1D Column Research Articles

Adsorption for efficient low carbon hydrogen production: part 1\u2014adsorption equilibrium and breakthrough studies for H2/CO2/CH4 on zeolite 13X

Reforming of fossil fuels coupled with carbon capture and storage has the potential to produce low-carbon H2 at large scale and low cost. Adsorption is a potentially promising technology for two key separation tasks in this process: H2 purification and CO2 capture. In this work, we present equilibrium adsorption data of H2 and CH4 on zeolite 13X, in addition to the already established CO2 isotherms. Further, we carry out binary (CO2–CH4) and ternary (H2–CO2–CH4) breakthrough experiments at various pressures and temperatures to estimate transport parameters, assess the predictive capacity of our 1D column model, and compare different multi-component adsorption models. CO2 adsorbs strongly on zeolite 13X, CH4 adsorbs less, and H2 adsorbs very little. Thus, H2 breaks through first, CH4 second (first in the binary breakthrough experiments) and CO2 last. Linear driving force (LDF) mass transfer coefficients are estimated based on a single breakthrough experiment and mass transfer is found to be fast for H2, slower for CH4, and slowest for CO2. The LDF parameters can be used in a predictive manner for breakthrough experiments at varying pressures, temperatures, flows, and, though with lower accuracy, even compositions. Heat transfer inside the column is described well with a literature correlation, thus yielding an excellent agreement between simulated and measured column temperatures. Ideal and real adsorbed solution theories (IAST and RAST, respectively) both model the observed breakthrough composition profiles well, whereas extended isotherms are inferior for predicting the competitive behavior between CH4 and CO2 adsorption. This study provides the groundwork necessary for full cyclic experiments and their simulation.

A multi-location peak parking approach for calculation of second dimensional retention indices for improved volatile compound identification with cryogen-free comprehensive heart-cut two-dimensional gas chromatography.

Comprehensive heart-cut multidimensional gas chromatography (CH/C MDGC) without a cryogenic trapping device was developed with an established approach for calculation of first and second dimensional retention indices (1I and 2I) for improved compound identification. A first dimensional (1D) DB-1MS column (60 m) and a second dimensional (2D) DB-WAX column (60 m) were applied with a Deans switch (DS) using a constant H/C window of 0.2 min and a periodic multiple heartcut strategy comprising 225H/C throughout the CH/C. 1I was calculated based on comparison of the middle of the heartcut time with the alkane retention times on the 1D column. A multi-location peak parking approach using sixteen sets of automated injections of alkane references was also established with the least square curve fitting method for construction of the alkane isovolatility curves which were applied for 2I calculation. The untargeted compound analysis of a perfume sample was then performed according to comparison with the libraries of mass spectra, 1I and 2I. The CH/C MDGC system with a 25 h analysis time showed a peak capacity (nc) of 9198 and 128 separated peaks with 71 compounds successfully identified according to MS, 1I and 2I library match under the established error approximation criteria. Furthermore, relationship between the analysis time and number of separated peaks was proposed based on the set of 84 identifiable compounds. With the compensation of lower separation performance and greater I errors, the analysis time could be reduced by applying a 2.5 min H/C window with a total analysis time of 2 h and nc of 1134.

The design and fabrication of ultrahigh-performance supercapacitor electrodes from bimetallic PBA/Ni(OH)2/Co3O4/NF quaternary hybrid nanocomposites

Quaternary PBA/Ni(OH)2/Co3O4/NF hybrid nanocomposites were successfully fabricated through a step-by-step strategy with 2D substrate, 1D column, and 3D PBA porous structures, which exhibited promising supercapacitor performance.

Modelling preferential flow through unsaturated porous media with the Preisach model and an extended Richards Equation to capture hysteresis and relaxation behaviour

The unsaturated flow of water in soil through unstable wetting fronts has been documented in literature. These instabilities can lead to the development of finger-flow profiles, whose paths can be “remembered” by a solid matrix of soil during future infiltration even after periods of desaturation. This process has been modelled for a 1D column of soil by the Richards equation, a non-equilibrium relaxation ODE, and Preisach hysteresis, all of which are required for finger flow. In this paper a comparison is made to similar work that use Parlange’s model of hysteresis and show that similar results are achieved by instead including the Preisach model. In addition, the model allows for the strength of hysteresis to be changed by a single parameter thus allowing the potential of parameter fitting of data in the future.

Comparison of Thermal and Flow-Based Modulation in Comprehensive Two-Dimensional Gas Chromatography—Time-of-Flight Mass Spectrometry (GC × GC-TOFMS) for the Analysis of Base Oils

Base oils are produced by refining crude oil or through chemical synthesis. They are a key component of engine oils. With an immense range of carbon numbers and boiling points, analyzing such complex mixtures is very difficult. The need to monitor industrial petroleum processing steps, as well as to identify petrochemical environmental pollutants, drives the search for improved characterization methods. Comprehensive two-dimensional gas chromatography (GC × GC) is one of the best tools for that. The modulator used in GC × GC is responsible for trapping/sampling the first dimension (1D) column analytes, then reinjecting them in the form of narrow bands onto the second dimension (2D) column for further separation. Modulators used today generally fall into two categories, thermal and flow ones. Heater-based thermal modulators trap the 1D column effluent at or above ambient temperatures. Flow-based modulators utilize storage loop(s) to collect the 1D effluent, which is subsequently flushed into the second-dimension column for further separation. A single-stage, consumable-free thermal modulator and a reverse fill/flush flow modulator were compared for the characterization of base oils. Both were evaluated on their ability to achieve separation of several conventional and synthetic engine oils components. A reverse column set, polar 1D and nonpolar 2D, allowed group-type analysis of all classes, including linear, branched, and aromatic species. The results show the ability to achieve a comprehensive separation of specific compound classes and the differentiation of engine oil types and manufacturers. Soft ionization assisted in tentative identification of two alkylated diphenylamines in each sample. The advantages and limitations of both thermal and flow modulation are presented.

A Molecular Crystal Shows Multiple Correlated Magnetic and Ferroelectric Switchings

Simultaneous control of the magnetic and electric properties of materials is crucial for their application in next-generation memory and sensor devices. Herein, we report a single-crystal Co(II) co...

Total-transfer comprehensive three-dimensional gas chromatography with time-of-flight mass spectrometry

Although comprehensive two-dimensional (2D) gas chromatography (GC × GC) is a powerful technique for complex samples, component overlap remains likely. An intriguing route to address this challenge is to utilize the additional peak capacity and chemical selectivity provided by comprehensive three-dimensional (3D) gas chromatography (GC3), especially with time-of-flight mass spectrometry detection (GC3-TOFMS). However, the GC3-TOFMS instrumentation reported to date has employed one or both modulators with a duty cycle < 100%, making the potential gain in detection sensitivity over GC × GC modest, or perhaps even worse. Herein, we describe instrumentation for GC3-TOFMS in which both modulators provide total-transfer (100% duty cycle). Specifically, the instrument is based on the facile modification of a commercial thermally modulated comprehensive GC × GC-TOFMS platform for modulation from the 1D column to the 2D column, with recently described dynamic pressure gradient modulation (DPGM) as the second modulator from the 2D column to the 3D column, which is a total-transfer flow modulation technique. Area measurements of 1D peaks are compared to the sum of 3D peak areas to validate the assumption that total-transfer from 1D to 3D is accomplished. Additionally, peak heights were amplified by as high as a factor of 177 (x̅ = 130, s = 47) via comparison of 1D peak heights to the maximum 3D peak heights. Column selection is explored, with emphasis on the resulting peak width-at-base on each dimension and usage of 3D space as evaluation metrics. Using a nonpolar × polar × ionic liquid column combination, an effective peak capacity which considers modulation-induced broadening as high as 32,300 for select analytes was achieved (x̅ = 19,900, s = 10,700). The analytical benefits of employing three selective phases, mass spectrometry detection, and total-transfer modulation are explored with separations of a metabolomics-type sample, i.e., derivatized porcine serum, and a jet fuel spiked with various sulfur-containing compounds.

A systematic investigation of comprehensive two-dimensional gas chromatography time-of-flight mass spectrometry with dynamic pressure gradient modulation for high peak capacity separations

Dynamic pressure gradient modulation (DPGM) in full modulation mode is optimized for comprehensive two-dimensional (2D) gas chromatography (GC × GC) with time-of-fight mass spectrometry (TOFMS) detection to obtain high peak capacity separations and demonstrate broad applicability for complex samples. A pulse valve introduces an auxiliary carrier gas flow at a T-union connecting the first dimension (1D) column to the second dimension (2D) column. At a sufficiently high auxiliary pressure (Paux) the 1D flow is temporarily stopped. Then, during each modulation period (PM) the valve is turned off briefly, a period termed the pulse width (pw), allowing the 1D effluent to essentially be reinjected onto the 2D column for the modulated separations. Modifications to the modulator assembly are provided to improve performance. Method optimization is demonstrated for a 116-component test mixture by tuning the Paux and the pw. For a PM = 2 s and 1F of 0.10 ml/min, the optimal pw and initial Paux selected were 200 ms and 330.9 kPa (33 psig), respectively. The 30 min separation of the test mixture provided a 1D peak capacity of 1nc = 330 and a 2D peak capacity of 2nc = 15, hence an ideal 2D peak capacity nc,2D = 1nc × 2nc = 4950. Likewise, the 2D peak capacity corrected for undersampling of the 1D separation was 4500 and corrected for both undersampling and sampling variation via statistical overlap theory was 4090. These results provide a 2-fold improvement in peak capacity relative to the previous DPGM study in full modulation mode for GC × GC-TOFMS. The optimized conditions were applied for a variety of applications: diesel fuel, derivatized cow serum, solid phase microextraction (SPME) of coffee headspace, and SPME of river water headspace. Additionally, the fraction of 2D separation space utilized (fcoverage), as defined by the minimum convex hull method, ranged from 0.60 to 0.85. We observed that any fcoverage correction to 2D peak capacity is highly sample dependent, since all samples, except for the diesel sample, were run with the same separation conditions, and yet the fcoverage ranged from 0.60 to 0.80.

Multidimensional gas chromatographic‒Mass spectrometric method for separation and identification of triacylglycerols in olive oil.

A 'heart-cut' multidimensional gas chromatography‒mass spectrometry (H/C MDGC‒MS) method for separation and identification of triacylglycerols (TAGs) in extra virgin olive oil was developed. A GC configuration, comprising a non-polar first dimension (1D) column (15 m length) and a mid-polarity second dimension (2D) column (9 m length), was employed. Standard TAGs were used to test and demonstrate the H/C MDGC method, for identification of TAG components and to validate the method. Various chromatographic conditions such as column flow and temperature program were evaluated. The 1D separation resulted in overlap of some standard TAG peaks. These overlapped 1D regions of the standard TAGs were H/C to 2D for further separation and resulted in clearly distinguished individual TAG component peaks. The 1D separation of olive oil TAGs displayed three major peaks and four minor peaks. The application of the H/C MDGC method to olive oil TAGs resulted in the separation of each sampled 1D region into two or more TAG peaks. TAG components in olive oil resolved on the 2D column were identified based on characteristic mass fragment ions such as [M-RCO2]+, [RCO+128]+, [RCO+74]+ and RCO+ and comparison of their mass spectra with that of the standard TAGs. Sixteen olive oil TAGs were identified by MS after 2D separation. The repeatability of the H/C method was evaluated in terms of retention time shift and area response in the 2D and found to be <0.02% and <8% RSD respectively.

Mixed Columnar Assembly of Ferroelectric and Antiferroelectric Benzene Derivatives Bearing Multiple -CONHC14H29 Chains.

The discotic hexagonal columnar (Colh) liquid crystalline phases of simple benzene derivatives bearing -CONHC14H29 chains at the 1-, 3-, and 5-positions (3BC) and 1-, 2-, 4-, and 5-positions (4BC) display ferroelectricity and antiferroelectricity, respectively. The phase transition behavior, molecular assembly structures, dielectric response, and ferroelectric properties of their mixed crystals [(3BC)1-x(4BC)x] were evaluated to clarify the nanoscaling effect on the collective inversion of the one-dimensional (1D) N-H···O═ hydrogen bonding interaction observed in the (3BC)∞ chain. A small quantity of 4BC doped into 3BC (x ≤ 0.03) maintained the ferroelectric polarization-electric field response (P-E) in the (3BC)1-x(4BC)x chains, where the antiferroelectric 4BC molecules in the ferroelectric 3BC column act as a pinning potential site for dipole inversion. On the contrary, a relatively large amount of 4BC doping (x ≥ 0.1) forms a domain separation state between the hydrogen-bonded (3BC)∞ and (4BC)∞ columns, in which the ferroelectric P-E hysteresis completely disappeared. The correlation length for the appearance of ferroelectricity in the 1D column was estimated to be ∼40 nm in the Colh liquid crystalline phase of 3BC.

Physical Foam Stability of Loose Sandy-Clay: a Porosity Role in the Conditioned Soil

To prevent the collapse and settlement of fine granular soil during earth pressure balance (EPB) tunneling or tunneling balance machine (TBM) operations, foaming agent mixing is one of the most efficient techniques. This work focuses on the stability of loose sandy-clay soil conditioned with the foaming agent. Four reconstituted loose sandy-clay soils were conditioned with the foaming agent CLB F5/AC. Using optical observation, Turbiscan analysis, and foam volume determination, the stability of foam mixed with fine soils was studied based on drainage coalescence and coarsening phenomena that occurred over time. Additionally, foam stability under gravity drainage was analyzed through a (one-dimensional) 1D column experiment. Variation in the FIR (foam injection ratio) shows that there is a limit FIR value from which the foam begins to be observed in the soil sample, involving a discontinuous porosity increase to the detriment of the continuous porosity decrease. An approach that considered this discontinuous porosity generated by the inclusion of gas bubbles was used to describe foam bubble degradation. Tests carried out on foam alone showed its rapid degradation compared with that of the foam added and mixed in the soil. Fine particles of clay allow foam stability even in the soil mixture. The foam volume in the soil decreases according to constant volume stages separated by a fast volume decrease. Both drainage and coalescence phenomena have occurred significantly for high values of FIRs. From the 1D column experience, foam bubbles modify the drainage kinetics by accelerating the drainage velocity compared with that of unconditioned soil. The foam behavior evolution over time when mixed with the soil can be analyzed using the same theory of the behavior of the foam alone.

Purification Efficiency for Treated Waste Water in Case of Joint Infiltration with Water Originating from Precipitation

The decentralized treatment of wastewater and its on-site infiltration is common practice, especially in rural areas. However, uncertainties exist on the degradation potential of treated wastewater constituents mixed with additional infiltration of large quantities of water originating from precipitation. The intermixture of these waters is causing a reduction of residence times of the treated wastewater as well as an increased water saturation within the unsaturated soil zone. This can lead to a negative influence on the purification efficiency. Laboratory-scale 1D column experiments, accompanied by numerical simulations of water flow using the software code HYDRUS 1D, have been performed to evaluate the risks for a reduction of the degradation efficiency. Water content measurements and analysis of relevant organic substances in samples taken at different depths were the basis for evaluating the influence of the joint infiltration on the purification efficiency. The results highlight that a joint infiltration of treated wastewater and additional water originating from precipitation is not affecting the degradation efficiency for treated wastewater constituents. Degradation rates under these conditions were similar to the infiltration of treated wastewater alone. Timeframes with high water saturation were limited to the duration of the precipitation event.

Injection of Zerovalent Iron Gels for Aquifer Nanoremediation: Lab Experiments and Modeling

One of the main technical problems faced during field-scale injections of iron microparticles (mZVI) for groundwater nanoremediation is related to their poor colloidal stability and mobility in porous media. In this study, a shear-thinning gel, composed of a mixture of two environmentally friendly biopolymers, i.e., guar gum and xanthan gum, was employed to overcome these limitations. The slurry rheology and particle mobility were characterized by column transport tests. Then, a radial transport experiment was performed to mimic the particle delivery in more realistic conditions. The gel, even at a low polymeric content (1.75 g/L), proved effective in enhancing the mobility of high concentrated mZVI suspensions (20 g/L) in field-like conditions. The high radius of influence (73 cm) and homogeneous iron distribution were achieved by maintaining a low injection overpressure (&lt;0.4 bar). Based only on the information derived from column tests, the MNMs 2018 software (Micro- and Nanoparticle transport, filtration, and clogging Model-Suite) was able to predict the particle distribution and pressure build-up measured in the radial domain. Experimental and simulated results showed good agreement, thus proving that a simplified experimental-modeling procedure based on 1D column tests could be used to effectively upscale the slurry behavior to more representative scales, e.g., radial domains.

High resolution two-dimensional liquid chromatography coupled with mass spectrometry for robust and sensitive characterization of therapeutic antibodies at the peptide level

Separations of complex peptide mixtures have been a common target application for two-dimensional liquid chromatography over the last few decades. These separations have most frequently been carried out at the capillary scale, with columns on the order of 75 µm i.d. and flow rates on the order of 500 nL/min. Recently, however, several groups have worked to optimize comprehensive 2D-LC (LC × LC) separations of peptides at the analytical scale (i.e., 2 mm i.d. columns, and ca. 1 mL/min flow rates) and demonstrated peak capacities on the order of 5000 in analysis times of a few hours, using reversed-phase separations in both dimensions. In this paper we aim to advance the performance of such separations in two primary ways. First, we demonstrate that active solvent modulation (ASM) can be used to improve the 2D peak capacity by both enabling use of long and highly efficient first dimension (1D) columns, and by mitigating the deleterious effects of injecting large fractions of 1D effluent into the small columns that are required for fast and highly sensitive second dimension (2D) separations. Taken together these two benefits enable the realization of a peak capacity of 10,000 in an analysis time of four hours. This comes at the cost of increased instrument complexity compared to 1D-LC separations, but the 2D-LC approach is unquestionably the most efficient way to improve upon the resolving power of existing 1D-LC. Second, we have systematically studied the compromise between the peak capacity of each 2D separation and the operating pressure required to achieve that peak capacity. Understanding this compromise will be important to the development of LC × LC methods that both produce high peak capacities, and are sufficiently robust to operate for days at a time without significant losses in separation performance. Based on the results of this study we chose conditions for subsequent separations that required less than 400 bar operating pressure in the second dimension, but yielded a 2D peak capacity of about 3500 in 2 h. After 160 h of continuous operation of the LC × LC separation under these conditions (and about 20,000 injections into the 2D column) the 2D column had only lost about 18% of its initial isocratic efficiency. These results should motivate further development and implementation of such high performing and robust separations for the identification and quantification of peptides in a variety of application areas, including digests of therapeutic proteins such as monoclonal antibodies.

Dynamic pressure gradient modulation for comprehensive two-dimensional gas chromatography

We report the discovery, preliminary investigation, and demonstration of a novel form of differential flow modulation for comprehensive two-dimensional (2D) gas chromatography (GC×GC). Commercially available components are used to apply a flow of carrier gas with a suitable applied auxiliary gas pressure (Paux) to a T-junction joining the first (1D) and second (2D) dimension columns. The 1D eluate is confined at the T-junction, and introduced for 2D separation with a cyclic rhythm, dependent upon the relationship of the modulation period (PM) to the pulse width (pw), where pw is defined as the time interval when the auxiliary gas flow at the T-junction is off. We refer to this flow modulation technique as “dynamic pressure gradient modulation” (DPGM) since a pressure gradient oscillates with the PM along the 1D and 2D column ensemble providing temporary stop-flow conditions and fast 2D flow rates, resulting in 100% duty cycle and full modulation. A 90-component test mixture was used to evaluate the technique with a pw of 60 ms and a PM of 750 ms. The resulting peaks were narrow, with 2Wb ranging from about 20–180 ms. With an average 1Wb of 3 s and a 2nc of 10, a 2D peak capacity, nc,2D, for the 25 min separation was 5000. The detector response enhancement factor (DREF) is reported, defined as the peak height of the highest modulated 2D peak divided by the unmodulated 1D peak height (DREF = 2h/1h). The DREF ranged from about 7–87, depending on the 1Wb and 2Wb for a given analyte. A diesel sample was analyzed to demonstrate performance with a complex sample. Based upon the average 1Wb of 5 s and an average 2Wb of 168 ms, a nc,2D of 8640 was obtained for the 60 min diesel separation. Finally, the modulation principle was investigated as a function of PM, pw, and the volumetric flow rates, 1F and 2F. The measured 2Wb correlate well with the theoretical 2D injected width, given by 2Winj = (1F/2F) ·PM. However, the relevant 1F appears to be dictated by the 1D flow rate when no pressure is applied (during the pw interval), instead of 1F being the average flow rate on 1D (defined by the 1D dead time). The findings provide strong evidence for a differential flow modulation mechanism.

Nanoscale Effects in One-Dimensional Columnar Supramolecular Ferroelectrics.

Organic ferroelectrics have been actively developed with the goal of fabricating environmentally friendly and low-cost memory devices. The remanent polarization of hydrogen-bonded organic ferroelectrics approaches that of the inorganic ones. Nanoscale fabrication of organic ferroelectrics is an essential aspect of high-density memory devices. A pyrene derivative with four tetradecylamide (-CONHC14 H29 ) chains (1) formed an amide-type N-H⋅⋅⋅O hydrogen-bonded one-dimensional (1D) column, which demonstrated ferroelectricity in the discotic hexagonal columnar (Colh ) liquid crystalline phase through the inversion of the orientation of the hydrogen-bonded chains. On the contrary, similar chiral pyrene derivatives bearing 3,7-dimethyl-1-octhylamide chains (S-2 and R-2) did not indicate the Colh phase and ferroelectricity. Homogeneous mixed liquid crystals (1)1-x (S-2)x (i.e., between the ferroelectric 1 and the non-ferroelectric S-2) enable the control of the nanoscale aggregation state of the organic ferroelectrics, resulting in a nanoscale effect of the 1D supramolecular ferroelectrics. Ferroelectric mixed liquid crystals (1)1-x (S-2)x were observed at x≦0.03, where one S-2 molecule was inserted after every thirty-three 1 molecule in the mixed liquid crystal (1)33 (S-2). An average (1)34 length of approximately 12 nm was required to maintain the 1D ferroelectricity, which was similar to the nanoscale limit of inorganic ferroelectrics, such as hafnium oxide thin film (≈15 nm).

Impact of data bin size on the classification of diesel fuels using comprehensive two-dimensional gas chromatography with principal component analysis

Principal component analysis (PCA) is a widely applied chemometric tool for classifying samples using comprehensive two-dimensional (2D) gas chromatography (GC × GC) separation data. Classification via PCA can be improved by 2D binning of the data. A “standard operating procedure (SOP) bin size” is often applied to improve the S/N and to mitigate potential retention time misalignment issues. The SOP bin size is generally selected to be slightly larger than the typical 2D peak dimensions. In this study we examine to what extent a single SOP bin size is optimal for all of the class comparisons that can be made in a single PCA scores plot. For this purpose, a GC × GC-FID dataset comprised of 5 different diesel fuels (i.e., 5 sample classes), each run with 4 replicates using a reverse column configuration (polar 1D column and non-polar 2D column) was utilized. The dataset was collected within about one day, which minimized retention time misalignment in order to allow the study to focus on S/N enhancement concurrent with maintaining the chemical selectivity provided by the GC × GC separations. A total of 110 bin sizes were evaluated. Degree-of-class separation (DCS) was utilized as a quantitative metric to assess the impact of binning in improving separation in the scores plot. The DCS was calculated pair-wise between nearest neighbor sample classes for each of the 5 sample classes in the scores plot (5 sample class pairs). Results indicated the SOP bin size did not provide the highest DCS for any of the 5 fuel pairs. Each fuel pair is found to have its own optimal bin size, suggesting the binning finds the balance between S/N optimization concurrent with leveraging the chemical selectivity information differences in the samples as manifested in their GC × GC separation “patterns”. Robustness of the findings in this study were supported by leaving out one fuel at a time and re-running the PCA models.

Multidimensional gas chromatography investigation of concentration and temperature effects of oxime interconversion on ionic liquid and poly(ethylene glycol) stationary phases

This study develops analytical approaches using comprehensive heart-cut multidimensional gas chromatography (H/C MDGC) to experimentally investigate effects of concentration and temperature on peak shapes and on kinetic analysis of E/Z isomerisation of oximes which undergo various extents of interconversion on 1D and 2D separation columns. Different stationary phase combinations were investigated. An SLB-IL76 1D column results in good separation of the isomers but with negligible interconversion (1Dsep). Precise targeted heart-cuts (H/C; 3–15 s windows) and cryogenic trapping of selected sections eluting from this 1D column allows well controlled E/Z isomer ratios to be delivered to a 2D poly(ethyleneglycol) (PEG) phase column. This phase catalyses oxime interconversion, with separation; this is termed 2Dinter. This column set describes a 1Dsep × 2Dinter arrangement. The interconversion forward rate constant (k1UE, calculated by using DCXplorer) was found to be independent of the %E isomer (i.e. first order kinetics); k1UE increased at higher temperature (increased Gibbs activation energies, ΔGapp). In addition, a long 1D SLB-IL111 column gave oxime separation with interconversion (1Dinter). Comprehensive multiple H/C of the zone performed on the 2D PEG (2Dinter) at 40, 60 and 80 °C resulted in a 2D presentation (1Dinter × 2Dinter) with a unique rectangular display of interconversion from each H/C pulse with varied isomer concentration ratios. Data for k1UE from 1DGC analysis suggests underestimation of k1UE on 1Dinter SLB-IL111 from the 2D result. The k1UE value on 2Dinter PEG column is more reliably evaluated by summation of all the 2Dinter profiles rather than that obtained from the average value for the individual H/C pulses.

Throwing in a Monkey Wrench to Test and Determine Geared Motion in the Dynamics of a Crystalline One-Dimensional (1D) Columnar Rotor Array.

Crystals of molecular rotor 1 with a central 1,4-phenylene rotator linked to two molecules of the steroid mestranol were prepared with 1%, 5%, 20%, and up to 40% of the analogous 2, which contains a larger 2,3-difluorophenylene rotator and effectively acts as a monkey wrench that affects the rotation of the host. The packing motif of the desired P32 crystal form consists of 1D columns of nested rotors arranged in helical arrays with the central aromatic rotators disordered over two sites related by 85° rotation about their 1,4-axes. Rotational dynamics measured by quadrupolar echo 2H NMR line shape analysis were analyzed in terms of a process model that involves degenerate 180° jumps in the fast exchange regime combined with a highly correlated and entropically demanding jump of 85° between the two dynamically disordered sites. While the enthalpic and entropic barriers for the 180° jump estimated from 2H T1 measurements were Δ H⧧ = 2.7 ± 0.1 kcal mol-1 and Δ S⧧ = -5.0 ± 0.5 cal mol-1 K-1, respectively, the corresponding parameters for the slower 85° jumps, determined by line shape analysis, were Δ H⧧ = 2.2 kcal mol-1 and Δ S⧧ = -23 cal mol-1 K-1. Increasing amounts of the larger molecular rotor 2 in the solid solution results in significant dynamic perturbations as the guest, acting as a monkey wrench, reaches values of one out of every five molecular rotors in the chain.

Column selection approach to achieve a high peak capacity in comprehensive three-dimensional gas chromatography

The separation power of comprehensive three-dimensional gas chromatography (GC3) is substantially enhanced through proper selection of the phase volume ratio, β, of each column relative to each other on successive dimensions. Consideration and application of the ratio of phase volume ratios, βr, or β ratio, between successive dimensions has been a relatively un-studied approach to maximize separating power in comprehensive multidimensional GC instrument design. Herein, proper selection of βr in multidimensional GC is shown to control the elution temperature, Te, of analytes throughout a 40 min primary (1D) column separation, and thus better control width-at-base, W, on all three dimensions. Specifically, between the 1D and secondary (2D) columns, a βr of 0.45 was applied, and between the 2D and tertiary (3D) columns a βr of 1.0 was applied. A total ideal peak capacity of 30,600, or a peak capacity production of ~770 peaks/min, was accomplished with the GC3 instrument with the reconfigured parameters. Additionally, due to the complex nature of this three-dimensional data, a novel approach to “slicing” the chromatographic run into user-defined time intervals is shown. This novel way to view the data still elicits a traditional GC×GC chromatograms, but with the focus on 2D × 3D separations. Moreover, due to proper βr selection, every 2 s window (i.e. every 1D modulation period) is shown to have a peak capacity of ~50–100 for each 2D × 3D separation. This high overall peak capacity (30,600) and peak capacity per 1D modulation (~50–100), courtesy of proper column selection, is demonstrated to hold great promise to physically separate truly complex mixtures.