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Absorption takes a chemical substance into a material's bulk, as when carbon dioxide dissolves in water. Adsorption instead concerns accumulation at a boundary. Bulk uptake and interfacial accumulation can coexist; total uptake alone does not separate their contributions. This use of absorption concerns material uptake, whereas absorbance describes attenuation of electromagnetic radiation.

A species bound at a surface. A measured orientational distribution need not imply one unique adsorption site or bonding geometry.

A contiguous sequence of segments making contacts with an adsorbing surface. The adsorption energy gained per contact competes with the loss of chain configurations. A chain can have several trains separated by loops rather than lying wholly flat.

Adsorption is accumulation of a substance at an interface. Binding a solute to a packing surface can delay its passage through a chromatography column. Ideal size-exclusion chromatography separates through SEC pore access without such binding; extra retention from adsorption requires a different interpretation.

For a gas contacting a solid, adsorption concentrates molecules at the boundary; absorption takes material into the bulk. A porous solid can have a large internal surface area: binding on pore walls is still adsorption, even though those walls lie inside the particle. Both processes can occur together. Desorption returns adsorbed material to the surrounding phase. The useful question is therefore not just how much material disappeared from the gas, but where it went and whether it returns when the pressure falls.

An adsorption site model turns this spatial distinction into counting. With twelve identical adsorption sites and three bound molecules, the surface coverage is $\theta =3/12=1/4$. Filling six gives $\theta =1/2$; filling twelve gives a complete monolayer. These are configurations illustrating the count, rather than measured arrangements or claims that all real surfaces have twelve sites.

The translational Helmholtz free energy cost of restricting a dilute ideal gas from a volume $V$ to an area $A$ at the same temperature. For identical particle number and mass,Here $\Lambda$ is the thermal de Broglie wavelength. This contribution is positive for $V/A\gg \Lambda$; a favourable binding energy must be added separately to predict net adsorption.

An adsorption site is a position or local environment at which a chemical species can be retained at a boundary. Treating all adsorption sites as identical is an assumption about their binding properties, not a definition of adsorption.

The Brunauer-Emmett-Teller multilayer adsorption model, distinguishing first-layer binding from higher layers. Suitable portions of an adsorption isotherm can estimate accessible surface area.

Condensation in a wetting confined geometry at a vapor pressure below planar-interface saturation. A concave liquid meniscus has lower equilibrium vapor pressure in the capillarity approximation. Gap size, contact angle and surface adsorption affect the actual onset.

A catalytic surface site is a location on a solid surface capable of participating in a catalytic route. The schematic notation $\ast$ denotes a vacant site; $\mathrm{A}\ast$ denotes A bound there. A minimal illustrative catalytic cycle isThe first step represents adsorption; the second combines conversion and release. Cancelling $\ast$ and $\mathrm{A}\ast$ gives $\mathrm{A}\rightleftharpoons \mathrm{B}$. The site is regenerated even though its occupancy changes during the cycle. This is an original bookkeeping model, not a measured reaction mechanism for manganese dioxide.

If the only site states are vacant and occupied by A, the site inventory obeys $n_{\ast }+n_{\mathrm{A}\ast }=n_{\mathrm{sites}}$. A blocked or inaccessible part of a particle does not contribute available catalytic surface sites merely because it contributes mass. Different surface structures can have different abilities to bind and convert reactants; equal geometric surface area need not mean equal catalytic activity.

The chromatographic mobile phase carries solutes through the apparatus. In liquid chromatography it is a liquid solvent or chemical solution.

The eluent is the supplied chromatographic mobile phase. Its composition can alter both solute solubility and competition for adsorption sites, so changing the eluent can change retention even with the same chromatographic stationary phase.

For a dilute solute distributed between two liquid regions at local chemical equilibrium, define the chromatographic partition coefficient asHere $c_m,c_s$ are concentrations expressed in the same units, $V_m,V_s$ specify accessible volume in the chromatographic mobile phase and immobilized liquid chromatographic stationary phase, respectively, $n$ is total solute amount of substance, and $f_m$ is the fraction of that amount of substance in the chromatographic mobile phase. Assume a constant chromatographic partition coefficient, rapid exchange, unchanged phases and temperature, and no chemical reaction. A chemical equilibrium population still exchanges molecules; it is not permanently divided into two sets.

The amount of substance balance proves the expression for $f_m$. Increasing either $K$ or $V_s/V_m$ reduces the mobile fraction, illustrating why a concentration ratio alone cannot determine retention. For surface adsorption, specify an adsorption storage law instead of assigning an arbitrary liquid volume to the solid.

An original discrete model makes the separation visible. In each identical cell, first establish local chemical equilibrium, then advance only the mobile fraction by one cell; let the stationary fraction wait. Repeat twelve times, without any additional spreading. With $V_s=V_m$, stipulated chromatographic partition coefficients $K_A=1/3$ and $K_B=3$ give $f_A=3/4$ and $f_B=1/4$. Each cycle contributes mean displacement $f_m$ cells, so the mean positions after twelve cycles are nine cells and three cells. Redistribution itself broadens each band: the cell positions have a binomial distribution with parameters $12,f_m$. These dimensionless chosen values illustrate transport, not measurements of any particular substances.

The chromatographic stationary phase remains in place during separation. A porous packing in size-exclusion chromatography supplies internal liquid regions with size-dependent accessibility; ideal separation requires no adsorption of the solute to the packing.

A chromatographic stationary phase may instead expose a solid surface for adsorption, or retain an immobilized liquid into which solutes partition. In ordinary silica gel thin-layer chromatography, interactions with the surface delay migration. This mechanism differs from ideal SEC pore access.

Chromatography separates components of a mixture through different migration rates in contact with a chromatographic stationary phase while a chromatographic mobile phase transports them. Liquid chromatography describes the physical state of the transporting phase; size-exclusion chromatography describes a separation mechanism. Classification by phase and classification by mechanism answer different questions. In ideal size-exclusion chromatography, differential access to liquid-filled pores replaces binding as the source of differential migration.

In many other forms of chromatography, a solute repeatedly leaves the chromatographic mobile phase and returns to it. Reversible adsorption holds it at a surface; partition distributes it between the chromatographic mobile phase and an immobilized liquid chromatographic stationary phase. Spending more time stationary means less progress with the moving fluid. Two initially overlapping components can therefore emerge as separate bands without either being permanently trapped. Chromatography is useful both for comparing a sample with reference substances and for collecting separated components; a visible band need not contain just one substance.

Relative retention belongs to the sample together with the chosen chromatographic stationary phase, chromatographic mobile phase, eluent composition, and temperature. Changing these conditions can change the separation order. Chemical polarity helps explain interactions in some systems but is not a universal ranking rule. In thin-layer chromatography, a spot's TLC retardation factor is consequently conditional evidence about identity, rather than a fixed identifier intrinsic to a molecule.

Fine-grained hydrous silicate minerals with structures and surface properties important to adsorption and water-rock interaction.

Desorption releases material previously retained at a boundary. At chemical equilibrium, adsorption and desorption can both continue while their mean rates balance.

An emission-limited thermionic current is set by the rate at which the heated surface supplies electrons, with nearly complete collection. At fixed temperature, increasing the attracting electric potential difference then produces an approximate collection plateau. That plateau is the useful regime for fitting the Richardson-Dushman law, provided the electric field has not significantly lowered the surface barrier.

The emitting surface still matters in this regime. Adsorption changes the work function; different crystal faces can have different barriers. Heating may desorb contaminants or change a coating, so repeated measurements at the same temperature need not agree unless the surface preparation is controlled. For fixed $A,T$, a barrier change $\Delta W$ multiplies $J$ by $e^{-\Delta W/(k_{B}T)}$. In the chosen model at $1000\mathrm{K}$, raising the barrier by $0.10\mathrm{eV}$ reduces $J$ to about 0.313 of its previous value.

In an idealized rigid-globe weighing, subtract the evacuated assembly's mass from the filled assembly's mass, then divide by the internal volume. Establish the filled sample's pressure and temperature before comparing gases. The subtraction removes the container's large contribution, making a small gas contribution accessible. A real measurement also needs corrections or bounds for residual gas, adsorption, leaks, changing vessel volume and external buoyancy. The Rayleigh-Ramsay argon density experiment shows why preparation-route comparisons add information beyond repeated weighings of one sample.

A porous gel changes the electrophoretic mobility of charged synthetic polymers through confinement, deformation and pore-to-pore dynamics. Free-draining charge and friction can both grow proportionally to chain length, leaving free-solution mobility nearly length independent; matrix obstruction adds size sensitivity. reptation supplies one weak-field long-chain regime, not a universal calibration. Matrix concentration, effective charge, solvent conditions, conformation, topology, adsorption, electro-osmotic drift and heating can all alter migration. Size standards should match the relevant chemistry and operating regime.

In heterogeneous catalysis, the catalyst and reactants occupy different thermodynamic phases; a solid surface can furnish the catalytic route.

For example, specify dissolved hydrogen peroxide as the reactant, water as the solvent, and solid manganese dioxide as the catalyst. The solid and liquid chemical solution are separate thermodynamic phases. A dispersion that looks thoroughly mixed still contains those separate phases; mixing distributes contact, rather than making the solid molecularly dissolved. The manganese dioxide peroxide contact demonstration makes the arrival of the liquid at the solid tangible.

A useful surface-route picture is approach from the liquid, adsorption at a catalytic surface site, conversion through surface-bound reaction intermediates, and release of reaction products. ^[ref] This sequence organizes possible roles; it is not a verified sequence of elementary reactions for every catalyst, or for the particular manganese dioxide demonstration. The net chemical equation supplies neither the binding geometry nor the identity of the working catalytic surface site.

This contact requirement makes surface area and diffusion practically important. More exposed solid can provide more catalytic surface sites, whereas diffusion through the surrounding liquid can limit their supply of reactants. Changing stirring or particle size can therefore change the observed reaction rate without identifying the microscopic rate constant. A recoverable solid is attractive for reuse, but separation alone does not establish retained activity: compare with catalyst deactivation.