Pressure Swing Research Articles

Optimal design and operation of reactive distillation systems and reactive dividing wall systems with pressure swing distillation and hybrid distillation-pervaporation

Process intensification is essential in exploring more energy-efficient processes, and key examples related to fluid separations are reactive distillation and hybrid distillation-pervaporation processes. This work will consider the reaction and separation of a general quaternary reactive system with a minimum boiling binary azeotrope AC, in a reactive distillation column where, given the thermodynamics limitations, further downstream separation is required. Low and high chemical equilibrium is considered for the reaction. For the downstream purification, both pressure swing distillation and a hybrid distillation-pervaporation process are considered. For each of the structures, their intensified equivalent dividing wall structures are also considered, including a hybrid reactive dividing wall system. It is shown that reactive distillation followed by a hybrid distillation-pervaporation system can save up to 24% energy compared to reactive distillation with pressure swing separation, and that the dividing wall column counterpart structures have lower production-based total annualised costs than the corresponding base systems.

Development of switchless thin-plate sorption compressor and miniaturized check valves for 5 K J- T cooler

The cell of the sorption compressor developed in this paper has a thin-plate shape to accelerate the pressure swing by reducing the heating and cooling periods. Its width, height and thickness are 100 mm, 100 mm and 4.6 mm, respectively. Two identical cells filled with 22.8 g of charcoal mass are operated alternately to generate and maintain significant pressure difference for the 5 K J-T cooler with the pre-cooling temperature of 15 K. The designed nominal pressure of the high-pressure and the low-pressure parts of the J-T cooler are 1000 kPa and 196 kPa, respectively. The mass flow rate and the pressure gradient of the thin-plate sorption compressor with commercial check valves are measured experimentally. As the performance of the compressor, COP of the compressor is estimated and compared with the compressor of previous researches. Furthermore, to reduce leakage rate and thermal inertia of check valves in the compressor, miniaturized check valve is specially designed and fabricated to replace the commercial valve. When the flow direction is reversed in the valve, the leakage is passively prevented by contacting two metal surfaces at low temperature (30 K). The essential parts of the valve are critically miniaturized to reduce the overall thermal inertia of the compressor system. The cracking pressure and the leakage rate of the developed check valve and the commercial check valve are measured to compare.

Microcellular Thermoplastic Polyurethane (TPU) with Multimodal Cell Structure Fabricated Based on Pressure Swing Strategy and Its Compressive Mechanical Properties

Microcellular Thermoplastic Polyurethane (TPU) with Multimodal Cell Structure Fabricated Based on Pressure Swing Strategy and Its Compressive Mechanical Properties

Evaluation of the CH4/CO2 separation by adsorption on coconut shell activated carbon: Impact of the gas moisture on equilibrium selectivity and adsorption capacity

Upgrading biogas to biomethane is of great interest to change the energy matrix by feeding the renewable fuel produced from biomass waste into natural gas grids or directly using it to replace fossil fuels. The study aimed to assess the adsorption equilibrium of CH4, CO2, and H2O on a coconut-shell activated carbon (CAC 8X30) to provide data for further studies on its efficiency in upgrading biogas by Pressure Swing Adsorption (PSA). The adsorbent was characterized, and equilibrium parameters were estimated from monocomponent CH4, CO2, and H2O equilibrium isotherms. Binary and ternary equilibrium isotherms were simulated, and the selectivity and adsorption capacity of the CAC 8X30 were calculated in dry and wet conditions and then compared with zeolite 13X as a reference material. Regarding characterization, Nitrogen and Hydrogen Physisorption results indicated that 94 % of the pore volume is concentrated in the region of micropores. The adsorption affinity with CAC 8X30 estimated from monocomponent isotherms was in the order KH20>KCO2>KCH4. IAST-Langmuir model simulations presented good agreement with experimental binary equilibrium data. Further simulations indicated equilibrium selectivity for CO2 over CH4 (e.g., 4.7 at 1 bar and 298 K for a mixture of CH4/CO2, 60/40 vol%), which increased in the presence of moisture, indicating its suitability for upgrading humid biogas. Simulations for zeolite 13X suggested that the material is unsuitable in the presence of water vapor but presents higher selectivity than the CAC 8X30 in dry conditions. Hence, the integration of both materials might be helpful for biogas upgrading.

Onboard pre-combustion carbon capture with combined-cycle gas turbine power plant architectures for LNG-fuelled ship propulsion

This paper investigates the concept of pre-combustion carbon capture (Pre-CCS) with a combined cycle gas turbine (CCGT) propulsion system to achieve energy efficient carbon capture onboard a Liquid Natural Gas fuelled vessel. A basic CCGT model with energy efficiency of 51.6 % when using LNG as fuel was integrated with a Pre-CCS system composed of a steam methane reformer, water–gas shift reactors, pressure swing adsorption (SMR-PSA), and liquid CO2 storage. Various waste heat utilisation schemes integrated with the CCGT-reformer were modelled in Aspen HYSYS. The modelling of the waste heat recovery networks as energy streams integrating between various processes and unit of operations has facilitated a closed-loop simulation of various systems. It was concluded that a proper utilisation of the high-grade heat from the gas turbine (GT) exhaust and from the reformer is crucial to improve the overall energy efficiency and carbon capture rate, exemplified by a scheme where the heating needs for the SMR and the cooling needs from the water–gas-shift reactors are fully integrated. When optimised, the integrated system had an overall energy efficiency of 41.5 % and 43.2 % (i.e. an efficiency loss of 10.2–10.5 percentage points from the base CCGT system) accompanied with specific GHG emission reduction of 51.2 % and 52.3 % for operation of the GT at a turbine entry temperature of 1700 K and 1850 K, respectively. Intermediate levels of reforming, where the GT uses a mix of LNG and reformate gases, were also simulated, showing an almost linear evolution from the 100 % LNG feed to the GT to the 100 % reformate case. Such a strategy could be used for gradual evolution to meet the required CO2 reduction timeline. It was determined that the 100 % reformate case provides the highest CO2 capture rate. Estimates of other emissions from the GT assuming typical combustor residence times for the whole range of fuel blends were also carried out, showing that the overall greenhouse gas emission is dominated by CO2, given that the GT emits negligible N2O and unburnt methane. Some capital cost estimates were also made to determine the unit price of hydrogen fuel produced onboard, suggesting that the CAPEX was not prohibitive. These findings support the pre-combustion CCS − CCGT integrated system as a promising long-term decarbonisation and propulsion strategy to comply with emissions regulations, displaying good performance in terms of cost, energy consumption, and CO2 reduction. The scalability and adaptability of the proposed system for existing and new-built ships across the decarbonisation timeline is also discussed.

Molecular insights into improved oxygen adsorption: Ag+ and Ce3+ doping in Li-LSX for air separation

Pressure swing adsorption (PSA) is a cost-effective and efficient method for oxygen production. It is crucial to improve the adsorption capacity of zeolite adsorbent material to facilitate oxygen production for PSA. Based on the molecular simulation method, the Ag+ and Ce3+ were doped into Lithium-based Low Silica X (Li-LSX) zeolite to enhance the adsorption of O2. The developed adsorption model is in good agreement with the experimental results. Equilibrium parameters including adsorption capacity, heterogeneity, and N2/O2 selectivity were obtained by fitting with the Langmuir-Freundlich model. The results showed that the N2/O2 selectivity of AgLi-LSX with a 30% Ag+ exchange ratio was 3.2% higher compared with Li-LSX, while the adsorption capacity of CeLi-LSX with a 30% Ce3+ exchange ratio was 27.4% greater for O2 than Li-LSX. In addition, the isosteric adsorption heats and distributions of potential energy were simulated to reveal the mechanism of performance enhancement. The adsorption capacity for O2 exhibited a sustained increase trend as the exchange ratio of Ce3+ increased. The findings of this research can guide the development of oxygen-selective adsorbents and reduce the cost of PSA oxygen production.

Effects of aluminium/Clay ratio on the adsorption selectivity of aluminium pillared clays for Biogas purification

Biogas, a sustainable energy source, is hampered by CO2 and N2. Commercially purifying it to biomethane involves pressure or vacuum swing adsorption. The efficiency and cost-effectiveness of these techniques pivot on the adsorption selectivity of the employed adsorbent material. This study examined the impact of varying metal/clay ratios in porous aluminium pillared clays on adsorption selectivity. Characterization techniques, including nitrogen adsorption/desorption, XRD, FTIR, SEM, and Raman spectroscopy, were employed. High-pressure adsorption capacity for CO2, CH4, and N2 was investigated up to 1000 kPa. Selectivity for CO2/CH4, CO2/N2, and CH4/N2 binary mixtures was calculated using IAST. Results indicate that changing the metal/clay ratio altered physiochemical properties, enhancing adsorption capacity and selectivity. AlPILC-4 demonstrated maximum surface area (158 m2∙g-1) and adsorption capacity (0.35–1.13 mmol∙g-1) for all gases, while AlPILC-2 exhibited the highest selectivity (11.85–1.85) at 100 kPa. The decrease in the surface area at higher metal/clay ratio apprehends to the saturation of swelling capacity of the parent clay. However, increase in the competitive adsorption with surface area resulted in a decrease in the selectivity of the samples. Working capacity of the modified samples calculated at two different regeneration pressures (100 kPa and 0.133 kPa) help comprehend the cost layout and efficiency of the prepared materials. Notably, the results mirrored the trends observed in adsorption capacity, with values nearly 200 % higher than those of the parent clay.

On the benefits of Counter-Current regeneration on a partial pressure swing Adsorptive reactor (PPSAR) with application to the Water Gas Shift reaction

This work demonstrates the benefits of carrying out counter-current over co-current regeneration during the operation of a Partial Pressure Swing Adsorptive Reactor with application to the Water Gas Shift reaction. Our previously introduced dynamic, multidomain, multiscale model is used to compare two theoretical case studies employing co-current and counter-current regeneration modes, respectively. The process conditions for the two regeneration case studies remain identical apart from the employed regeneration modality. This allows for the elucidation of the process performance benefits arising solely from the adaptation of the employed regeneration mode.

Six-Tower Pressure Swing Adsorption Demonstration Animation

The Pressure Swing Adsorption (PSA) technique is a widely embraced automated method for gas separation within the industrial sector, prized for its operational simplicity and substantial economic benefits. In practice, the process typically involves the use of multiple towers to facilitate the completion of the PSA cycle. However, with the increasing number of towers in a PSA system, the intricacies of the cyclic process tend to amplify, posing challenges for novices attempting to grasp the mechanics of a six-tower PSA cycle. Utilizing animation can facilitate the process of comprehending these complex techniques by presenting them in a simplified and visually engaging format. Therefore, our research group has designed an animated depiction of a six-tower PSA device, predicated on the prototype established in our laboratory. This animation furnishes an inclusive demonstration of a complete cycle, encompassing twelve steps, pertaining to the operation of a six-tower PSA. It is our aspiration that this tool will prove advantageous for those who are embarking on the journey of understanding multi-tower PSA, as well as for seasoned professionals engaged in the field of pressure swing adsorption.

Fine-tuned MOF-74 type variants with open metal sites for high volumetric hydrogen storage at near-ambient temperature

Adsorbent-based hydrogen storage systems offer a potential solution to current challenges in hydrogen storage, particularly those requiring high pressures or cryogenic temperatures. Specifically, the use of metal–organic frameworks (MOFs) featuring open metal sites that strongly adsorb hydrogen represents a promising strategy for near-ambient-temperature hydrogen storage. This study investigates the hydrogen storage properties of M2(dondc) (M = Mg2+, Co2+, and Ni2+), an extended version of MOF-74. Among this series, Ni2(dondc) exhibits the second-highest volumetric hydrogen capacity of 10.74 g L−1 at 298 K under pressure swing adsorption conditions (100 to 5 bar) at ambient temperatures. The superior hydrogen storage performance of Ni2(dondc) is attributed to its highly polarizable Ni open metal sites and a significant heat of adsorption of 12.2 kJ mol−1. These findings are corroborated by temperature-programmed desorption spectroscopy and van der Waals-corrected density functional theory calculations. In addition to its exceptional hydrogen capacity, Ni2(dondc) exhibits robust structural stability and long-term durability, positioning it as a promising candidate for near-ambient-temperature hydrogen storage applications.

A System for the Combined Carbon Capture and Utilization to Produce Renewable Methanol from Biogas

AbstractCoupling of biogas upgrading and power‐to‐X is challenging due to the intermittent cheap energy availability. A system was designed that overcomes the technical challenges in this coupling. This is possible by alternating biogas upgrading and methanol synthesis in a reactor operating both as sorption‐enhanced synthesis reactor and as upgrading unit by pressure swing adsorption. It was observed that this concept is feasible in both fixed‐ and fluidized‐bed reactors, and the potential for economic performance improvement was quantified in approximately 20 % increase of the internal rate of return.

Zeolite-coated 3D-printed gyroid scaffolds for carbon dioxide adsorption

3D-printed adsorbents are gaining increased attention owing to their potential in overcoming operational challenges faced by the conventionally structured counterparts. In this work, cylindrical scaffolds of triply periodic minimal surface (TPMS) configuration were synthesized using 3D-printing by stereolithography. This unique gyroid sheet TPMS network was selected as it offers a high surface-area-to-volume ratio. The surface of the scaffolds was modified by a silanization process followed by coating via grafting with zeolite 13X crystals toward CO2 adsorption application. A secondary zeolite coating step was also employed to enhance the zeolite 13X loading, resulting in zeolite loadings of 16 wt% and 23 wt% after the primary and secondary coatings, respectively. Following morphological and structural characterization, the CO2 adsorption performance of the 3D-printed materials was evaluated with respect to adsorption capacity, kinetics, selectivity, and heat of adsorption. Cyclic stability was also assessed over CO2 adsorption–desorption pressure swing adsorption cycles at 25 °C. Comparative analysis showed that the 3D-printed coated samples exhibited higher CO2/N2 selectivity and improved cyclic stability with a slightly lower CO2 adsorption capacity than the zeolite 13X powder. The heat of adsorption ranged from 18 to 41 kJ mol−1 for both the powder and the coated adsorbents, indicating physisorption. The gyroid lattice of the 3D-printed structures, featuring a densely arranged network of smooth, interconnected flow channels, facilitated molecular transport thus yielding higher CO2 adsorption kinetics than the powder. Indicatively, the primary and secondary coatings attained an equilibrium capacity of 4 mmol g−1 at 25 °C in 62 and 57 min, respectively, while the powder required 110 min at the same conditions. The 3D-printed materials exhibited also significantly higher CO2/N2 selectivity values of 569 and 115 at 50 mbar and 1 bar, respectively, for the primary coating sample, and 536 and 73 at 50 mbar and 1 bar, respectively, for the secondary coating one. The findings highlight the potential of 3D-printing to produce coated structured adsorbents with complex geometries for sustainable CO2 capture and gas adsorption processes.

Performance assessment of activated carbon thermally modified with iron in the desulfurization of biogas in a static batch system supported by headspace gas chromatography

A static batch arrangement composed of anti-leak vials coupled to gas chromatography is proposed as a complementary system for performance assessment of biogas desulfurization by adsorption. For testing, a modified commercial activated carbon produced by controlled thermal treatment in the presence of iron(III) species improved biogas desulfurization. The adsorbents showed a superior hydrogen sulfide removal compared to ordinary one. Pseudo-first-order, pseudo-second-order, and Bangham’s kinetic models were used to fit experimental data. All studied samples followed pseudo-first-order model, indicating the predominance of physisorption, and Bangham’s model, confirming that the micropores structure played an important role for gases diffusion and adsorbent capacity. Additionally, the materials were characterized by N2 adsorption–desorption, X-ray diffraction, infrared spectroscopy, scanning electron microscopy and energy-dispersive spectroscopy. The thermal treatment associated with iron impregnation caused significant modifications in the surface of the materials, and the iron species showed two main benefits: an expressive increase in the specific area and the formation of specific adsorption sites for hydrogen sulfide removal. The results reinforce the advantages of iron-modified adsorbents in relation to their non-modified counterparts. The analytical methodology based on the confinement of multiple gases contributes to improving the understanding of the hydrogen sulfide adsorption process using pressure swing adsorption technology.Graphical

Photosynthetic process for removing H2S and CO2 from biogas using the microalgae Chlorella sorokiniana

Biogas is an alternative source of energy that contributes on reducing the emissions of polluting gas in comparison to fossil fuels as well as promoting the treatment of organic waste. However depending on the substrate used in its production, it may have a high concentration of carbon dioxide (CO2) and hydrogen sulfide (H2S); in these cases a treatment is necessary to make its use viable, for comply with current legislation and avoid damage to materials and health. Currently, the most widely used methods are physical-chemical, such as absorption, adsorption, membrane separation, and Pressure Swing Adsorption (PSA), among others. However, these methods are expensive and generate waste that needs to be treated. In this sense, biological methods have proved to be promising alternatives, especially photosynthetic processes using microalgae. This study aimed to evaluate the efficiency in removing CO2 and H2S from biogas through a bench-scale purifier prototype consisting of a photobioreactor and an absorption column, in a continuous biogas flow system. The experiment lasted 240 hours, during which 9 m³ of biogas were treated. In the first 24 hours, the flow rate was 1 L/min, resulting in an average removal of 60.8% of H2S and 20.2% of CO2. Between 24 hours and 240 hours of the study, the average biogas flow rate was 0.54 L/min, and an improvement in removal was observed, reaching 83.4% of H2S and 29.7% of CO2. The system showed efficiency in biogas treatment. However, possibilities for improvement were identified in terms of biogas flow and process, which could further enhance the results presented here.

Rapid and Accurate Screening of the COF Space for Natural Gas Purification: COFInformatics.

In this work, we introduced COFInformatics, a computational approach merging molecular simulations and machine learning (ML) algorithms, to evaluate all synthesized and hypothetical covalent organic frameworks (COFs) for the CO2/CH4 mixture separation under four different adsorption-based processes: pressure swing adsorption (PSA), vacuum swing adsorption (VSA), temperature swing adsorption (TSA), and pressure-temperature swing adsorption (PTSA). We first extracted structural, chemical, energy-based, and graph-based molecular fingerprint features of every single COF structure in the very large COF space, consisting of nearly 70,000 materials, and then performed grand canonical Monte Carlo simulations to calculate the CO2/CH4 mixture adsorption properties of 7540 COFs. These features and simulation results were used to develop ML models that accurately and rapidly predict CO2/CH4 mixture adsorption and separation properties of all 68,614 COFs. The most efficient separation process and the best adsorbent candidates among the entire COF spectrum were identified and analyzed in detail to reveal the most important molecular features that lead to high-performance adsorbents. Our results showed that (i) many hypoCOFs outperform synthesized COFs by achieving higher CO2/CH4 selectivities; (ii) the top COF adsorbents consist of narrow pores and linkers comprising aromatic, triazine, and halogen groups; and (iii) PTSA is the most efficient process to use COF adsorbents for natural gas purification. We believe that COFInformatics promises to expedite the evaluation of COF adsorbents for CO2/CH4 separation, thereby circumventing the extensive, time- and resource-intensive molecular simulations.

Life cycle assessment of post-combustion carbon capture and storage for the ultra-supercritical pulverized coal power plant

In this paper, different emerging post-combustion technologies, i.e., monoethanolamine (MEA), aqueous ammonia, pressure swing adsorption (PSA), temperature swing adsorption (TSA), membrane and calcium looping, were applied to an ultra-supercritical coal-fired power plant for carbon capture. A ‘cradle-to-grave’ life cycle assessment (LCA) was conducted to evaluate the technical performance and environmental impacts of the power plant with six emerging carbon capture technologies. Carbon capture significantly influences the impact categories directly associated with flue gas emission. The application of carbon capture reduced the GWP in the range of 49–75 %. TAP also reduced in the range of 18–51 %. However, the human toxicity potential, eutrophication potential, ecotoxicity potential and particulate matter formation potential increased due to energy and resource consumption in the upstream and downstream processes. For the life cycle water consumption potential, it decreased by 8 % with calcium looping, whereas it increased in the range of 36–75 % with other post-combustion technologies. The highest reduction in GWP and the least reduction in power efficiency was observed in calcium looping because of the high-temperature heat recovery from flue gas and elimination of complex solvent manufacturing. The plant with aqueous ammonia and membrane separation had the second and third highest reductions in GWP. In addition, the lowest values for TAP, FEP, and MEP were obtained in the membrane system. With MEA for CO2 capture, the total GWP value of the plant is slightly higher than these three technologies mentioned above, and the highest HTPc, FETP, and METP can be observed in this case. TSA and PSA have the most significant environmental impacts in most categories due to higher energy requirements.

Sedation-Ventilation Interaction in Acute Hypoxemic Respiratory Failure: Secondary Analysis of the Land and Diaphragm-Protective Ventilation by Means of Assessing Respiratory Work (LANDMARK) Trial

BackgroundVentilation and sedation are used for the management of acute hypoxemic respiratory failure (AHRF), but their optimal combination to minimize the risks of ventilation is not well understood. Research questionWhat are the individual effects and interactions of inspiratory and end-expiratory pressure (PEEP), sedation, and venovenous extracorporeal membrane oxygenation (VV-ECMO) on respiratory drive, effort, and lung-distending pressure in patients with AHRF triggering the ventilator? Study designand methods: Secondary exploratory analysis of a trial of lung and diaphragm protection in AHRF. Inspiratory pressure, sedation, PEEP, and VV-ECMO were titrated while respiratory drive (airway pressure in the first 100 milliseconds, P0.1), effort (esophageal pressure swing, |ΔPes|), and lung-distending pressure (dynamic transpulmonary driving pressure, ΔPL,dyn) were recorded. Associations were evaluated using linear mixed effects regression models including pre-specified terms for potential interactions. ResultsThe study included 223 individual measurements of P0.1 and 235 individual measurements of |ΔPes| and ΔPL,dyn from 30 patients. Propofol attenuated P0.1 (–0.4 cm H2O, 95% CI –0.3, –0.1 per 10 mcg/kg/min increase), |ΔPes| (–2.5 cm H2O, 95% CI –3.4, –1.7 per 10 mcg/kg/min increase) and ΔPL,dyn (–1.6 cm H2O, 95% CI –2.3, –0.8 per 10 mcg/kg/min increase). The effect of inspiratory pressure on |ΔPes| varied depending on propofol dose: with higher propofol dose, inspiratory pressure resulted in higher ΔPL,dyn. Under VV-ECMO, patients (n=16) had significantly lower |ΔPes| (–10 cm H2O, 95% CI –17.5, –2.5) and required less sedation to reduce |ΔPes| than without VV-ECMO (n=14). InterpretationMechanical ventilation, sedation, and VV-ECMO exert interdependent effects on respiratory drive, effort, and lung-distending pressure in AHRF. Patients under VV-ECMO require less sedation to control respiratory effort.

Simulation of Olive Pomace Gasification for Hydrogen Production Using Aspen Plus: Case Study Lebanon

Biomass is a renewable energy source gaining attention for its potential to replace fossil fuels. Biomass gasification can produce hydrogen-rich gas, offering an environmentally friendly fuel for power generation, transportation, and industry. Hydrogen is a promising energy carrier due to its high energy density, low greenhouse gas emissions, and versatility. This study aims to develop a hydrogen generation plant using a dual fluidized bed gasifier, which employs steam as a gasifying agent, to convert olive pomace waste from the Lebanese olive oil industry into hydrogen. The process is simulated using Aspen Plus and Fortran coding, and it includes a drying unit, gasification unit, gas cleaning unit, steam methane reformer unit, water–gas shift reactor unit, and a pressure swing adsorption unit. The generated gas composition is verified against previous research. Sensitivity analyses are conducted to investigate the impacts of the steam-to-biomass ratio (STBR) and gasification temperature on gas composition, demonstrating a valid STBR range of 0.5 to 1 and a reasonable gasification temperature range of 700 °C to 800 °C. Further sensitivity analyses assess the impact of reformer temperature and the steam-to-carbon ratio (S/C) on the gas composition leaving the steam methane reformer.

Biogas upgrading using shaped MOF MIL-160(Al) by pressure swing adsorption process: Experimental and dynamic modelling assessment

Biogas has been introduced as a sustainable source of energy, which is considered as a promising alternative for conventional fossil fuels. Indeed, biogas requires to be upgraded from the impurities, specifically, carbon dioxide to be commercially utilized. In this study, the potential of shaped form MIL-160(Al) as a water stable Al dicarboxylate microporous MOF has been assessed concerning the biogas upgrading application. To this end, firstly, the dynamic fixed-bed adsorption of carbon dioxide and methane was investigated at 313 K and 4.0 bar. The measured breakthrough outcomes were simulated with a developed mathematical model, which the results confirmed an acceptable potential of model predictions. Afterwards, a pressure swing adsorption (PSA) process with 5-steps was designed relying on dynamic equilibrium results, and experimentally validated by a lab-scale PSA set-up for a 50:50 CO2/CH4 mixture. Finally, an industrial PSA process was designed to have a precise knowledge on the potential of MIL-160(Al) for biogas upgrading for large scale applications. The results demonstrated the purity and recovery of methane around 99 % and 63 %, respectively, which indicated the appealing capacity of this adsorbent for such a purpose.

Awake pronation with helmet CPAP in early COVID-19 ARDS patients: effects on respiratory effort and distribution of ventilation assessed by EIT.

Prone positioning with continuous positive airway pressure (CPAP) is widely used for respiratory support in awake patients with COVID-19-associated acute respiratory failure. We aimed to assess the respiratory mechanics and distribution of ventilation in COVID-19-associated ARDS treated by CPAP in awake prone position. We studied 16 awake COVID-19 patients with moderate-to-severe ARDS. The study protocol consisted of a randomized sequence of supine and prone position with imposed positive end-expiratory pressure (PEEP) of 5 and 10 cmH2O delivered by helmet CPAP. Respiratory mechanics and distribution of ventilation were assessed through esophageal pressure (PES) and electrical impedance tomography (EIT). At the end of each 20-min phase, arterial blood gas analysis was performed, and PES swing and EIT tracings were recorded for the calculation of the respiratory mechanics and regional ventilation. The patient's position had no significant effects on respiratory mechanics. EIT analysis did not detect differences among global indices of ventilation. A significant proportion of pixels in the sternal region of interest showed an increase in compliance from the supine to prone position and PaO2/FIO2 increased accordingly. The best improvement of both PaO2/FIO2 and sternal compliance was obtained in the prone position with PEEP 10 cmH2O. In the studied subjects, prone positioning during CPAP treatment raised oxygenation without improvement of "protective" ventilation or global ventilatory inhomogeneity indices. Prone positioning with higher PEEP significantly increased the compliance of sternal regions.