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Methane adsorption on various metal-organic frameworks and determination of the average adsorption heats at supercritical temperatures and pressures
Adsorption of methane on three samples of metal-organic framework structures (MOF), which contain copper, aluminum or zinc atoms, was measured at temperatures ranging from 303 to 333 K and pressures up to 40 MPa using a precise volumetric-gravimetric unit. The determined values of adsorption volumes and characteristic energies served to evaluate the average heats of adsorption, which were compared to the average isosteric heats of adsorption.
Review of the potential and challenges of MOF-based adsorption heat pumps for sustainable cooling and heating in the buildings
Heat pumps are regarded as the most suitable means to meet the future demand of heating and cooling in the building, as they require small input of electrical energy and output high thermal energy. Vapor compression heat pump (VCHP) and transcritical-CO 2 heat pump are the two major heat pump technologies currently dominating the market. However, VCHP system suffers from its fugitive emission of hydrofluorocarbon (HFC) refrigerants, and transcritical-CO 2 system requires high operating pressure (typically 9–13 MPa). For low-to-medium temperature heating and cooling applications thermally driven adsorption heat pump (AHP) provides a better alternative to VCHP and transcritical-CO 2 system as AHP uses natural refrigerants and operates at a much lower pressure. But currently available AHP technology has the limitation of low coefficient of performance (COP). Advances in synthesizing metal-organic frameworks (MOF) with high gas adsorption capacity have created an opportunity to address the problem of low COP of current AHP technology. Here, this article reviews the progress made in the past decade in utilizing MOF and conventional adsorbents with different working fluids in AHP technology and compares their performance. The article also summarizes the key challenges for the MOF-based AHP technology and provides the authors’ perspective to address these challenges.
Experimentally Measured Thermal Masses of Adsorption Heat Exchangers
The thermal masses of components influence the performance of many adsorption heat pump systems. However, typically when experimental adsorption systems are reported, data on thermal mass are missing or incomplete. This work provides original measurements of the thermal masses for experimental sorption heat exchanger hardware. Much of this hardware was previously reported in the literature, but without detailed thermal mass data. The data reported in this work are the first values reported in the literature to thoroughly account for all thermal masses, including heat transfer fluid. The impact of thermal mass on system performance is also discussed, with detailed calculation left for future work. The degree to which heat transfer fluid contributes to overall effective thermal mass is also discussed, with detailed calculation left for future work. This work provides a framework for future reporting of experimental thermal masses. The utilization of this framework will enrich the data available for model validation and provide a more thorough accounting of adsorption heat pumps.
Screening of working pairs for adsorption heat pumps based on thermodynamic and transport characteristics
Not Available
Adsorption Heat Pump Development At JPL
In simple sorption refrigeration system, low pressure gases are physically adsorbed onto or chemically absorbed into various solids, typically near ambient temperatures or above.
Bounding Limitations in the Practical Design of Adsorption Heat Pump Water Heaters
The boundary temperatures for any sorption-based technology can be estimated on the basis of Trouton s hypothesis that isosteres, extrapolated to infinite pressure (or analogously to infinite temperature) meet at a single point. In this paper we discuss the consequences of this hypothesis for many sorption devices that are thermally operated, suitable for exploiting renewable energy resources, or making better use of high or low level thermal energy. Trouton s hypothesis is independent of the working fluids making it particularly useful to both liquid-vapor and solid-vapor systems. We exemplify the use of the derived boundary temperatures derived from Trouton s hypothesis to important processes such as ice making, space cooling in hot climates, deep freezing, and residential hot water production. The boundary temperatures help determine which sorption or solar heating technology may be better suited to serve the given application, or whether it is beyond the scope of sorption systems.
Differential Heat of Adsorption and Isosteres
Heat of adsorption is a basic thermodynamic property extensively used not only for understanding thermal effects and heat management in industrial gas storage and separation processes but also for development and validation of adsorption models and materials force fields. Despite a long history of theoretical studies and a vast experimental literature, controversies often arise in the thermodynamic analysis of heat effects due to various assumptions used to describe gas adsorption and inconsistencies between direct calorimetric measurements and isosteric heat obtained from various adsorption isotherms. Here we present a rigorous theoretical procedure for predicting isosteric heat without any assumption about the geometry of porous adsorbents or operating conditions. Quantitative relations between the differential heat and various isosteres have been established with the grand-canonical Monte Carlo simulation for gas adsorption in amorphous as well as crystalline porous materials. The inconsistencies and practical issues with conventional methods for the analysis of the heat effect have been clarified in the context of the exact results for model systems. Via the resolution of a number of controversies about heat analysis, we hope that the new theoretical procedure will be adopted for both fundamental research and industrial applications of gas adsorption processes.
Heats of adsorption of carbon dioxide on silver
Heats of adsorption of carbon dioxide on silver /I/ oxide and copper /II/ oxide by gas chromatography
Estimation of isosteric heat of adsorption from generalized Langmuir isotherm
Simulation and design of adsorptive separation units demand accurate estimation of thermodynamic properties. Isosteric heat of adsorption as calculated from generalized Langmuir (gL) isotherm coupled with Clausius-Clapeyron expression for pure component and mixed-gas adsorption equilibria is presented in this work. The estimated isosteric heat of adsorption as functions of surface loading and composition is validated against the experimental data for various adsorption systems. Furthermore, the gL results are compared against classical Langmuir (cL) and Toth isotherm for pure components and with Ideal Adsorbed Solution Theory (IAST) for mixed-gas adsorption equilibria. Furthermore, the comparison highlights that gL outperforms cL and Toth for pure component adsorption and IAST for mixed-gas adsorption, and gL reliably captures the loading dependence and the composition dependence for isosteric heat of adsorption.
Adsorption system heat exchanger
In one aspect, a heat exchanger layer for an adsorption bed heat exchanger assembly is provided. The heat exchanger layer includes at least one fluid tube configured to supply a heat transfer fluid, a sorbent containment structure having a plurality of compartments, and a sorbent disposed within the plurality of compartments.
New Carbon-Based Porous Materials with Increased Heats of Adsorption for Hydrogen Storage
Hydrogen fuel cell vehicles are a promising alternative to internal combustion engines that burn gasoline. A significant challenge in developing fuel cell vehicles is to store enough hydrogen on-board to allow the same driving range as current vehicles. One option for storing hydrogen on vehicles is to use tanks filled with porous materials that act as “sponges” to take up large quantities of hydrogen without the need for extremely high pressures. The materials must meet many requirements to make this possible. This project aimed to develop two related classes of porous materials to meet these requirements. All materials were synthesized from molecular constituents in a building-block approach, which allows for the creation of an incredibly wide variety of materials in a tailorable fashion. The materials have extremely high surface areas, to provide many locations for hydrogen to adsorb. In addition, they were designed to contain cations that create large electric fields to bind hydrogen strongly but not too strongly. Molecular modeling played a key role as a guide to experiment throughout the project. A major accomplishment of the project was the development of a material with record hydrogen uptake at cryogenic temperatures. Although the ultimate goal was materials that adsorb large quantities of hydrogen at room temperature, this achievement at cryogenic temperatures is an important step in the right direction. In addition, there is significant interest in applications at these temperatures. The hydrogen uptake, measured independently at NREL was 8.0 wt %. This is, to the best of our knowledge, the highest validated excess hydrogen uptake reported to date at 77 K. This material was originally sketched on paper based on a hypothesis that extended framework struts would yield materials with excellent hydrogen storage properties. However, before starting the synthesis, we used molecular modeling to assess the performance of the material for hydrogen uptake. Only after modeling suggested record-breaking hydrogen uptake at 77 K did we proceed to synthesize, characterize, and test the material, ultimately yielding experimental results that agreed closely with predictions that were made before the material was synthesized. We also synthesized, characterized, and computationally simulated the behavior of two new materials displaying the highest experimental Brunauer$-$Emmett$-$Teller (BET) surface areas of any porous materials reported to date (~7000 m 2 /g). Key to evacuating the initially solvent-filled materials without pore collapse, and thereby accessing the ultrahigh areas, was the use of a supercritical CO 2 activation technique developed by our team. In our efforts to increase the hydrogen binding energy, we developed the first examples of “zwitterionic” metal-organic frameworks (MOFs). The two structures feature zwitterionic characteristics arising from N-heterocyclic azolium groups in the linkers and negatively charged Zn 2 (CO 2 ) 5 nodes. These groups interact strongly with the H 2 quadrupole. High initial isosteric heats of adsorption for hydrogen were measured at low H 2 loading. Simulations were used to determine the H 2 binding sites, and results were compared with inelastic neutron scattering. In addition to MOFs, the project produced a variety of related materials known as porous organic frameworks (POFs), including robust catechol-functionalized POFs with tunable porosities and degrees of functionalization. Post-synthesis metalation was readily carried out with a wide range of metal precursors (Cu II , Mg II , and Mn II salts and complexes), resulting in metalated POFs with enhanced heats of hydrogen adsorption compared to the starting nonmetalated materials. Isosteric heats of adsorption as high as 9.6 kJ/mol were observed, compared to typical values around 5 kJ/mol in unfunctionalized MOFs and POFs. Modeling played an important role throughout the project. For example, we used molecular simulations to determine that the optimal isosteric heat of adsorption (Q st ) for maximum hydrogen delivery using MOFs is approximately 20 kJ/mol. If the heat of adsorption is too low, little hydrogen is adsorbed. If the heat of adsorption is too high, it is difficult to recover the hydrogen at the desorption pressure. The results supported the major premise of this project that increasing Q st for MOFs with large surface areas is required to attain current hydrogen storage targets in terms of deliverable capacity.
A Simple Bond-Additivity Model Explains Large Decreases in Heats of Adsorption in Solvents Versus Gas Phase: A Case Study with Phenol on Pt(111) in Water
Previously, we reported the low-coverage heat of adsorption of phenol on Pt(111) facets of a Pt wire in aqueous phase to be approximately 21 kJ/mol (relative to aqueous phenol) on the basis of measurements of the adsorption equilibrium constant. This is much smaller than the heat we reported for gas-phase phenol adsorption at this same low coverage on single-crystal Pt(111) under ultrahigh vacuum (200 kJ/mol) on the basis of adsorption calorimetry measurements. Here we quantitatively analyze the individual contributions that give rise to this 179 kJ/mol difference using a simple pairwise bond-additivity model, taking advantage of experimental data from the literature to estimate the bond energies. The dominant contribution to the lowering in heat when phenol is adsorbed in water is the energy cost to break the strong bond of liquid water to Pt(111) (~116 kJ per mole of phenol area). The water–phenol bonding is lost on one face of the phenol, and this costs ~50 kJ/mol, but this is nearly compensated by the new water–water bonding (~53 kJ/mol of phenol area). The results indicate that the intrinsic bond energy between phenol and Pt(111) is not very different in the gas versus the aqueous phase, provided one takes into consideration the expectation that water forces phenol into islands of high local coverage even at low average coverage (for the same reason that phenol has limited solubility in water). Furthermore, this explains the lack of a strong coverage dependence in the heat of adsorption when it is measured in aqueous phase, whereas it decreases by ~57 kJ/mol with coverage when it is measured in gas phase. This bond-additivity analysis presented here can be easily generalized to other adsorbates, surfaces, and solvents. It clarifies why catalysis with molecules such as phenol which have very strong bonding to Pt-group metals can proceed rapidly at room temperature in liquid solvents such as water but would never proceed in the gas phase at room temperature due to irreversible site poisoning.
Low-coverage heats of adsorption. iii - alkali metal ions on tungsten, atom-metal interaction theory
Heats of adsorption of sodium, rubidium, and cesium ions on tungsten substrate
Low-coverage heat of adsorption. ii - alkali metal atoms on tungsten, lennard-jones atom- atom interaction theory
Heat of adsorption for sodium, rubidium, and cesium on tungsten substrate - chemisorption
Lunar fines and terrestrial rock powders - Relative surface areas and heats of adsorption
Apollo 11 lunar fines and ground terrestrial mafic rock powders effective surface areas and heats of adsorption, using Brunauer-Emmett-Teller Kr adsorption method
Low-coverage heat of adsorption. i - alkali metal atoms on tungsten, atom-metal inter- action theories
Experimental values of heat of adsorption for sodium, rubidium, and cesium on tungsten substrate
Interaction energy and isosteric heat of adsorption between hydrogen and magnesium diboride
Hydrogen storage materials form a crucial research topic for future energy utilization employing hydrogen and among those of interest magnesium diboride (MgB 2 ) has shown its prevalence. In this study, a first-principles analytical adsorption model of one hydrogen molecule in the vicinity of various magnesium diboride crystal surfaces was developed in order to obtain surface thermodynamic properties as a function of molecular and lattice properties. Henry's law constant (K H ) and isosteric heat of adsorption (ΔH ads ) indicators of the affinity between a gaseous molecule and a solid surface are thus calculated. The results in this paper not only address questions pertaining to the first stage of hydrogen storage processes but also advance the understanding of physisorption thermodynamics of a neutral molecule (H 2 ) coming in contact with a layered metallic-like surface (MgB 2 ). Although the model is built from a framework of classical calculations, quantum effects are incorporated as the fractional charge of the ions on the free surfaces, which is essential for the calculation of analytic thermodynamic values that approximate calculations from other methods. To benchmark our theoretical models, periodic density functional calculations were performed to determine the interactions between H 2 and different MgB 2 surfaces from first-principles. By considering both the top and sublayers of MgB 2 in calculating interaction energy, we have analytically and computationally calculated the interaction energies of H 2 molecules and MgB 2 's terminated planes, and witnessed the strong dependence of interaction energies on surface charges. We have also observed a dipole flipping phenomenon which explains the discontinuity seen in the interaction energy graph of Mg(0001). Both analytical and computational results showed heat of adsorption at zero coverage varying at a very low range (<7 kJ mol -1 ).