations (e.g., Si distribution vs. Brønsted acid strength vs. olefin selectivity). We operate under ISO/IEC 17025 accreditation with in‑house reference SAPO materials (SAPO‑34, ‑11, ‑5) that have been characterised by international round‑robin exercises. Our proprietary data fusion engine combines over 40 parameters (including Si(4Al) fraction, NH₃‑TPD peak temperature, B/L ratio, micropore volume, and coke deposition rate) into a single “SAPO Quality and Performance Index” (SQPI), which provides a benchmark against a database of >80 industrial and research‑grade samples.
We achieve exceptional precision: < 1.5% RSD for Si distribution by NMR, < 0.2 wt% for phase purity by XRD, < 0.01 mmol/g for acid site density, and < 0.5% for BET area. Our turnaround time for the full characterisation suite (including catalytic testing) is 14–20 working days, with expedited 10‑day service for urgent process optimisation. Crucially, our team of PhD‑level solid‑state chemists, catalyst scientists, and NMR spectroscopists provides a comprehensive interpretative report that translates each parameter into actionable guidance—e.g., how to adjust Si content to tune acidity, how to detect and eliminate extra‑framework aluminium species, and how to optimise crystallite size to improve diffusivity. With over 40 successful projects on SAPO and related molecular sieves, we empower our clients to achieve reproducible synthesis, enhance catalytic performance, and accelerate the development of next‑generation separation and conversion technologies—all with the highest level of scientific rigour and technical credibility.