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A mica mineral with an idealized endmember composition $\mathrm{KA}{\mathrm{l}}_3\mathrm{S}{\mathrm{i}}_3{\mathrm{O}}_{10}(\mathrm{OH}{)}_2$. Its formula contains one tetrahedral Al and two octahedral Al per formula unit. Under ideal independent mixing on crystallographic sites, an endmember thermodynamic activity includes all mixed sites rather than only a bulk mole fraction.

The Nernst equilibrium potential is the inside-minus-outside membrane potential at which one ion species has equal electrochemical potential on both sides of a cell membrane. At uniform temperature $T$, using the same reference chemical potential on both sides, $z\ne 0$ is the signed ion charge number, $R$ the molar gas constant, $F$ the Faraday constant, and $a$ the dimensionless thermodynamic activity of that ion. For an ideal dilute chemical solution, the activity ratio becomes the concentration ratio. See Purves et al.: the forces that create membrane potentials and the Nernst equation.

The short derivation is to set the outside-to-inside electrochemical potential change from membrane transport to zero: $RT\ln (a_{\mathrm{inside}}/a_{\mathrm{outside}})+zFV=0$, and solve for $V$. An open pathway carrying only this species by passive transport then has this reversal potential. A balance of several nonzero ion electric currents does not establish this equilibrium condition for each species.

In the dilute ideal particle-count description, osmolarity is the total amount of substance of independently dissolved solute particles per volume of chemical solution: $c_{\mathrm{osm}}={\sum }_j{n}_j/V$. It includes both membrane-permeating and retained solutes; specifying a particular membrane is unnecessary to count particles. A neutral undissociated solute contributes one particle per molecule, whereas separated ions are counted individually. Common units are $\mathrm{osmol}{\mathrm{L}}^{-1}$ or $\mathrm{mOsm}{\mathrm{L}}^{-1}$, with one osmole denoting one mole of the counted particles. Osmolality uses mass of solvent instead of volume of chemical solution; the two numerical values should not be identified without the appropriate mass-to-volume conversion.^[ref]

This ideal counting definition states its scope: interactions can require a thermodynamic activity description of osmotic pressure. Tonicity asks a different question, namely how that surrounding chemical solution changes a specified biological cell's volume through its particular cell membrane.

Osmotic pressure is the excess pressure needed on a chemical solution to maintain osmotic thermodynamic equilibrium with pure solvent across a semipermeable membrane. For a nearly incompressible solvent, equality of chemical potential gives $\Pi \simeq -(RT/{\bar{V}}_w)\ln a_w$. It is an equilibrium property; an observed initial swelling rate is a different measurement.^[ref]

For a dilute ideal chemical solution of retained particles,Here $n$ is the amount of substance of independently dissolved solute particles, measured in moles; $V$ is the final volume of chemical solution, not the starting volume of pure solvent. Count the resulting ions separately if a solute dissociates; do not multiply twice if $n$ already counts them. With $c_{\mathrm{osm}}$ in $\mathrm{mol}{\mathrm{m}}^{-3}$ and $R$ in $\mathrm{J}\mathrm{mo}{\mathrm{l}}^{-1}{\mathrm{K}}^{-1}$, $RT{c}_{\mathrm{osm}}$ has units $\mathrm{J}{\mathrm{m}}^{-3}=\mathrm{Pa}$. This resembles the ideal gas law, although the particles here are dissolved in a liquid.

The assumptions are uniform temperature, a dilute ideal chemical solution, a nearly incompressible solvent, and a semipermeable membrane that retains the counted solutes while passing solvent. Association, incomplete dissociation and interactions change the relation between added material and independent particles; nonideal thermodynamic activities invalidate simple particle counting. The formula does not describe a concentrated brine merely because the apparatus contains a membrane.

A short derivation explains why particles are counted. In an ideal mixture, $a_w=x_w=n_w/(n_w+n)$, with $n_w$ the amount of substance of water. If $n\ll n_w$, then $-\ln x_w=\ln (1+n/n_w)\simeq n/n_w$ and $V\simeq n_w{\bar{V}}_w$. Substitution gives $\Pi \simeq RTn/V$. This is a dilute-limit approximation, not a claim that water molecules stop moving or that dissolved particles are a gas.

A plausible hypothesis is that broad specificity emerges from a flexible, chemically heterogeneous binding cavity containing overlapping recognition sites, coupled to an energy-driven cycle that exports many different bound molecules. The cavity recognizes combinations of physical properties rather than one unique chemical structure. Different substrates can use different subsets of contacts and different routes through the same multidrug efflux pump. This is a testable mechanism, not a claim that every pump has identical architecture.

The hypothesis has three parts. First, a large cavity contains patches providing hydrophobic contacts, aromatic contacts, hydrogen bonds and electrostatics. A chemically diverse set of substrates may share an aromatic region, a charged group or the ability to partition into the lipid bilayer. Each can make a favorable but different combination of contacts. Internal water can mediate alternative interactions rather than requiring a rigidly preorganized set of donors and acceptors. Second, local side-chain and backbone flexibility allows several cavity shapes. Third, the large-scale transport cycle changes accessibility and affinity so that occupancy of a permissive binding region can be converted into release on the far side.

These ideas have structural precedents. X-ray crystallography of AcrB identified an aromatic, multisite drug-binding region and different conformations in its three subunits, consistent with a functional rotation through binding and export states.^[ref] Further structures distinguished an access pocket and a deeper binding pocket separated by a flexible switch loop.^[ref] The observation supports overlapping recognition and staged movement; the proposed energetic and kinetic roles of each contact still require testing. AcrB is the proton-coupled inner-membrane component of a larger bacterial export assembly, rather than an ATP-powered pump by itself.

A conformational ensemble makes the hypothesis quantitative. Let the unbound pump occupy conformations $j$ with probabilities $p_j$, and let substrate $s$ have an association constant $K_{a,j,s}$ in conformation $j$. If these states equilibrate rapidly before significant transport, a simple equilibrium binding polynomial givesThe expression follows by adding the bound population contributed by each unbound state at low free substrate concentration. Distinct substrates can bind well overall even when their favorable conformations are different. For example, with $p_1=0.9$, $p_2=0.1$, $K_{a,1,s}=10^4{\mathrm{M}}^{-1}$ and $K_{a,2,s}=10^7{\mathrm{M}}^{-1}$, the apparent constant is $1.009\times 10^6{\mathrm{M}}^{-1}$. A minority state dominates the binding contribution. These are illustrative numbers, not measured pump parameters. A working pump is driven and may not equilibrate rapidly, so its transport kinetics cannot in general be reduced to this binding expression.

Permissive recognition is compatible with directional transport only when the cycle is coupled to a driving reaction. For an ATP-binding cassette transporter, ATP binding and ATP hydrolysis couple rearrangement of nucleotide-binding and transmembrane regions. For a proton-driven pump such as AcrB, proton movement down its electrochemical gradient couples to structural changes. Neither substrate affinity alone nor random thermal motion supplies sustained uphill transport. In a tightly coupled model exporting one drug molecule while importing $n$ protons, the molar cycle Gibbs free energy iswhereHere $a$ denotes dimensionless thermodynamic activity, $F$ the Faraday constant, $\psi$ electric potential, and $z_D$ the charge of the transported drug species. Forward operation requires $\Delta G_{\mathrm{cycle}}<0$; equilibrium stall has equality. This states an energetic bound under the stated coupling assumption, not a measured proton-to-drug ratio for AcrB. Mixed protonation states, coupling slippage and alternative pathways require a more detailed model.

Several predictions distinguish flexible multisite recognition from an indiscriminately sticky cavity. A mutation removing one aromatic contact should disproportionately affect a subset of substrates that use that region, while leaving others relatively intact. Altering a common gating element may impair many substrates despite preserving some equilibrium binding. Rigidifying a flexible recognition loop could narrow the range even when transport of a favored substrate survives. Different drugs may compete strongly, weakly or asymmetrically depending on overlap and pathway occupancy; failure of simple competitive kinetics would not alone prove distinct sites in a driven, multi-state system.

Test these predictions with a chemically varied panel, including transported compounds and matched nontransported controls. Measure direct transport in lipid vesicles or another defined system while controlling orientation, pump amount, membrane leak and the driving gradient. For a proton-coupled pump, vary pH and membrane potential separately where possible and include an energy-collapse control; establish that the collapse does not merely destroy membrane integrity. For an ATP-driven pump include no-ATP and hydrolysis-defective controls. Measure binding and driving-energy consumption independently, because drug-stimulated ATP hydrolysis or proton flow can be uncoupled from productive export. Growth-based resistance alone is insufficient: altered drug uptake, metabolism and expression also change survival.

Use cryo-electron microscopy or X-ray crystallography with several chemically different drugs to test different contact maps and cavity shapes, then validate those differences by targeted mutations. Confirm expression, assembly, membrane localization and protein folding for every altered pump. molecular dynamics can predict alternative entry routes and local reorganization, but force-field choices, drug protonation and limited sampling must be varied or checked; a docking score alone is not evidence of transport. single-molecule Förster resonance energy transfer or electron paramagnetic resonance can test whether different drugs stabilize different dynamic states and whether the driving reaction changes state occupancy.

Finally, membrane partitioning may explain part of the apparent range: a pump can collect chemically varied compounds that share access to the same membrane-facing route. Measure drug partitioning and free aqueous concentration, since equal added concentrations need not give equal local exposure at the pump. The strongest support would be substrate-specific contact and dynamics changes, preserved transport energetics, and direct export measurements showing that one adaptable recognition apparatus feeds a shared directional cycle.

The average electric current is the number of channels times their ion-channel open probability times the electric current carried by an open channel:Consequently the identifiable answer isTODO (missing input): The source does not supply $V_K$ or the potassium thermodynamic activities for this experiment. A unique numerical electrical conductance cannot follow from the listed electric current, count and ion-channel open probability alone. For the explicitly additional choice $V_K=-90$ mV, ${\gamma }_K=125$ pS. Taking $V_K=-100$ mV instead gives $100$ pS: both match the measured electric current. The table in question 3 describes a skeletal-muscle resting state, and cannot silently supply the conditions of this separate recording.

Rapid permeation is possible because the hydrated pore and coordinating groups of the selectivity filter provide a favorable free-energy landscape for repeated ion transit. Several ions can occupy the filter and their interactions favor onward passage, while the channel remains open for many successive transits. Selectivity need not mean that each transported ion remains tightly trapped for a long time. This is passive downhill transport; it does not consume one ATP molecule per ion crossing.

A useful organizing principle is Gibbs free energy: at specified temperature and pressure a coupled process is favorable when its total $\Delta G$ is negative. For each chemical species,The relative amounts of chemical substances determine the available Gibbs free energy, beyond counting energy in individual bonds. Nutrient oxidation and light-driven chemistry can maintain nonequilibrium compositions. ATP hydrolysis can drive biosynthesis, transport and motion of molecular motors when reactions are coupled so that their total free-energy change is favorable. Breaking an inorganic phosphate bond itself costs energy; the favorable net hydrolysis includes formation and solvation of the products and depends on their thermodynamic activities.

Redox Gibbs free energy comes from transferring electrons between donors and acceptors: $\Delta G=-nF\Delta E$. Electron transfer in respiration or photosynthesis can help establish an electrochemical gradient. For a mole of ions moving from side 1 to side 2,The concentration and electrical terms together drive transport and can power ATP synthase. ATP-driven pumps can conversely build gradients. Chemiosmosis is the coupling between this gradient and chemical synthesis, not the creation of Gibbs free energy by an enzyme.

Mechanical work and elastic storage are other forms: a motor can do $\int Fdx$ or $\int \tau d\theta$, and an approximately Hookean element stores $k{x}^2/2$. ATP-driven motors convert Gibbs free energy into motion, while externally forced reverse motion can sometimes drive chemical synthesis. A photon brings energy $h\nu$; light photon absorption initiates chemistry in photosynthesis and light-driven pumps, with some energy inevitably dissipated. Living cells use these conversions for structure, movement, homeostasis and synthesis, while releasing heat and exporting entropy. At a single uniform temperature, dissipated heat cannot be completely recycled into useful work.

Let $r=a_{\mathrm{ADP}}/a_{\mathrm{ATP}}$ and use a one-molar standard state, so the inorganic phosphate activity is approximately $a_P=0.006$. With the source's stated standard hydrolysis value,The downhill proton-transfer Gibbs free energy is $F\Delta p$ for the signed driving force $\Delta p=-0.150$ V. Ideal reversible balance of one complete turn requiresSolving yieldsAt 298.15 K the estimate is $3.39\times 10^2$. Temperature is not specified in this paragraph; the first value explicitly adopts physiological temperature rather than pretending it is supplied. The unexpectedly large ADP/ATP ratio follows from using the printed standard value $-50$ kJ/mol with the stated dilute inorganic phosphate. One must not silently replace that value by another convention or treat it as the already concentration-corrected cellular hydrolysis Gibbs free energy.

This estimate assumes ideal thermodynamic activities, consistent pH and magnesium conventions, tight coupling of ten protons to three ATP, no leak or transport overhead, and operation close to reversible balance. A working cell is not in global equilibrium. Net synthesis at this fixed driving force requires $\Delta G_{\mathrm{turn}}<0$, hence $r$ above this reversible-balance threshold; finite chemical kinetics and dissipation prevent the stoichiometry alone from determining an exact physiological ratio.

Use signed ion valence $z$ and define $V={\psi }_1-{\psi }_2$. The molar electrochemical potential in side $i$ of an ideal dilute solution isTransfer of an infinitesimal amount $dn$ from side 1 to side 2 changes the total Gibbs free energy by $({\tilde{\mu }}_2-{\tilde{\mu }}_1)dn$. At equilibrium this derivative is zero, soFor a cell with side 1 inside, this is $E_i=(RT/z_{i}F)\ln (c_{i,\mathrm{out}}/c_{i,\mathrm{in}})$. The concentrations are equilibrium free-ion concentrations, not automatically their exact initial values. For nonideal solutions the ratio must be a ratio of thermodynamic activities. The temperature and solvent must be common to both reservoirs, and an ion must actually be able to exchange for this equilibrium condition to be dynamically established.

Equal compartment volumes are unnecessary for deriving the voltage law, but help specify number conservation if concentration changes are appreciable. For equal volume $\mathcal{V}$ and a monovalent cation transfer $n$ from side 1 to 2, $c_1=c_1^0-n/\mathcal{V}$, $c_2=c_2^0+n/\mathcal{V}$. Combined with the membrane capacitance, this gives an implicit finite-reservoir equilibrium rather than treating both concentrations as externally clamped.

At $T=310.15$ K, $RT/F=26.72666$ mV. Always retain the valence sign. For the two monovalent positive ions,For calcium, $z=2$ and the specified voltage is positive:For chloride, $z=-1$ reverses the sign in the Nernst equation:These values use thermodynamic activities approximated by the given concentrations. Calcium is the free concentration relevant to its electrochemical potential, rather than total bound plus free intracellular calcium. Ratios use matching concentration units, so a ratio of millimolar values is already dimensionless. Failure to include the factor of two for calcium or the negative charge of chloride would change the answer substantially.

Usable biological free energy has several interconvertible forms. At approximately fixed temperature and pressure, chemical reactions are described by chemical potentials, ${\mu }_i={\mu }_i^{\circ }+RT\log a_i$, and ${\Delta }_{r}G={\sum }_i{\nu }_i{\mu }_i$. ATP hydrolysis, for example, has ${\Delta }_{r}G={\Delta }_r{G}^{\circ \prime }+RT\log (a_{\mathrm{ADP}}{a}_{\mathrm{Pi}}/a_{\mathrm{ATP}})$ under the specified biochemical standard-state convention. The activities and proton/ion convention matter. Breaking a bond alone costs energy; the net free-energy change includes the products, solvent and all bond changes, not a store released simply by snapping one bond.

Redox reactions provide free energy when electrons move between donors and acceptors with a favourable potential difference: $\Delta G=-nF\Delta E$. Electron-transfer chains can couple that drop to ion transport, building an electrochemical gradient. For transfer from an outer to an inner reservoir,Both concentration difference and electrical potential contribute. ATP synthase couples downhill ion flow to nucleotide free energy; driven pumps can perform the reverse conversion and maintain gradients used by transporters and excitability.

Mechanical work appears as $Fdx$ or torque times angle, and can be stored elastically, for example $\kappa x^2/2$. Molecular motors convert chemical free energy into movement or force; mechanically driven reactions can conversely reshape chemical transitions. Electrical energy can also be stored in membrane capacitance, while bulk ionic concentration gradients store additional chemical free energy. Light supplies photon energy $h\nu$, which photosynthetic machinery can convert into redox and chemical potential differences.

Coupling is essential: an overall favourable reaction can drive an unfavourable one only when their processes are linked, rather than merely present in the same cell. At fixed conditions the extracted work is bounded by the consumed free-energy decrease. Dissipation produces heat and entropy, so energy conservation does not mean all energy remains available for work. Thermal fluctuations can drive random motion, but a persistent directional cycle requires a nonequilibrium free-energy source; an equilibrium asymmetric structure alone is not a free motor.

Use the supplied $-50\mathrm{kJ}\mathrm{mo}{\mathrm{l}}^{-1}$ as a standard transformed Gibbs free energy of ATP hydrolysis, rather than replacing it with a different commonly quoted standard value. Approximate thermodynamic activities by concentrations divided by $c^{\circ }=1\mathrm{M}$, at an explicitly assumed $T=300\mathrm{K}$. The dimensionless reaction quotient isConsequentlyand the reverse synthesis cost is $g_{\mathrm{ATP}}=63.22\mathrm{kJ}\mathrm{mo}{\mathrm{l}}^{-1}$. Substituting bare millimolar numbers in this quotient without the standard state would give the wrong logarithm.

For outside-to-inside proton movement, the membrane potential is $\Delta \psi =-0.125\mathrm{V}$ and ${\mathrm{pH}}_{\mathrm{in}}-{\mathrm{pH}}_{\mathrm{out}}=0.5$, so $[H^{+}{]}_{\mathrm{in}}/[H^{+}{]}_{\mathrm{out}}=10^{-0.5}$. The molar electrochemical potential change isThus the available proton-motive force magnitude is $0.15476\mathrm{V}$, supplying $14.93\mathrm{kJ}\mathrm{mo}{\mathrm{l}}^{-1}$ per transported proton. Assuming one proton per c-subunit per revolution, three ATP per revolution and no leakage, slippage or transport overhead,The smallest integer permitting synthesis is therefore $\boxed{n_c=13}$ in this ideal budget. A ring of thirteen gives only a small driving margin; inefficiency or sustained finite output could require a larger ring. The result is an energetic lower bound and near-reversible estimate, not a unique structural determination from these data. Reasonable temperatures near $300$–$310\mathrm{K}$ leave the minimum integer thirteen. Additional membrane transport costs have been excluded explicitly.

At chemical equilibrium, ${\mu }_{\mathrm{AB}}={\mu }_{\mathrm{A}}+{\mu }_{\mathrm{B}}$. Using the number-concentration form givesHere $\Delta {\epsilon }_0$ is the reaction energy between the chosen molecular reference states. Rearranging,Define the dimensionless concentration equilibrium constant byThusThe standard concentration $c^{\circ }$ has the same units as $c_i$. It converts concentration ratios to ideal thermodynamic activities; changing it changes the numerical dimensionless $K_c$ for this dissociation, which creates an extra particle. The unnormalized quotient $c_{\mathrm{A}}{c}_{\mathrm{B}}/c_{\mathrm{AB}}$ instead has concentration units.^[ref]

The fixed nonproton thermodynamic activity ratio is $(0.1{)}^4(0.3)/(3\times 10^{-6})=10$. HenceUsing the supplied constants at $298\mathrm{K}$,At pH 7, $E\simeq 0.792\mathrm{V}$. This is the formal fixed-thermodynamic activity calculation requested; actual cerium speciation and thermodynamic activities would need to remain compatible with the chosen pH to realize it experimentally.

Pure solid CeO${}_2$ and liquid water have unit thermodynamic activity in the stated approximation, soThe power 11 and the four-electron denominator follow from the balanced conventional reaction; using the deposition reaction without reversing the potential would give inconsistent signs.

At $25^{\circ }\mathrm{C}$, $[\mathrm{O}{\mathrm{H}}^{-}]=10^{\mathrm{pH}-14}\mathrm{mol}\mathrm{d}{\mathrm{m}}^{-3}$ in the usual dilute-solution thermodynamic activity approximation. Therefore A: $10^{-2}\mathrm{M}$; B: $10^{-4}\mathrm{M}$; C: $10^{-4}\mathrm{M}$. These are initial concentrations; only C is actively buffered at its stated value.

The exponential function makes modest Gibbs free energy differences correspond to extreme equilibrium ratios. At 298 K, $RT\simeq 2.48\mathrm{kJ}\mathrm{mo}{\mathrm{l}}^{-1}$; for example,The minor equilibrium component may therefore lie below detection, or a species' required thermodynamic activity may be experimentally inaccessible. Apparently complete conversion supplies a bound on $K$, rather than an accurate finite value. Additionally, some reactions do not reach chemical equilibrium within a practicable observation time because of kinetic barriers. The thermodynamic identity still holds even when direct room-temperature determination of both sides of the equilibrium ratio fails.

Combining ${\Delta }_r{G}^{\circ }={\Delta }_r{H}^{\circ }-T{\Delta }_r{S}^{\circ }$ with the equilibrium relation givesIf reaction enthalpy and reaction entropy are approximately constant over the measurement interval, a plot of $y=\ln K$ against $x=1/T$ is straight, with slope $-{\Delta }_r{H}^{\circ }/R$ and intercept ${\Delta }_r{S}^{\circ }/R$. An exothermic reaction therefore has a positive slope. In the more general local form, the Gibbs–Helmholtz equation giveswhich is the Van't Hoff equation without assuming a constant enthalpy.

Use a dimensionless equilibrium constant built from thermodynamic activities. Measure sufficiently separated temperatures after verifying true equilibrium, and avoid phase changes or a changing chemical reaction. Temperature-dependent heat capacities cause curvature: the fitted straight-line slope then estimates an interval-dependent enthalpy. Small errors in the equilibrium measurements can produce large slope errors over a narrow $1/T$ range. The entropy intercept is particularly sensitive because $1/T=0$ requires distant extrapolation, and slope/intercept errors are correlated. A numerical line through a few points is not, by itself, evidence that all these assumptions hold.

The equilibrium molecular-acid concentration is $\boxed{[{\mathrm{H}}_2{\mathrm{N}}_2{\mathrm{O}}_2]=0.162\mathrm{mol}{\mathrm{L}}^{-1}}$. From the supplied pH convention,With only these monovalent ions appreciably present, electroneutrality requires $[\mathrm{H}{\mathrm{N}}_2{\mathrm{O}}_2^{-}]=[{\mathrm{H}}^{+}]$. Substitution in the acid dissociation constant givesThis calculation assumes ideal thermodynamic activities for the acid and its conjugate base as well as for ${\mathrm{H}}^{+}$, negligible water autoionization, negligible second dissociation, and no additional electrolyte. The acid's analytical concentration would include its dissociated fraction and be approximately $0.16220\mathrm{M}$, rather than exactly the molecular-acid concentration requested.

The standard Gibbs energy of reaction givesThe positive standard Gibbs energy of reaction means that dissociation is unfavourable when every thermodynamic activity equals one; it does not forbid partial dissociation. The corresponding $\mathrm{p}{K}_a=-{\log }_{10}{K}_a$ is about $7.21$.